march 08, 2016 p.o. box 13087 - san antonio express-news · 08/03/2016 · encana oil & gas...

Encana Oil & Gas (USA) Inc., by its authorized agent, Encana Services Company Ltd. Republic Plaza 370 17th Street Suite 1700 Denver CO 80202 USA 303.623.2300 encana.com

March 08, 2016 Texas Commission on Environmental Quality via STEERS Air Permits Initial Review Team (APIRT) MC-161 P.O. Box 13087 Austin, TX 78711-3087 Re: Non-rule Standard Permit Registration Revision

Encana Oil & Gas (USA) Inc. Patton Trust South Production Facility – Karnes County, Texas Customer Reference Number: CN601451149 Regulated Entity Number: RN106397284 Registration Number: 125964

APIRT: Encana Oil & Gas (USA) Inc. (“Encana”) is submitting the enclosed standard permit application to register the proposed revisions for the Patton Trust South Production Facility under 30 TAC §116.602 – NON RULE 2012-NOV-08. This registration includes updates to: the FIN designations of existing facilities, gas stream compositions, and daily gas throughput, and the addition of insignificant sources, a vapor recovery unit, and two operating scenarios. If you have any questions or require additional information, please contact me at 720.876.5731 or by email at [email protected]. Sincerely, Encana Oil & Gas (USA) Inc.

Jeanette Liang Air Quality Specialist Enclosures cc: Mr. George Ortiz, Air Section Manager, TCEQ Region 13

NON-RULE STANDARD PERMIT REGISTRATION REVISION FOR

ENCANA OIL & GAS (USA) INC. PATTON TRUST SOUTH PRODUCTION FACILITY

KARNES COUNTY, TEXAS CUSTOMER REFERENCE NO. CN601451149

REGULATED ENTITY NO. RN106397284 REGISTRATION NO. 125964

Submitted To:

TEXAS COMMISSION ON ENVIRONMENTAL QUALITY AIR PERMITS INITIAL REVIEW TEAM

MC-161 P.O. BOX 13087

AUSTIN, TEXAS 78711-3087

Submitted By:

ENCANA OIL & GAS (USA) INC. 370 17TH ST, SUITE 1700

DENVER, CO 80202

MARCH 2016

NON-RULE STANDARD PERMIT REGISTRATION REVISION

PATTON TRUST SOUTH PRODUCTION FACILITY

ENCANA OIL & GAS (USA) INC. I

CONTENTS

1.0 INTRODUCTION .................................................................................................................. 2

1.1 Project Overview ........................................................................................................ 2

1.2 Site Location .............................................................................................................. 3

2.0 SITE PROCESS INFORMATION ........................................................................................ 5

2.1 Process Description ................................................................................................... 5

2.2 Emission Controls ...................................................................................................... 6

2.3 Planned Maintenance, Startup, and Shutdown Activities .......................................... 7

2.4 Alternate Operating Scenarios (AOS) Associated With Planned MSS Activities ....... 8

3.0 EMISSIONS DATA ............................................................................................................. 10

3.1 Emission Sources .................................................................................................... 10

3.2 Analyses .................................................................................................................. 11

3.3 Modeled Analyses ................................................................................................... 12

4.0 IMPACTS EVALUATION ................................................................................................... 15

4.1 Generic Modeling Tables ......................................................................................... 15

4.2 Dispersion Modeling ................................................................................................ 15

4.3 Alternate NO2 Background Concentration Justification ........................................... 15

5.0 REQUIREMENTS AND APPLICABILITY .......................................................................... 19

5.1 General Requirements and Applicability .................................................................. 19

5.2 Specific Requirements of 30 TAC §116.602 – NON RULE 2012-NOV-08 ............. 24

5.3 Federal Requirements and Applicability .................................................................. 28

APPENDICES

Appendix A Emissions Calculations

Appendix B Impacts Analyses

Appendix C Gas and Liquid Analyses

Appendix D Graphics: Area Map, Process Flow Diagram

Appendix E Supporting Documents



ENCANA OIL & GAS (USA) INC. 1

1.0 INTRODUCTION




1.0 INTRODUCTION

1.1 PROJECT OVERVIEW

Encana Oil & Gas (USA) Inc. (“Encana”) owns and operates the Patton Trust South Production Facility in Karnes County, Texas. The site is an existing oil and gas production facility that consists of separators, heater treaters, line heaters, compressor engines, cooler engines, vapor recovery units (“VRU”), oil/condensate and produced water storage tanks, a process flare, a utility flare, vapor recovery towers (“VRT”), a glycol unit, lease automatic custody transfer (“LACT”) units, and oil/condensate and produced water loadouts. The purpose of this submittal is to authorize the revisions listed below to the current authorization (Permit No. 125964) under 30 TAC §116.602 – NON RULE 2012-NOV-08.

Site Updates:

Addition of the following emission sources: One (1) VRU Compressor Engine – Cummins G8.3 (FIN/EPN: ENGVRU-04); Up to 12 catalytic heaters grouped under FIN/EPN: CAT-HTR; One (1) oil/condensate 1,000 bbl oil/condensate tank (FIN: OILTK-23).

The following updates are represented in this submittal, which are representative of the site’s current processes:

Revise the following FIN designations:

Summary of FIN Designation Revisions Previous FIN New/Revised FIN LPDS-GAS PROD-GAS

HT-GAS PROD-GAS

IPCOMP-MSS PROD-GAS

Update ProMax model to consolidate gas stream compositions of previous FINs “LPDS-

GAS” and “HT-GAS” into one composition; Increase the annual average daily produced gas throughput from 27 MMscf/day to 33

MMscf/day; Decrease the maximum H2S concentration at the site from 188 ppmv to 174 ppmv; Update the fugitive component counts, process description, and process flow diagram.




The total potential to emit (“PTE”) site-wide volatile organic compound (“VOC”), nitrogen oxides (“NOx”) and carbon monoxide (“CO”) emissions are expected to exceed the 100 ton per year threshold for major source; therefore, Encana is required to obtain a federal operating permit (“FOP”) pursuant to 30 TAC Chapter 122. Encana is submitting a Title V application concurrently with this submittal. The documentation included in this submittal demonstrates compliance with all applicable state and federal standards.

1.2 SITE LOCATION

The Patton Trust South Production Facility is located in Karnes County, approximately 4.1 miles east of Karnes City, Texas. A scaled area map that shows the location of the Patton Trust South Production Facility and the 0.25-mile radius is included in Appendix D. The distance to the nearest property line and receptor is greater than 50 feet.

- Latitude / Longitude: 28.893137 / -97.834560




2.0 SITE PROCESS INFORMATION




2.0 SITE PROCESS INFORMATION

2.1 PROCESS DESCRIPTION

The Patton Trust South Production Facility receives a three-phase stream from onsite (within 0.25 mile) and offsite production wells via pipeline to separators. Liquids from the separators are sent to heater treaters (FIN: HTR-01 through HTR-04, HTR-06 through HTR-08) which heat the stream enabling further separation of gas from the oil/condensate and produced water. The produced water from the inlet separators and the heater treaters is routed to a heater treater (FIN: HTR-05) for further separation of oil/condensate and then to the produced water storage tanks (FIN: PWTK-01 to PWTK-05). The oil/condensate from the heater treaters is routed to the VRTs for further stabilization and then to the oil/condensate storage tanks (FIN: OILTK-01 to OILTK-22). The tanks (FIN: OILTK-01 through OILTK-23; PWTK-01 through PWTK-05) are controlled by a vapor recovery unit (“VRU”), driven by a natural gas engine (FIN: ENGVRU-04). A small amount of liquids off the compressors and various process equipment are routed to the drip VRT for stabilization and then to the oil/condensate storage tanks (FIN: OILTK-21, OILTK-22). The oil/condensate from the oil/condensate storage tanks (FIN: OILTK-01 through OILTK-22) passes through the LACT units to another oil/condensate tank (FIN: OILTK-23) and is then removed from the tanks by pipeline or loaded into trucks (FIN: LOAD) for up to 2,500 loadouts per year. Produced water is loaded into trucks (FIN: LOAD) for transport offsite. Flashed gas off the VRTs (FIN: VRT-GAS, DRIPVRT-GAS) is hard-piped to and compressed by VRU compressors, driven by natural gas-powered engines (FIN: ENGVRU-01 through ENGVRU-03). Flashed gas off the VRTs (FIN: VRT-GAS, DRIPVRT-GAS) may also be routed to the process flare (FIN/EPN: FLR-02). Flashed gas off of the heater treaters and the low pressure drip scrubber (FIN: PROD-GAS), and the VRU compressors is compressed by the flash gas compressors, driven by natural gas-powered engines (FIN: ENG-04 through ENG-06). Flashed gas off of the heater treaters and the low pressure drip scrubber (FIN: PROD-GAS) may also be routed to the utility flare (FIN/EPN: FLR-01). Gas off the inlet separators (FIN: PROD-GAS) is either sent directly to the utility flare (FIN/EPN: FLR-01), gas sweetening unit, or compressed by the IP compressors, driven by natural gas-powered engines (FIN: ENG-01 through ENG-03). Gas from the IP and flash compressors is routed to coolers, driven by natural gas-powered engines (FIN: ENG-07, ENG-08). The liquids off the cooler scrubber that are routed through a line heater (FIN: HTR-10) and then to a low pressure drip scrubber, will be sent offsite via pipeline to the Patton Trust North Production Facility. Following the cooler scrubber, the produced gas is treated in a gas sweetening unit (a closed system with no associated emissions) and a glycol unit (FIN: DEHY-01, HTR-09). A fraction of the sweetened gas is routed to a fuel conditioning skid (no associated emissions) and used on site for fuel. The remaining gas is sent to the sales pipeline or used for gas lift.




Other sources of emissions include piping fugitive emissions (FIN: FUG), catalytic heaters (FIN: CAT-HTR) used in various operations at the site, and emissions from planned MSS activities, which are detailed in Section 2.3. See Appendix D for a simplified process flow diagram.

2.2 EMISSION CONTROLS

Vapors from the oil/condensate and produced water storage tanks (FIN: OILTK-01 through OILTK-23, PWTK-01 through PWTK-05) are routed to the process flare (FIN/EPN: FLR-02) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. Vapors from the storage tanks (FIN: PWTK-01 to PWTK-05, OILTK-01 through OILTK-23) are routed to a VRU compressor, driven by a natural gas-powered engine (FIN: ENGVRU-04) for 98% capture/control efficiency with the vent gas being routed back to the process flare (FIN/EPN: FLR-02) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. The VRU at the Patton Trust South Production Facility is a natural gas engine-driven mechanical VRU (mVRU) and operates in conjunction with an electric blower system. Encana maintains records of the following design requirements for claiming 98% control (Table 8 of 30 TAC §116.602 NON RULE 2012-NOV-08):

The VRUs use a pressure sensing device that provides constant pressure readings to maintain a pressure inside the storage tanks below the thief hatches opening pressure.

Properly designed bypass system: when the VRUs are taken offline for repairs or maintenance, the electric blowers routed vapors to the process flare for control.

Adequate compressor selection: an estimated gas production and number of flash vessels were provided to the VRU vendor to determine adequately sized compressors for use at the site.

Oil/condensate and produced water loading vapors (FIN: LOAD) are routed to the process flare (FIN/EPN: FLR-02) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. The tank trucks are not leak tested based on EPA standards (NSPS XX); therefore, a vapor capture/collection efficiency of 70% was used in the emission calculations. Flashed gas off the VRTs (FIN: VRT-GAS, DRIPVRT-GAS) may be routed to the process flare (FIN/EPN: FLR-02) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. Produced gas (FIN: PROD-GAS) may be routed to the utility flare (FIN/EPN: FLR-01) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. Flash tank vapors from the glycol unit flash tank (FIN: DEHY-01) are premixed with the primary fuel gas and controlled by the unit reboiler for 99% control of VOC and H2S (EPN: DEHY-01) or are routed to the process flare (FIN/EPN: FLR-02) for 99% (C3) / 98% (C4+) control of VOC and 98% control of H2S. Emissions from the glycol unit flash tank are conservatively calculated




assuming that flash tank vapors are routed to the control device with the lowest destruction efficiency (process flare) for the entire year. Condenser vapors from the glycol unit condenser (FIN: DEHY-01) are premixed with the primary fuel gas and controlled by the unit reboiler for 99% control of VOC and H2S (EPN: DEHY-01) or are routed to the unit glow plug for 98% control of VOC and H2S. Emissions from the glycol condenser are conservatively calculated assuming that condenser vapors are routed to the control device with the lowest destruction efficiency (glow plug) for the entire year. Leak Detection and Repair Program (LDAR): Emissions from fugitive components in gas and liquid service have the uncontrolled potential to emit greater than 25 tpy VOC and are, therefore, subject to a LDAR program as specified in Table 9 in paragraph (m) of the non-rule standard permit. Encana has implemented the applicable LDAR Program from Table 9 of this standard permit. Emission control efficiencies associated with this LDAR program have been applied to the fugitive emissions (FIN: FUG) included in this submittal.

2.3 PLANNED MAINTENANCE, STARTUP, AND SHUTDOWN ACTIVITIES

This permit registration includes estimated emission rates from additional planned MSS activities at this site. Annual frequencies of planned MSS activities represented in this submittal are intended to be potential-to-emit/worst case scenarios. The actual annual frequency of each activity necessary to maintain good working order of facilities/equipment may vary. Emission calculations from the following planned MSS activities are included in this submittal:

Degassing and cleaning the heater/boiler (FIN/EPN: MSS-HTRDEG, MSS-HTRCLN) Pig launcher degassing (FIN/EPN: MSS-PIG) Cleaning oil/condensate and produced water storage tanks (FIN/EPN: MSS-TNKCLN) Compressors Blowdowns/Startups (FIN/EPN: COMP-MSS/FLR-01)




2.4 ALTERNATE OPERATING SCENARIOS (AOS) ASSOCIATED WITH PLANNED

MSS ACTIVITIES

During IP compressor engine (FIN: ENG-01 through ENG-03) downtime for routine maintenance, produced gas that cannot be compressed is routed to the utility flare for control (FIN/EPN: PROD-GAS/FLR-01). During flash gas compressor engine (FIN: ENG-04 through ENG-06) downtime for routine maintenance, produced gas is routed to the utility flare for control (FIN/EPN: PROD-GAS/FLR-01) and flash gas off the VRTs is routed to the process flare for control (FIN/EPN: VRT-GAS, DRIPVRT-GAS/FLR-02). During VRU compressor engine (FIN: ENGVRU-01 through ENGVRU-04) downtime for routine maintenance, flash gas off the VRTs and the storage tanks is routed to the process flare for control (FIN/EPN: VRT-GAS, DRIPVRT-GAS, PWTK-01 to PWTK-05, OILTK-21, OILTK-22/FLR-02).




3.0 EMISSIONS DATA




3.0 EMISSIONS DATA

3.1 EMISSION SOURCES

Emission sources for the Patton Trust South Production Facility are shown in this section. Emission rates are based on an annual average daily produced throughput of 33 MMscf, 9,000 bbl oil/condensate, and 3,500 bbl produced water. Emissions calculations for these sources under current and future operations are in Appendix A. It is requested that the worst-case total emissions from each operating scenario be used as the representative emissions in the authorization for this site as they are the most conservative.

Summary of Emission Sources and Calculation Methods

Source FIN EPN Calculation Method

Fugitive Emissions FUG FUG TCEQ Fugitive Guidance –

O&G Operations

IP Compressor Engines Caterpillar G3516B

Waukesha L7044GSI

Caterpillar G3516B

ENG-01

ENG-02

ENG-03

ENG-01

ENG-02

ENG-03

EPA AP-42, Vendor data, and

Material Balance for SO2

Flash Gas Compressor Engines Caterpillar G3516B

Caterpillar G3516B

Waukesha L7044GSI

ENG-04

ENG-05

ENG-06

ENG-04

ENG-05

ENG-06

Cooler Engines Arrow VRG330

Arrow VRG330

ENG-07

ENG-08

ENG-07

ENG-08

VRU Compressor Engines Cummins G855 Cummins G855

GM Vortec 5.7L

Cummins G8.3

ENGVRU-01

ENGVRU-02

ENGVRU-03

ENGVRU-04

ENGVRU-01

ENGVRU-02

ENGVRU-03

ENGVRU-04

0.5 MMBtu/hr Heater Treaters

HTR-01

through

HTR-05

HTR-01

through

HTR-05

EPA AP-42 and Material

Balance for SO2

1.5 MMBtu/hr Heater Treaters

HTR-06

through

HTR-08

HTR-06

through

HTR-08

0.75 MMBtu/hr Glycol Unit Reboiler HTR-09 HTR-09

1.5 MMBtu/hr Line Heaters HTR-10 HTR-10

12 – 3,000 Btu/hr Catalytic Heaters CAT-HTR CAT-HTR




Source FIN EPN Calculation Method

Glycol Unit (Condenser) DEHY-01 DEHY-01 ProMax v3.2

Glycol Unit (Flash Tank) DEHY-01 FLR-02 ProMax v3.2, TCEQ Flare

Factors

Truck Loading (Uncaptured) LOAD LOAD EPA AP-42

Truck Loading (Controlled) LOAD FLR-02

EPA AP-42, TCEQ Flare

Factors and Material Balance

for SO2

500-bbl Oil/Condensate Tanks

OILTK-01

through

OILTK-22

FLR-02 Breathing/Working and Flash

Analyses, AP-42, GOR

Method, TCEQ Flare Factors

and Material Balance for SO2

1,000-bbl Oil/Condensate Tank OILTK-23 FLR-02

500-bbl Produced Water Tanks

PWTK-01

through

PWTK-05

FLR-02

Utility Flare FLR-01 FLR-01

TCEQ Flare Factors and

Material Balance for SO2 Process Flare FLR-02 FLR-02

Flash and IP Compressors

Blowdowns/Startups COMP-MSS FLR-01

Vapor Recovery Tower Gas VRT-GAS FLR-02

GOR Method, TCEQ Flare

Factors and Material Balance

for SO2

Drip Vapor Recovery Tower Gas DRIPVRT-GAS FLR-02

Heater Treater Gas

Separator Gas

Produced Gas during Compressor

Downtime

PROD-GAS FLR-01

Planned MSS Activities

MSS-HTRDEG

MSS-PIG

MSS-HTRCLN

MSS-TNKCLN

MSS-HTRDEG

MSS-PIG

MSS-HTRCLN

MSS-TNKCLN

EPA AP-42 and Ideal Gas Law

3.2 ANALYSES

Emissions are based on site-specific gas and liquid analyses from the Monson Unit (see Appendix C). Flash, gas, and liquid compositions were obtained from ProMax modeling using the below gas and liquid analyses.




Summary of Gas and Liquid Analyses

Sample Type Sample Location / Sample Date Equipment / Process Calculated

Gas Monson Unit – First Stage Separator Gas

03/20/2015 Input to ProMax Model

Liquid

Monson Unit – First Stage Separator

Hydrocarbon Liquid

03/20/2015

Input to ProMax Model

3.3 MODELED ANALYSES

The process model ProMax v3.2 was used to model the compositions listed in the below table for use in the emission calculations. ProMax models were created for each mode of operations: current and future operations. The models were only used to obtain stream compositions and gas-to-oil ratios (“GOR”) of streams shown in the table below but not to evaluate mass emissions. The calculation method for each source is detailed in Section 3.1. The models reports are in Appendix E.

Summary of ProMax Model Stream Applications

Type ProMax Model Process Stream Equipment / Process Calculated

Gas Separator Gas – LP Sep Gas

Fugitive emissions - Gas components

Flare emissions – various streams

Planned MSS emissions

Fuel Gas1 Fuel Gas – Outlet Gas Flare pilot emissions

Emissions from combustion sources

Liquid Sales Oil Liquid – Outlet Oil Fugitive emissions - Liquid components

B/W Vapor2 Vapor in equilibrium with liquid ProMax

Stream: Sales Oil Liquid – Outlet Oil

Breathing/Working emissions – Storage tanks

Loading emissions

Liquid Drip Liquid - Drip Oil (ProMax Stream) Drip (Oil/Cond.) tank emissions -

Breathing/working

Flash Flash off drip tanks – Drip Tank Flash Flash emissions – Drip (Oil/Cond.) storage

tanks

Flash Flash off VRTs – VRT Gas Flash emissions – VRTs

Flash Flash off drip VRT – Drip VRT Gas Flash emissions – Drip VRT

Flash Flash off Heater Treaters – Stream 11 Flash emissions – Heater Treaters

1 Conservatively assumed H2S content of fuel gas after sweetening is 24 ppmv. Fuel gas composition was normalized by adding propane. 2 The composition of the vapor in equilibrium with the modeled Sales Oil Liquid – Outlet Oil at the maximum bulk liquid temperature was calculated based on the vapor pressure of each component of the liquid mixture. This composition was used to estimate storage tanks breathing/working emissions and loading emissions. The calculation method for this composition is documented in Appendix C.




Type ProMax Model Process Stream Equipment / Process Calculated

Gas Glycol Unit Condenser – Condenser

Vapor Glycol Unit emissions

Gas Glycol Unit Flash Tank – Flash Sep Gas Glycol Unit emissions




4.0 IMPACTS EVALUATION




4.0 IMPACTS EVALUATION

In accordance with paragraph (b)(8) of 30 TAC §116.602 – NON RULE 2012-NOV-08, an impacts analysis as specified in paragraph (k) has been conducted to demonstrate compliance with applicable National Ambient Air Quality Standards (“NAAQS”), State Property Line Standard, and Effects Screening Levels (“ESL”). The tables in Appendix B demonstrate compliance with the relevant NAAQS, State Property Standard, and ESL.

4.1 GENERIC MODELING TABLES

Impacts evaluations for SO2, benzene and H2S were conducted using the Generic Modeling Results tables in paragraph (m) of 30 TAC §116.602 – NON RULE 2012-NOV-08 to show that protectiveness limits have been met at the nearest property line.

4.2 DISPERSION MODELING

Dispersion modeling (SCREEN3) of NO2 emissions from all applicable sources was performed to ensure compliance with the hourly NAAQS for NO2. The maximum predicted impacts are shown at distances beyond the property line.

4.3 ALTERNATE NO2 BACKGROUND CONCENTRATION JUSTIFICATION

There is no NO2 monitor located in Karnes County or near the Patton Trust South Production Facility. Therefore, out of county monitors were reviewed for representativeness. The monitored concentration from the Corsicana Airport monitor was determined to be a conservative estimate of monitored emissions surrounding the Patton Trust South Production Facility. The Corsicana Airport monitor is located in Navarro County. A comparison of county-wide emissions was conducted using the 2011 National Emissions Inventory data from the EPA website. The emissions from Navarro County are approximately two (2) times the emissions from Karnes County.




2011 National Emission Inventory Data (NOx) By County3 Source Sector Navarro Karnes

Mobile 3,363 570

Industrial Processes 3,308 2,900

Biogenics 817 429

Fuel Combustion 87 294

Fires 141 68

Miscellaneous 10 4

Total 7,726 4,265

A comparison of actual emissions within 10 km of the site and within 10 km of the monitor was also conducted. Counties located within 10 km of the site and 10 km of the monitor were identified. Only one county is within a 10 km radius of the Patton Trust South Production Facility: Karnes County. The Corsicana Airport monitor is located over 10 km from any adjacent county. Emissions inventory data were reviewed, by county, for both the monitor and the site. Locations of facilities were identified, and NOx emissions were summed if they met the 10 km distance criteria. A complete list of facilities and associated NOx emissions and locations reviewed are included in Appendix B.

NOx Emissions within 10 km as reported

in 2014 Emissions Inventory4

Location NOx (tpy)

Patton Trust South Production Facility 147.09

Corsicana Airport Monitor 2,199.26

Population data from the US Census Website for Navarro county and Karnes county were compared. It is expected that a higher population would result in increased emissions from automobile traffic and industry. The population of Navarro County is over three (3) times the population of Karnes County.

Population Comparison5

County Population

Karnes 14,906

Navarro 48,195

The area surrounding the monitor and site were compared. The Patton Trust South Production Facility is located in a sparsely-populated rural area, outside Karnes City. The area surrounding the facility is relatively flat surrounded by county roads, vegetation, and other oil and gas

3 Source: http://www.epa.gov/air/emissions/ 4 2014 Point Source Emissions Inventory, TCEQ (https://www.tceq.texas.gov/airquality/point-source-ei/psei.html) 5 Source: http://quickfacts.census.gov, 2014 estimate




facilities. The Corsicana Airport monitor is located outside the city of Corsicana. There is an airport nearby, as well as well as county roads, and vegetation. The land surrounding the monitor is relatively flat. The Corsicana Airport monitor is located in an area with higher emissions and a higher population than the Patton Trust South Production Facility. Therefore, it is determined that the use of the Corsicana Airport monitor is conservative. Three years of monitor data were reviewed for completeness, following TCEQ Guidance (APDG 6232v2, Appendix D). The form and hourly concentration for the Corsicana Airport monitor is shown in the table below.

Corsicana Airport Monitor Design Value

Contaminant Monitor

Station County

Averaging

Period

Concentration

(µg/m3) Form

NO2 Corsicana

Airport Navarro 1-Hour 47.0

3-Year Average, 98th

Percentile of Daily

Maximums

2013-2015




5.0 REQUIREMENTS AND APPLICABILITY




5.0 REQUIREMENTS AND APPLICABILITY

5.1 GENERAL REQUIREMENTS AND APPLICABILITY

The general requirements listed in 30 TAC §116.610 and §116.615 for issuance of a standard permit are satisfied as described below.

5.1.1 §116.610 Applicability

(a) Under the Texas Clean Air Act, §382.051, a project that meets the requirements for a standard permit listed in this subchapter or issued by the commission is hereby entitled to the standard permit, provided the following conditions listed in this section are met. For the purposes of this subchapter, project means the construction or modification of a facility or a group of facilities submitted under the same registration.

(1) Any project that results in a net increase in emissions of air contaminants from

the project other than carbon dioxide, water, nitrogen, methane, ethane, hydrogen, oxygen, or those for which a national ambient air quality standard has been established must meet the emission limitations of §106.261 of this title relating to Facilities (Emission Limitations), unless otherwise specified by a particular standard permit.

As specified in paragraph (h) of 30 TAC §116.602 – NON RULE 2012-NOV-08, total maximum estimated emissions meet the most stringent emission limitations outlined in this paragraph. See demonstration of compliance in Appendix A.

(2) Construction or operation of the project must be commenced prior to the effective date of a revision to this subchapter under which the project would no longer meet the requirements for a standard permit.

Encana currently operates all existing equipment pursuant to the requirements of this subchapter. Encana will ensure that subsequent revisions to this subchapter are met.

(3) The proposed project must comply with the applicable provisions of the Federal Clean Air Act (FCAA), §111 (concerning New Source Performance Standards) as listed under 40 Code of Federal Regulations (CFR) Part 60, promulgated by the United States Environmental Protection Agency (EPA).

Sources at the site meet all applicable provisions of 40 CFR Part 60. See discussion in Section 5.3 for more details.

(4) The proposed project must comply with the applicable provisions of FCAA, §112 (concerning Hazardous Air Pollutants) as listed under 40 CFR Part 61, promulgated by the EPA.




Operations at the site do not trigger any additional applicable provisions of 40 CFR Part 61 regarding hazardous air pollutants.

(5) The proposed project must comply with the applicable maximum achievable control technology standards as listed under 40 CFR Part 63, promulgated by the EPA under FCAA, §112 or as listed under Chapter 113, Subchapter C of this title (relating to National Emissions Standards for Hazardous Air Pollutants for Source Categories (FCAA, §112, 40 CFR Part 63)).

Sources at the site meet all applicable provisions of 40 CFR Part 63. See discussion in Section 5.3 for more details.

(6) If subject to Chapter 101, Subchapter H, Division 3 of this title (relating to Mass Emissions Cap and Trade Program) the proposed facility, group of facilities or account must obtain allocations to operate.

Facilities in Karnes County are not subject to the Mass Emissions Cap and Trade Program. (b) Any project that constitutes a new major stationary source or major modification as

defined in §116.12 of this title (relating to Nonattainment and Prevention of Significant Deterioration Review Definitions) is subject to the requirements of §116.110 of this title (relating to Applicability) rather than this subchapter.

The Patton Trust South Production Facility is not located in a nonattainment area; therefore, this project does not constitute a new major source or a major modification as defined in §116.12 of this title and therefore is not subject to the 116.110 regulations. (c) Persons may not circumvent by artificial limitations the requirements of §116.110 of this

title. Encana is not circumventing by artificial limitations the requirements of §116.110 of this title. (d) Any project involving a proposed affected source (as defined in §116.15(1) of this title

(relating to Section 112(g) Definitions)) shall comply with all applicable requirements under Subchapter E of this chapter (relating to Hazardous Air Pollutants: Regulations Governing Constructed or Reconstructed Major Sources (FCAA, §112(g), 40 CFR Part 63)). Affected sources subject to Subchapter E of this chapter may use a standard permit under this subchapter only if the terms and conditions of the specific standard permit meet the requirements of Subchapter E of this chapter.

Operations at the site do not involve an affected source as defined in §116.15(1) of this title (relating to Section 112(g) Definitions); therefore, this paragraph does not apply.




5.1.2 §116.615 General Conditions

The following general conditions are applicable to holders of standard permits, but will not necessarily be specifically stated within the standard permit document. (1) Protection of public health and welfare. The emissions from the facility, including

dockside vessel emissions, must comply with all applicable rules and regulations of the commission adopted under Texas Health and Safety Code, Chapter 382, and with the intent of the Texas Clean Air Act (TCAA), including protection of health and property of the public.

The emissions from the facilities represented in the registration comply with all applicable rules and regulations adopted under the Texas Health and Safety Code, Chapter 382, and with the intent of the TCAA including protection of the health and property of the public. (2) Standard permit representations. All representations with regard to construction plans,

operating procedures, and maximum emission rates in any registration for a standard permit become conditions upon which the facility or changes thereto, must be constructed and operated. It is unlawful for any person to vary from such representations if the change will affect that person's right to claim a standard permit under this section. Any change in condition such that a person is no longer eligible to claim a standard permit under this section requires proper authorization under §116.110 of this title (relating to Applicability). If the facility remains eligible for a standard permit, the owner or operator of the facility shall notify the executive director of any change in conditions which will result in a change in the method of control of emissions, a change in the character of the emissions, or an increase in the discharge of the various emissions as compared to the representations in the original registration or any previous notification of a change in representations. Notice of changes in representations must be received by the executive director no later than 30 days after the change.

Encana operates the facilities included in this registration as represented in this documentation. If, at any time Encana intends to change a representation, the executive director will be notified. (3) Standard permit in lieu of permit amendment. All changes authorized by standard permit

to a facility previously permitted under §116.110 of this title shall be administratively incorporated into that facility's permit at such time as the permit is amended or renewed.

Changes to the equipment authorized under Permit No. 125964 that are included in this standard permit will be administratively incorporated. (4) Construction progress. Start of construction, construction interruptions exceeding 45

days, and completion of construction shall be reported to the appropriate regional office not later than 15 working days after occurrence of the event, except where a different time period is specified for a particular standard permit.

Encana will meet construction notification requirements as applicable. (5) Start-up notification.




(A) The appropriate air program regional office of the commission and any other air pollution control agency having jurisdiction shall be notified prior to the commencement of operations of the facilities authorized by a standard permit in such a manner that a representative of the executive director may be present.

(B) For phased construction, which may involve a series of units commencing operations at different times, the owner or operator of the facility shall provide separate notification for the commencement of operations for each unit.

(C) Prior to beginning operations of the facilities authorized by the permit, the permit holder shall identify to the Office of Permitting, Remediation, and Registration, the source or sources of allowances to be utilized for compliance with Chapter 101, Subchapter H, Division 3 of this title (relating to Mass Emissions Cap and Trade Program).

(D) A particular standard permit may modify start-up notification requirements. Encana has submitted notification (as required in 30 TAC §116.602 – NON RULE 2012-NOV-08) prior to construction or implementation of changes. (6) Sampling requirements. If sampling of stacks or process vents is required, the standard

permit holder shall contact the commission's appropriate regional office and any other air pollution control agency having jurisdiction prior to sampling to obtain the proper data forms and procedures. All sampling and testing procedures must be approved by the executive director and coordinated with the regional representatives of the commission. The standard permit holder is also responsible for providing sampling facilities and conducting the sampling operations or contracting with an independent sampling consultant.

If sampling is required, Encana will contact the regional office prior to sampling to obtain the proper data forms and procedures. (7) Equivalency of methods. The standard permit holder shall demonstrate or otherwise

justify the equivalency of emission control methods, sampling or other emission testing methods, and monitoring methods proposed as alternatives to methods indicated in the conditions of the standard permit.

As Encana has represented in this registration, it does not intend to use alternative methods for emission control, sampling or emissions testing. (8) Recordkeeping. A copy of the standard permit along with information and data sufficient

to demonstrate applicability of and compliance with the standard permit shall be maintained in a file at the plant site and made available at the request of representatives of the executive director, the United States Environmental Protection Agency, or any air pollution control agency having jurisdiction. For facilities that normally operate unattended, this information shall be maintained at the nearest staffed location within Texas specified by the standard permit holder in the standard permit registration. This information must include, but is not limited to, production records and operating hours. Additional recordkeeping requirements may be specified in the conditions of the standard permit. Information and data sufficient to demonstrate applicability of and compliance with the standard permit must be retained for at least two years following the date that the information or data is obtained. The copy of the standard permit must be maintained as a permanent record.




A copy of the standard permit along with a copy of this registration will be maintained in a file at the field office. (9) Maintenance of emission control. The facilities covered by the standard permit may not

be operated unless all air pollution emission capture and abatement equipment is maintained in good working order and operating properly during normal facility operations. Notification for emissions events and scheduled maintenance shall be made in accordance with §101.201 and §101.211 of this title (relating to Emissions Event Reporting and Recordkeeping Requirements; and Scheduled Maintenance, Startup, and Shutdown Reporting and Recordkeeping Requirements).

Emission controls at the site are maintained in good working order and operated properly during normal facility operations. (10) Compliance with rules. Registration of a standard permit by a standard permit applicant

constitutes an acknowledgment and agreement that the holder will comply with all rules, regulations, and orders of the commission issued in conformity with the TCAA and the conditions precedent to the claiming of the standard permit. If more than one state or federal rule or regulation or permit condition are applicable, the most stringent limit or condition shall govern. Acceptance includes consent to the entrance of commission employees and designated representatives of any air pollution control agency having jurisdiction into the permitted premises at reasonable times to investigate conditions relating to the emission or concentration of air contaminants, including compliance with the standard permit.

This standard permit registration constitutes Encana’s acknowledgement and agreement of the terms stated in the paragraph above. (11) Distance limitations, setbacks, and buffer zones. Notwithstanding any requirement in any

standard permit, if a standard permit for a facility requires a distance, setback, or buffer from other property or structures as a condition of the permit, the determination of whether the distance, setback, or buffer is satisfied shall be made on the basis of conditions existing at the earlier of: (A) the date new construction, expansion, or modification of a facility begins; or (B) the date any application or notice of intent is first filed with the commission to

obtain approval for the construction or operation of the facility. Encana will comply with applicable distance requirements in place on the date this registration is first filed with the TCEQ.




5.2 SPECIFIC REQUIREMENTS OF 30 TAC §116.602 – NON RULE 2012-NOV-08

(a) Applicability The Patton Trust South Production Facility is an oil and gas site, which consists of stationary facilities, that produces and processes natural gas, crude oil/condensate, and produced water found in geologic formations and meets the conditions outlined in paragraph (a)(1) of this rule.

(b) Definitions and Scope Encana understands the definitions and will ensure all requirements outlined in the scope of this paragraph are met.

(c) Authorized Facilities, Changes and Activities The Patton Trust South Production Facility is an existing oil and gas site (OGS) which meets the registration requirements of paragraph (c)(2). This site will meet the conditions outlined in this section.

(d) Facilities and Exclusions

Applicable facilities located at the Patton Trust South Production Facility are permissible and may be included in this registration.

(e) Best Management Practices (BMP) and Best Available Control Technology

(BACT) Requirements (1) Facilities which have the potential to emit air contaminants are

maintained in good working order and operated properly during facility operations. Encana has established and will maintain a program to replace, repair, and/or maintain facilities to keep them in good working order.

(2) Applicable OGS facilities are operated at least 50 feet from any property line.

(3) The natural gas powered engines (FIN: ENG-01 through ENG-08, ENGVRU-01 through ENGVRU-04) meet the emission and performance standards listed in Table 6 in paragraph (m) of this rule and the requirements outlined in (3)(A) through (3)(E) of this paragraph.

(4) There are no open-topped tanks or ponds located at the Patton Trust South Production Facility.

(5) Process equipment and storage facilities (FIN: OILTK-01 through OILTK-23, PWTK-01 through PWTK-05, DEHY-01) individually meet the requirements of BACT listed in Table 10 in paragraph (m). The




uncontrolled combined emissions from process equipment and storage facilities have a PTE of ≥ 25 tpy and meet the “Combined Control Requirements” of Table 10.

(6) The following shall apply to all fugitive components associated with this project: (A) Seals and gaskets on components in VOC or H2S service will be

installed, checked, and properly maintained to prevent leaking. Applicable components will be physically inspected quarterly for leaks.

(B) Fugitive components have an uncontrolled potential to emit greater than 25 tpy VOC and are therefore subject to a leak detection and repair (“LDAR”) program and additional requirements as specified in Table 9.

(C) Encana will repair fugitive components found to be leaking. (D) Tank hatches will remain closed except for sampling, gauging,

loading, unloading, or planned maintenance activities. (E) New and reworked valves and piping connections will be located

in a place that is reasonably accessible for leak checking during plant operation and underground process pipelines will contain no buried valves such that fugitive emission monitoring is rendered impractical (to the extent of which good engineering practices will permit).

(7) Tanks and vessels will utilize a paint color that minimizes the effects of solar heating or utilize alternate control.

(8) Emission estimation methods have been used in a way that is consistent with protocols established by the commission.

(9) The glycol reboiler (FIN: HTR-09) is used to control emissions from the glycol dehydration unit flash tank and condenser (FIN: DEHY-01). The vapors are premixed with fuel gas and basic monitoring is applied, therefore 99% control of VOC and H2S may be claimed.

(10) The vapor recovery system operating at this site will meet the appropriate design, monitoring, and recordkeeping in Table 7 and Table 8 in paragraph (m), as applicable.

(11) The flares (FIN: FLR-01, FLR-02) at this site are used for control of emissions from production with a destruction efficiency of 99% (C3) / 98% (C4+) for VOCs and 98% for H2S. The flares meet the design and operating requirements outlined in this subsection.

(12) There are no thermal oxidation or vapor combustion control devices located at this site.

(f) Registration, Revision, and Renewal Requirements

(1) For all previous claims of this standard permit (or any previous version of this standard permit) existing authorized facilities, or group of facilities, are not required to meet the requirements of this standard permit, with the




exception of planned MSS, until a renewal under the standard permit is submitted after December 31, 2015. Existing authorized facilities meet the applicable requirements of this standard permit.

(2) This submittal includes changes other than authorizing planned MSS at an existing OGS under this standard permit; therefore, this subsection does not apply.

(3) Facilities registered under this standard permit are not also authorized by a permit under 30 TAC §116.111, General Application.

(4) Required notification was submitted through the e-Permits system prior to construction or implementation of changes for this project.

(5) This registration meets the emission limitations, registration timeframe, required documentation, applicable fees, and construction and operation requirements of this standard permit.

(6) If the site’s emissions increase, Encana will submit the proper notification and or registration.

(g) Any claim under this standard permit must comply with all applicable requirements of 30 TAC §116.610; §116.611, Registration to Use a Standard Permit; §116.614, Standard Permit Fees; and §116.615, General Conditions. This standard permit supersedes: the notification requirements of 30 TAC §116.615, General Conditions; and the emission limitations of 30 TAC §116.610(a)(1), Applicability.

Claims under this standard permit comply with the applicable requirements of this paragraph.

(h) Emission Limitations

Total maximum estimated registered emissions are based on representative worst-case operations and meet the limitations established in paragraph (k) of this standard permit. Compliance with emission limitations of this standard permit is demonstrated in Appendix A.

(i) Planned Maintenance, Start-ups and Shutdowns (MSS) Encana has included planned maintenance, start-up, and shutdown (MSS) emissions in this registration.

(j) Records, Sampling and Monitoring Required records, sampling, and monitoring data will be maintained electronically or hard copy at the field office and will be readily available to the agency or local pollution control program with jurisdiction upon request.




(k) Emission Limits Based on Impacts Evaluation Impacts evaluations have been completed in accordance with the specifications of this standard permit to demonstrate compliance with the NAAQS for NO2 and SO2, the state property line standard for H2S, and with the hourly ESL for benzene.

(l) Existing, Unchanged Facilities and Projects Before Effective Date. The

requirements in 30 TAC §116.620 are applicable to existing unchanged facilities and new or changing facilities as specified in paragraph (a)(1) of this standard permit.

Existing, new, and changing facilities will meet the requirements specified in this standard permit.

(m) The following Tables shall be used as required by this standard permit.

The applicable tables included in this paragraph were used as required by this standard permit.




5.3 FEDERAL REQUIREMENTS AND APPLICABILITY

This section presents a review of the federal air quality regulations that apply to operations as of March 2016 at the Patton Trust South Production Facility.

5.3.1 Title 40 CFR Part 60 – NSPS

The table below presents the New Source Performance Standards (NSPS) that are potentially applicable to facilities at the Patton Trust South Production Facility.

Subpart Title 40 CFR Part 60 Applicability

Subpart A General Provisions: §60.18 – General control device and work practice requirements

The flares at this site are designed to operate in accordance with the requirements of this subpart.

Subpart Dc Standards of Performance for Small Industrial-Commercial-Institutional Steam Generating Units

The maximum design heat input capacity of each external combustion unit operating at this site is less than 100 MMBtu/hr; therefore, this subpart does not apply.

Subpart K Standards of Performance for Storage Vessels for Petroleum Liquids for Which Construction, Reconstruction, or Modification Commenced After June 11, 1973, and Prior to May 19, 1978

The storage tanks at the site commenced construction after May 19, 1978; therefore, this subpart does not apply.

Subpart Ka Standards of Performance for Storage Vessels for Petroleum Liquids for Which Construction, Reconstruction, or Modification Commenced After May 18, 1978 and Prior to July 23, 1984

The storage tanks at the site commenced construction after July 23, 1984; therefore, this subpart does not apply.

Subpart Kb Standards of Performance for Storage Vessels for Petroleum Liquids for Which Construction, Reconstruction, or Modification Commenced After July 23, 1984

The produced water storage tanks (FIN: PWTK-01 to PWTK-05) and oil/condensate storage tanks (FIN: OILTK-01 to OILTK-23) at the site each have a storage capacity less than 1,589.874 cubic meters (m3); therefore, this subpart does not apply per §60.110b(d)(4).





Subpart KKK

Standards of Performance for Equipment Leaks of VOC From Onshore Natural Gas Processing Plants for Which Construction, Reconstruction, or Modification Commenced After January 20, 1984, and on or Before August 23, 2011.

This site does not meet the definition of natural gas processing plant as defined in 40 CFR §60.631; therefore, this subpart does not apply.

Subpart LLL

Standards of Performance for SO2 Emissions From Onshore Natural Gas Processing for Which Construction, Reconstruction, or Modification Commenced After January 20, 1984, and on or Before August 23, 2011

This site does not operate an affected facility under this subpart; therefore, this subpart does not apply.

Subpart IIII

Standards of Performance for Stationary Compression Ignition Internal Combustion Engine

This site does not operate an affected facility under this subpart; therefore, this subpart does not apply.





Subpart JJJJ

Standards of Performance for Stationary Spark Ignition Internal Combustion Engines

The stationary spark-ignited internal combustion engines at the site (FIN: ENG-01 through ENG-06) are non-emergency, >1,350 HP and were manufactured after July 1, 2007; therefore, they are subject to the requirements of this subpart per §60.4230(a)(4)(i). Encana will comply with the applicable testing, reporting, monitoring, and recordkeeping requirements of this subpart.

The stationary spark-ignited internal combustion engines at the site (FIN: ENG-07, ENG-08, ENGVRU-01, ENGVRU-02, ENGVRU-03) are non-emergency, 4SRB, <500 HP and were manufactured after July 1, 2008; therefore, they are subject to the requirements of this subpart per §60.4230(a)(4)(iii). Encana will comply with the applicable testing, reporting, monitoring, and recordkeeping requirements of this subpart.

The stationary spark-ignited internal combustion engine at the site (FIN: ENGVRU-04) was manufactured before June 12, 2006; therefore, this subpart does not apply.





Subpart OOOO

Standards of Performance for Crude Oil and Natural Gas Production, Transmission, and Distribution

The site does have potentially applicable sources. However, all storage vessels (except two listed below) have annual VOC emissions below 6 tpy, each.

Two storage tanks at the site (FIN: OILTK-21, OILTK-22) were previously authorized with PTE VOC emissions > 6 tpy, each and were manufactured after August 23, 2011. However, due to updated throughputs, VOC emissions from these storage tanks are anticipated to be < 6 tpy, each and an applicability determination will be completed at that time. Encana will maintain documentation of actual VOC emissions in accordance with applicable recordkeeping requirements of this subpart.

Some onsite pneumatic controllers, with a bleed rate > 6 scfh, were constructed after August 23, 2011. These pneumatic controller affected facilities will meet the requirements of §60.5390 as applicable.

Some onsite reciprocating gas compressors were constructed after August 23, 2011. These compressors will meet the requirements of §60.5385 as applicable.

5.3.2 Title 40 CFR Part 61 – NESHAP

The table below presents the National Emission Standards for Hazardous Air Pollutants (“NESHAP”) that are potentially applicable to facilities at the Patton Trust South Production Facility.


Subpart V National Emission Standards for Equipment Leaks (Fugitive Emission Sources)

No sources at this site will operate in volatile hazardous air pollutant (VHAP) service as defined in §61.241 of this subpart.




5.3.3 Title 40 CFR Part 63 – MACT

The table below presents the National Emission Standards for Hazardous Air Pollutants (NESHAP) that are potentially applicable to facilities at the Patton Trust South Production Facility.


Subpart HH National Emission Standards for Hazardous Air Pollutants From Oil and Natural Gas Production Facilities

This site is an OGS located at an area source of HAP emissions and operates a large TEG dehydration unit (FIN: DEHY-01) which is an affected source. The unit is exempt from the requirements of paragraph §63.764(d) per §63.764(e)(ii) as actual benzene emissions as determined with federally enforceable controls are less than 1 tpy. Encana will comply with this subpart by meeting the record keeping requirements of §63.774(d)(1).

Subpart ZZZZ

National Emission Standards for Hazardous Air Pollutants for Stationary Reciprocating Internal Combustion Engines

Engines at the site (FIN: ENG-01 through ENG-08, ENGVRU-01 through ENGVRU-03) are new stationary RICE located at an area source of HAPs. Per §63.6590, the engines will meet the requirements of this part by meeting the requirements of 40 CFR Part 60 Subpart JJJJ, as applicable.

The VRU compressor at the site (FIN: ENGVRU-04) is an existing non-emergency, non-black start 4SRB stationary RICE ≤ 500 HP located at an area source of HAPs and will meet the applicable requirements of §63.6603(a) - Table 2d.10.



ENCANA OIL & GAS (USA) INC.

APPENDIX A EMISSIONS CALCULATIONS

Oil and Gas Emissions Spreadsheet

OIL AND GAS FACILITY GENERAL INFORMATION

Company Name Encana Oil & Gas (USA) Inc.

Field Name Eagle Ford

Facility/Well Name Patton Trust South Production Facility

Nearest City/Town Karnes City

API Number/SIC Code 1311

Latitude/Longitude 28.893137 / -97.83456

County Karnes

PI-7, PI-7 CERT, APD- CERT, E-Permits? PI-1S

Authorization Type NRSP

Registration Number 125964

Customer Number (if known) CN601451149

Regulated Number (if known) RN106397284

Natural Gas Site Throughput (MMSCF/day): 33.00

Produced Water Site Average Throughput (bbl/day): 3,500

Oil/Condensate Site Average Throughput (bbl/day): 9,000

Drip (Oil/Cond.) Site Average Throughput (bbl/day): 19

Produced Water Site Maximum (bbl/day): 6,000 (used for max hourly calculations)

Oil/Condensate Site Maximum (bbl/day): 14,000 (used for max hourly calculations)

Drip (Oil/Cond.) Site Maximum (bbl/day): 19 (used for max hourly calculations)

H2S Concentration - Maximum Stream (PPMV): 174

Is the gas sweet or sour? Sour

Is this site operational/producing? Yes

Has the site been registered before? Yes

Are MSS emissions included in this registration? Yes

EQUIPMENT/PROCESSES AT SITE HOW MANY FOR THIS PROJECT/SITE?

ICE Engines 12

Turbines 0

Diesel Engines 0

Heaters-Boilers 11

Oil / Condensate Tanks 23

Produced Water Tanks 5

Miscellaneous Tanks 0

Loading Jobs 2

Glycol Units 1

Amine Units 0

Vapor Recovery Units 4

Flares-Vapor Combustors 2

Thermal Oxidizers 0

Encana Oil & Gas (USA) Inc.Patton Trust South Production Facility

Emissions Summary Table

Stream characterizationAlternate OperatingScenarios

Stream Flow Pressure

1 2 3 lb/hrlb/hr

Natural Gaslb/hr

Condensatetpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

Natural Gas

OR Condensate

Steady-state

ORPeriodic

High

ORLow

FUG FUG Fugitive Emissions X X X X 6.960 1.966 4.994 30.485 -- -- -- -- -- -- -- -- -- -- 0.019 0.083 0.001 0.003 -- -- 0.539 2.359 N & C S -- 8,760

ENG-01 ENG-01 IP Compressor Engine - Caterpillar G3516B X X X X 2.464 2.464 -- 10.794 3.042 13.326 3.955 17.323 0.103 0.449 0.103 0.449 0.034 0.148 0.005 0.020 -- -- 0.335 1.466 0.526 2.304 N S -- 8,760

ENG-02 ENG-02 IP Compressor Engine - Waukesha L7044GSI X X X 2.593 2.593 -- 11.356 1.852 8.111 4.815 21.089 0.271 1.187 0.271 1.187 0.046 0.201 0.022 0.096 -- -- 0.285 1.248 0.394 1.724 N S -- 8,760

ENG-03 ENG-03 IP Compressor Engine - Caterpillar G3516B X X X X 2.282 2.282 -- 9.994 3.042 13.326 3.955 17.323 0.102 0.448 0.102 0.448 0.034 0.148 0.005 0.020 -- -- 0.152 0.666 0.343 1.503 N S -- 8,760

ENG-04 ENG-04 Flash Compressor Engine - Caterpillar G3516B X X X X 2.282 2.282 -- 9.994 3.042 13.326 3.955 17.323 0.102 0.448 0.102 0.448 0.034 0.148 0.005 0.020 -- -- 0.152 0.666 0.343 1.503 N S -- 8,760

ENG-05 ENG-05 Flash Compressor Engine - Caterpillar G3516B X X X X 2.464 2.464 -- 10.794 3.042 13.326 3.955 17.323 0.103 0.449 0.103 0.449 0.034 0.148 0.005 0.020 -- -- 0.335 1.466 0.526 2.304 N S -- 8,760

ENG-06 ENG-06 Flash Compressor Engine - Waukesha L7044GSI X X X 2.593 2.593 -- 11.356 1.852 8.111 4.815 21.089 0.254 1.111 0.254 1.111 0.043 0.188 0.021 0.090 -- -- 0.267 1.168 0.368 1.614 N S -- 8,760

ENG-07 ENG-07 Cooler Engine - Arrow VRG 330 X X X X 0.118 0.118 -- 0.519 0.420 1.839 0.720 3.152 0.012 0.052 0.012 0.052 0.002 0.009 0.001 0.004 -- -- 0.013 0.059 0.018 0.080 N S -- 8,760

ENG-08 ENG-08 Cooler Engine - Arrow VRG 330 X X X X 0.118 0.118 -- 0.519 0.420 1.839 0.720 3.152 0.012 0.052 0.012 0.052 0.002 0.009 0.001 0.004 -- -- 0.013 0.059 0.018 0.080 N S -- 8,760

ENGVRU-01 ENGVRU-01 VRU Compressor Engine - Cummins G855 X X 0.290 0.290 -- 1.271 0.414 1.815 0.414 1.815 0.032 0.138 0.032 0.138 0.005 0.023 0.003 0.011 -- -- 0.033 0.145 0.046 0.201 N S -- 8,760

ENGVRU-02 ENGVRU-02 VRU Compressor Engine - Cummins G855 X X 0.290 0.290 -- 1.271 0.414 1.815 0.414 1.815 0.032 0.138 0.032 0.138 0.005 0.023 0.003 0.011 -- -- 0.033 0.145 0.046 0.201 N S -- 8,760

ENGVRU-03 ENGVRU-03 VRU Compressor Engine - GM Vortec 5.7L X X 0.142 0.142 -- 0.622 0.203 0.888 0.406 1.777 0.015 0.067 0.015 0.067 0.003 0.011 0.001 0.005 -- -- 0.016 0.070 0.022 0.097 N S -- 8,760

ENGVRU-04 ENGVRU-04 VRU Compressor Engine - Cummins G8.3 X X X X 0.130 0.130 -- 0.570 0.520 2.279 0.780 3.418 0.019 0.083 0.019 0.083 0.003 0.014 0.002 0.007 -- -- 0.005 0.022 0.013 0.055 N S -- 8,760

HTR-01 HTR-01 Heater Treater X X X X 0.003 0.003 -- 0.012 0.049 0.215 0.041 0.180 0.004 0.016 0.004 0.016 0.002 0.007 1.0E-06 4.5E-06 -- -- 3.7E-05 1.6E-04 3.9E-05 1.7E-04 N S -- 8,760





HTR-06 HTR-06 Heater Treater X X X X 0.008 0.008 -- 0.035 0.147 0.644 0.124 0.541 0.011 0.049 0.011 0.049 0.005 0.022 3.1E-06 1.4E-05 -- -- 1.1E-04 4.8E-04 1.2E-04 0.001 N S -- 8,760



HTR-09 HTR-09 Glycol Unit Reboiler X X X X 0.004 0.004 -- 0.018 0.074 0.322 0.062 0.271 0.006 0.024 0.006 0.024 0.002 0.011 1.5E-06 6.8E-06 -- -- 5.5E-05 2.4E-04 5.9E-05 2.6E-04 N S -- 8,760

HTR-10 HTR-10 Line Heater X X X X 0.008 0.008 -- 0.035 0.147 0.644 0.124 0.541 0.011 0.049 0.011 0.049 0.005 0.022 3.1E-06 1.4E-05 -- -- 1.1E-04 4.8E-04 1.2E-04 0.001 N S -- 8,760

CAT-HTR CAT-HTR Catalytic Heaters X X X X 1.9E-04 1.9E-04 -- 0.001 0.004 0.015 0.003 0.013 2.7E-04 0.001 2.7E-04 0.001 1.2E-04 0.001 7.4E-08 3.2E-07 -- -- 2.6E-06 1.2E-05 2.8E-06 1.2E-05 N S -- 8,760

DEHY-01 DEHY-01 Glycol Unit (Condenser) X X X X 0.123 0.123 -- 0.539 -- -- -- -- -- -- -- -- -- -- 0.011 0.050 -- -- -- -- 0.027 0.120 N S -- 8,760OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02, PWTK-03, PWTK-04, PWTK-05,

OILTK-23

OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02, PWTK-03, PWTK-04, PWTK-05,

OILTK-23

Uncontrolled/Uncaptured Tanks X X X X 2.706 -- 2.706 2.014 -- -- -- -- -- -- -- -- -- -- 0.005 0.005 0.001 2.7E-04 -- -- 0.100 0.078 C S -- 7,884

LOAD LOAD Truck Loading X X X X 32.339 -- 32.339 5.103 -- -- -- -- -- -- -- -- -- -- 0.055 0.009 0.007 0.004 -- -- 1.170 0.185 C S -- NA

Flare Pilot X X X X 0.012 0.012 -- 0.054 0.008 0.037 0.017 0.073 -- -- -- -- 2.0E-04 0.001 2.4E-05 1.1E-04 2.1E-06 9.3E-06 -- -- 3.6E-04 0.002 N S -- 8,760

Combustion Products from Compressors Blowdowns/Startups X X -- -- -- -- 0.422 0.066 0.843 0.132 -- -- -- -- 0.026 0.004 -- -- -- -- -- -- -- -- N P L 312

Combustion Products from Produced Gas X X -- -- -- -- 25.133 54.638 50.176 109.078 -- -- -- -- 1.734 3.770 -- -- -- -- -- -- -- -- N S -- 8,760

Combustion Products from Produced Gas during Compressor Downtime X X -- -- -- -- 27.319 -- 54.539 -- -- -- -- -- 1.885 -- -- -- -- -- -- -- -- -- N S -- 8,760

COMP-MSS Compressors Blowdowns/Startups X X 0.664 0.664 -- 0.104 -- -- -- -- -- -- -- -- -- -- 0.002 2.5E-04 2.7E-04 4.3E-05 -- -- 0.025 0.004 N P L 312

Produced Gas X X 47.097 47.097 -- 102.384 -- -- -- -- -- -- -- -- -- -- 0.120 0.262 0.018 0.040 -- -- 1.852 4.027 N S -- 8,760

Produced Gas during Compressor Downtime X X 51.192 51.192 -- -- -- -- -- -- -- -- -- -- -- -- 0.131 -- 0.020 -- -- -- 2.013 -- N S -- 8,760

Flare Pilot X X X X 0.012 0.012 -- 0.054 0.008 0.037 0.017 0.073 -- -- -- -- 2.0E-04 0.001 2.4E-05 1.1E-04 2.1E-06 9.3E-06 -- -- 3.6E-04 0.002 N S -- 8,760

Combustion Products from Controlled Tanks X X X X -- -- -- -- 0.762 0.326 1.521 0.652 -- -- -- -- 0.099 0.027 -- -- -- -- -- -- -- -- C S -- 8,760

Combustion Products from Truck Loading X X X X -- -- -- -- 0.229 0.036 0.457 0.072 -- -- -- -- 0.029 0.017 -- -- -- -- -- -- -- -- C S -- NA

Combustion Products from Glycol Unit (Flash Tank) X X X X -- -- -- -- 0.078 0.341 0.155 0.681 -- -- -- -- -- -- -- -- -- -- -- -- -- -- N S -- 8,760

Combustion Products from Vapor Recovery Towers Gas X X X X -- -- -- -- 9.191 0.808 18.348 1.613 -- -- -- -- 0.823 0.072 -- -- -- -- -- -- -- -- N S -- 8,760

Combustion Products from Drip Vapor Recovery Tower Gas X X X X -- -- -- -- 0.041 0.181 0.083 0.362 -- -- -- -- 0.003 0.012 -- -- -- -- -- -- -- -- N S -- 8,760OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02, PWTK-03, PWTK-04, PWTK-05,

OILTK-23

Controlled Tanks X X X X 4.183 -- 4.183 1.890 -- -- -- -- -- -- -- -- -- -- 0.009 0.005 0.001 2.9E-04 -- -- 0.184 0.085 C S -- 8,760

LOAD Truck Loading X X X X 1.250 -- 1.250 0.197 -- -- -- -- -- -- -- -- -- -- 0.003 4.1E-04 3.1E-04 1.8E-04 -- -- 0.055 0.009 C S -- NA

DEHY-01 Glycol Unit (Flash Tank) X X X X 0.188 0.188 -- 0.822 -- -- -- -- -- -- -- -- -- -- 0.001 0.004 -- -- -- -- 0.006 0.028 N S -- 8,760

VRT-GAS Vapor Recovery Towers Gas X X X X 44.385 44.385 -- 3.902 -- -- -- -- -- -- -- -- -- -- 0.142 0.012 0.009 0.001 -- -- 2.175 0.191 N S -- 8,760

DRIPVRT-GAS Drip Vapor Recovery Tower Gas X X X X 0.213 0.213 -- 0.933 -- -- -- -- -- -- -- -- -- -- 4.7E-04 0.002 2.8E-05 1.2E-04 -- -- 0.006 0.027 N S -- 8,760

MSS-HTRDEG MSS-HTRDEG Heater Treater Degassing X 21.247 21.247 -- 0.193 -- -- -- -- -- -- -- -- -- -- 0.047 4.3E-04 0.006 5.5E-05 -- -- 0.727 0.007 N P L 144

MSS-HTRCLN MSS-HTRCLN Vacuum Trucks (Heater Treater Cleanout) X 1.455 -- 1.455 0.006 -- -- -- -- -- -- -- -- -- -- 0.002 1.0E-05 2.6E-04 1.1E-06 -- -- 0.053 2.1E-04 C P L 8

MSS-PIG MSS-PIG Pig Launcher Degassing X 0.093 0.093 -- 0.020 -- -- -- -- -- -- -- -- -- -- 1.8E-04 3.8E-05 3.0E-05 6.4E-06 -- -- 0.003 0.001 N P L 432

MSS-TNKCLN MSS-TNKCLN Vacuum Trucks (Oil/Condensate Tank Cleanout) X 5.181 -- 5.181 0.089 -- -- -- -- -- -- -- -- -- -- 0.009 1.5E-04 0.001 1.6E-05 -- -- 0.187 0.003 C P L 35

MSS-TNKCLN MSS-TNKCLN Vacuum Trucks (Produced Water Tank Cleanout) X 0.040 -- 0.040 1.5E-04 -- -- -- -- -- -- -- -- -- -- 6.8E-05 2.5E-07 7.2E-06 2.7E-08 -- -- 0.001 5.4E-06 C P L 8

Total Emissions [3] 183.300 131.152 52.147 218.067 55.382 140.458 100.833 242.686 1.125 4.928 1.125 4.928 3.094 5.109 0.495 0.741 0.044 0.049 1.640 7.184 9.751 18.796

Steady-state [3] 156.787 111.315 45.472 217.655 54.960 140.392 100.442 242.555 1.125 4.928 1.125 4.928 3.069 5.105 0.437 0.741 0.038 0.048 1.640 7.184 8.780 18.781

< 30 psig periodic releases [3] 28.016 21.340 6.676 0.412 0.422 0.066 0.843 0.132 -- -- -- -- 0.026 0.004 0.058 0.001 0.007 1.21E-04 -- -- 0.971 0.015

Periodic ≥ 30 psig, up to 600hr/yr [3] -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- -- --

Below permit limits? -- Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes -- -- Yes Yes

Total emissions 250.0 250.0 250.0 15.0 15.0 250.0 10.2 47.0 25.0

Steady-state or < 30 psig periodic releases 750.0 145.0 121.0 104.0 28.0 28.0 93.2 7.0 10.8

Periodic ≥ 30 psig, up to 600hr/yr 1635.0 318.0 15.4 9.8

MAXIMUM OPERATING SCHEDULE: Hours/Day Days/Week 7 Weeks/Year 52 Hours/Year 8760

[1] HAPs are included in Total VOC

[2] Specific HAPs included are listed on each source page

[3] Hourly site-wide totals were calculated for each operating scenario (normal and alternate). The worst case is represented here.

Alternate Operating Scenarios:1: VRU Downtime2: Flash Compressor Downtine3: IP Compressor Downtime

FLR-01

FLR-02

FLR-01

FLR-02

PROD-GAS

24

Estimated Emissions

Non-Rule Standard PermitEmission Limits

FormaldehydeSO2 H2S

Hrs/yr

Total HAPs[2]

ESTIMATED EMISSIONS

No

rma

l Benzene

Emission Source Name

PM10 PM2.5CO

EPN FIN

VOC[1] NOx

Encana Oil & Gas (USA) Inc.

Patton Trust South Production Facility

Fugitives Emission Calculations

EPN

Name

Note:

Weight Percents From Analyses Tab: The three parts are set up in this arrangement:

(1)

HC wt % 97.11% HC wt % 100.00% (2)

VOC wt % 28.55% VOC wt % 100.00% (3)

Benzene wt % 0.05% Benzene wt % 0.31%

HAPs wt % 0.83% HAPs wt % 9.64%H2S wt % 0.01% H2S wt % 0.00%

(1) Gas Service Stream

lb/hr tpy lb/hr tpy

Valve 1641 0.009920 16.279 71.301 97% 0.488 2.139

Pumps 0 0.005290 0 0 85% 0 0

Connector 4118 0.000440 1.812 7.936 0% 1.812 7.936

Flange 1513 0.000860 1.301 5.699 0% 1.301 5.699

Open-ended Line 31 0.004410 0.137 0.599 0% 0.137 0.599

Pressure Relief Valves 99 0.019400 1.921 8.412 NA 1.921 8.412

Other 53 0.019400 1.028 4.504 NA 1.028 4.504

Total: 22.477 98.451 6.687 29.289

Gas Service Emissions Uncontrolled Controlled

Pollutant Wt %Hourly Emissions

(lb/hr)Annual Emissions

(tpy)Hourly Emissions


(tpy)

VOC 28.55% 6.609 28.948 1.966 8.612

Benzene 0.05% 0.013 0.055 0.004 0.016

HAPs 0.83% 0.192 0.843 0.057 0.251

H2S 0.01% 0.002 0.009 0.001 0.003

(2) Liquid Service Streams

lb/hr tpy lb/hr tpy

Valve 1414 0.005500 97% 0 0.000216 97% 0 0.0000185 97% 7.777 34.063 0.233 1.022

Pumps 70 0.028660 85% 0 0.000052 85% 0 0.0011300 85% 2.006 8.787 0.301 1.318

Connector 3374 0.000463 0% 0 0.000243 0% 0 0.0000165 0% 1.562 6.842 1.562 6.842

Flange 1116 0.000243 0% 0 0.000006 0% 0 0.00000086 0% 0.271 1.188 0.271 1.188

Open-ended Line 81 0.003090 0% 0 0.000550 0% 0 0.0003090 0% 0.250 1.096 0.250 1.096

Relief Valves 31 0.016500 NA 0 0.030900 NA 0 0.0000683 NA 0.512 2.240 0.512 2.240

Other 113 0.016500 NA 0 0.030900 NA 0 0.0000683 NA 1.865 8.167 1.865 8.167

Total: 14.243 62.384 4.994 21.873

Liquid Service Emissions: Uncontrolled Controlled

Pollutant Wt %Hourly Emissions




(tpy)VOC 100.00% 14.243 62.384 4.994 21.873

Benzene 0.31% 0.044 0.191 0.015 0.067

HAPs 9.64% 1.373 6.014 0.481 2.109

H2S 0.00% 3.8E-05 1.7E-04 1.3E-05 5.8E-05

(3) Total Fugitive Emissions: Uncontrolled Controlled

PollutantHourly Emissions




(tpy)THC 36.720 160.834 11.681 51.162

VOC 20.852 91.332 6.960 30.485

Benzene 0.056 0.246 0.019 0.083

HAPs 1.566 6.857 0.539 2.359H2S 0.002 0.009 0.001 0.003

Uncontrolled TOC Emissions

TOC EmissionsHeavy Oil

Emission Factor (lb/hr TOC per component)

Control EfficiencyComponent Count

TOC EmissionsControl Efficiency

Component Count

Water/Oil

Control EfficiencyComponent

Light Oil Emission Factor (lb/hr TOC per component)

Component

Component CountEmission Factor (lb/hr TOC per component)

Control Efficiency Component Count

Emission Factor (lb/hr TOC per component)

FUG

Fugitive Emissions

Valves

GAS LIQUID

Component counts estimated based on 40 CFR 98 Subpart W, Table W-1C counts for Western US Onshore oil production and estimated counts at Encana sites.

VOC emission leak factors from "Air Permit Technical Guidance for Chemical Sources; Equipment Leak Fugitives", TCEQ, October 2000.

NRSP, Fugitives VOC PTE ≥ 25 tpy, H2S ≥ 5 tpy

Pumps, compressors, agitator seals Connectors/flangesLDAR Program

Directed/Nondirected maintenance NA

NA2,000 ppm with approved gas analyzer

ORAs calculated per 40 CFR 60.18(i)(2)(B)

500 ppm with approved gas analyzerOR

As calculated per 40 CFR 60.18(i)(2)(B)

Weekly AVO

Quarterly monitoring with approved gas analyzerOR

At least bi-monthly monitoring using the Alternative Work Practice [FLIR camera, 40 CFR 60.18(g) - (i)]

OREquipped with a shaft sealing system that prevents or

detects emissions of VOC from the seal.

Quarterly monitoring of accessible valves with approved gas analyzer.

ORAt least bi-monthly monitoring using the Alternative Work

Practice [FLIR camera, 40 CFR 60.18(g) - (i)]

Leak detection limit

Leak Detection Program Requirements

TOC Uncontrolled Emissions



Internal Combustion Engine Emissions

Site Location Discharge Parameters Fuel Data

County 23.00 Natural Gas

Region 1.17 7443

New to this registration? 992 1211

9126.00 1

Engine Data Method of Emission Control Federal Standards

Yes/No

EPN Oxidation Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:

HAPs are included in Total VOC

Horsepower:

Fuel consumption (Btu/hp-hr): Fuel H2S content of 24 ppm is conservatively assumed.

Hours of operation per year:

Engine Type:

SO2 Mass Balance calculation for sour gas fuel:

Fuel Heat Value (Btu/SCF) 1,211 MW SO2 = 64.06 grams/moleFuel H2S content (mol%) 0.002 Ideal Gas Law 385.22 SCF/lb-mole Calculation Method:

Hourly emission rate calculation:

SO2 produced (lb/hr) = 0.034 - Hourly emission rate (lb/hr) = EF (lb/MMBtu) × Fuel Consumption (Btu/hp-hr) × Engine rated power (hp) / 1,000,000 (Btu/MMBtu)

SO2 produced (tpy) = 0.148 - Hourly emission rate (lb/hr) = EF (g/hp-hr) × Engine rated power (hp) / 453.59 (g/lb)

Annual emission rate (tpy) = Hourly Emission Rate (lb/hr) × Hours of operation per year (hrs/yr)

To Determine Emissions for Air Permitting

Manufacturer uncontrolled

emission factor

AP-42, Table 3.2-2

UncontrolledEmissions


Manufacturer controlled emission

factor

NSPS JJJJ emission limit

NRSP emission limit

Emissions Emissions

(g/hp-hr) (lb/MMBtu) (lb/hr) (tpy) (g/hp-hr) (g/hp-hr) (g/hp-hr) (lb/hr) (tpy)

VOC (NMNEHC) 0.48 0.118 1.460 6.396 0.70 0.70 1.00 0.700 g/hp-hr 2.464 10.794

NOx 0.50 4.08 1.521 6.663 1.00 1.00 1.00 g/hp-hr 3.042 13.326

CO 2.43 0.317 7.393 32.381 2.00 2.00 3.00 1.30 g/hp-hr 3.955 17.323

PM (condensable) 0.00991 0.102 0.446 0.00991 lb/MMBtu 0.102 0.446PM2.5/10 (filterable) 0.0000771 0.001 0.003 0.0000771 lb/MMBtu 0.001 0.003

PMTOTAL 0.00999 0.103 0.449 0.00999 lb/MMBtu 0.103 0.449SO2 0.000588 0.006 0.026 0.034 0.148

Formaldehyde (HCHO) 0.44 0.0528 1.339 5.863 0.11 0.110 g/hp-hr 0.335 1.466

Benzene 0.000440 0.005 0.020 0.000440 lb/MMBtu 0.005 0.020Other HAPs* 0.0182 0.187 0.819 0.0182 lb/MMBtu 0.187 0.819Total HAPs** 0.526 2.304

* Other HAPs AP-42 factor is the sum of AP-42 factors for all HAPs in the appropriate AP-42 table, with a rating C or better, excluding Formaldehyde and Benzene.** Total HAPs = Formaldehyde + Benzene + Other HAPs, and Total HAPs are included in VOC

Gas Compression

11/19/2014

JEF03175

G3516B

AP-42, Table 3.2-2 AP-42, Table 3.2-2

Manufacturer controlled emission factor

Mass balance

AP-42, Table 3.2-2

AP-42, Table 3.2-2

No

Emission factor used

units

AP-42, Table 3.2-2

Adjusted manufacturer controlled emission factor

NRSP emission limit


Emission Factor Source

4 Stroke, Lean-Burn

8760

7,443

1,380

Sulfur Content (grains/100scf)

TCEQ Region 13

NSPS Subpart JJJJ

Other (Specify)

Stratified Charge MACT Subpart ZZZZ

NSPS Subpart IIII

Karnes

Stack diameter (feet)

Stack height (feet)

Stage Temperature (°F)

Caterpillar

IP Compressor Engine

ENG-01

Yes

Catalyst Type

Parameter Adjustment

Exhaust Flowrate (cfm)

Fuel Type

Heat Value (Btu/scf)

Fuel Consumption (BTU/bhp-hr)

Does the VOC emission factor being used below include formaldehyde?






Region 1.17 8273


8761.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.64 0.0296 2.370 10.382 0.70 0.70 1.00 0.700 g/hp-hr 2.593 11.356

NOx 13.70 2.21 50.742 222.249 1.00 1.00 0.50 0.500 g/hp-hr 1.852 8.111

CO 12.70 3.72 47.038 206.027 2.00 2.00 3.00 1.30 g/hp-hr 4.815 21.089



Formaldehyde (HCHO) 0.0205 0.285 1.248 0.0205 lb/MMBtu 0.285 1.248



1,680

8,273

ENG-02 Catalyst Type NSPS Subpart JJJJ

Waukesha MACT Subpart ZZZZ

Sulfur Content (grains/100scf)Exhaust Flowrate (cfm)

Karnes Stack height (feet) Fuel Type

Yes

TCEQ Region 13 Stack diameter (feet) Fuel Consumption (BTU/bhp-hr)

Stage Temperature (°F) Heat Value (Btu/scf)

IP Compressor Engine Parameter Adjustment NSPS Subpart IIII

L7044GSI

5283703776

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Gas Compression

5/26/2014


Yes


units Emission Factor Source

AP-42, Table 3.2-3

AP-42, Table 3.2-3

AP-42, Table 3.2-3

Mass balance

AP-42, Table 3.2-3

AP-42, Table 3.2-3




AP-42, Table 3.2-3






Region 1.33 7425


9243.00 1


Yes/No

EPN Oxidation Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-2




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 1.05 0.118 3.195 13.992 0.70 0.70 1.00 0.700 g/hp-hr 2.282 9.994

NOx 0.50 4.08 1.521 6.663 1.00 1.00 1.00 g/hp-hr 3.042 13.326

CO 2.97 0.317 9.036 39.577 2.00 2.00 3.00 1.30 g/hp-hr 3.955 17.323






1,380

7,425


Caterpillar MACT Subpart ZZZZ



Yes



IP Compressor Engine Parameter Adjustment NSPS Subpart IIII

G3516B

JEF02950

Stratified Charge

Other (Specify)

8760

4 Stroke, Lean-Burn

Gas Compression

8/21/2014


No



AP-42, Table 3.2-2

AP-42, Table 3.2-2

AP-42, Table 3.2-2

Mass balance


AP-42, Table 3.2-2


NRSP emission limit


AP-42, Table 3.2-2






Region 1.33 7425


9243.00 1


Yes/No

EPN Oxidation Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-2




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 1.05 0.118 3.195 13.992 0.70 0.70 1.00 0.700 g/hp-hr 2.282 9.994

NOx 0.50 4.08 1.521 6.663 1.00 1.00 1.00 g/hp-hr 3.042 13.326

CO 2.97 0.317 9.036 39.577 2.00 2.00 3.00 1.30 g/hp-hr 3.955 17.323






1,380

7,425





Yes



Flash Compressor Engine Parameter Adjustment NSPS Subpart IIII

G3516B

JEF03024

Stratified Charge

Other (Specify)

8760

4 Stroke, Lean-Burn

Gas Compression

10/2/2014


No



AP-42, Table 3.2-2

AP-42, Table 3.2-2

AP-42, Table 3.2-2

Mass balance


AP-42, Table 3.2-2


NRSP emission limit


AP-42, Table 3.2-2






Region 1.17 7443


9126.00 1


Yes/No

EPN Oxidation Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-2




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.48 0.118 1.460 6.396 0.70 0.70 1.00 0.700 g/hp-hr 2.464 10.794

NOx 0.50 4.08 1.521 6.663 1.00 1.00 1.00 g/hp-hr 3.042 13.326

CO 2.43 0.317 7.393 32.381 2.00 2.00 3.00 1.30 g/hp-hr 3.955 17.323






1,380

7,443





Yes




G3516B

JEF02817

Stratified Charge

Other (Specify)

8760

4 Stroke, Lean-Burn

Gas Compression

6/2/2014


No



AP-42, Table 3.2-2

AP-42, Table 3.2-2

AP-42, Table 3.2-2

Mass balance


AP-42, Table 3.2-2


NRSP emission limit


AP-42, Table 3.2-2






Region 1.17 7744


8162.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.16 0.0296 0.593 2.596 0.70 0.70 1.00 0.700 g/hp-hr 2.593 11.356

NOx 13.30 2.21 49.260 215.760 1.00 1.00 0.50 0.500 g/hp-hr 1.852 8.111

CO 11.50 3.72 42.594 186.560 2.00 2.00 3.00 1.30 g/hp-hr 4.815 21.089






1,680

7,744


Waukesha MACT Subpart ZZZZ



Yes




L7044GSI

5283703759

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Gas Compression

5/20/2014


Yes



AP-42, Table 3.2-3

AP-42, Table 3.2-3

AP-42, Table 3.2-3

Mass balance

AP-42, Table 3.2-3

AP-42, Table 3.2-3




AP-42, Table 3.2-3






Region 0.25 9000


406.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.04 0.0296 0.006 0.026 0.04 0.700 g/hp-hr 0.118 0.519

NOx 14.40 2.21 2.159 9.455 2.80 2.80 2.80 g/hp-hr 0.420 1.839

CO 16.30 3.72 2.444 10.703 4.80 4.80 4.80 g/hp-hr 0.720 3.152


PMTOTAL 0.0195 0.012 0.052 0.0195 lb/MMBtu 0.012 0.052SO2 0.000588 3.60E-04 0.002 0.002 0.009

Formaldehyde (HCHO) 0.09 0.0205 0.013 0.059 0.090 g/hp-hr 0.013 0.059



68

9,000


Arrow MACT Subpart ZZZZ



Yes



Cooler Engine Parameter Adjustment NSPS Subpart IIII

VRG 330

P-5312C

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Gas Cooler

3/19/2010


No



AP-42, Table 3.2-3

AP-42, Table 3.2-3

AP-42, Table 3.2-3

Mass balance

Manufacturer uncontrolled emission factor

AP-42, Table 3.2-3

Adjusted manufacturer uncontrolled emission factor



AP-42, Table 3.2-3






Region 0.25 9000


406.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.04 0.0296 0.006 0.026 0.04 0.700 g/hp-hr 0.118 0.519

NOx 14.40 2.21 2.159 9.455 2.80 2.80 2.80 g/hp-hr 0.420 1.839

CO 16.30 3.72 2.444 10.703 4.80 4.80 4.80 g/hp-hr 0.720 3.152



Formaldehyde (HCHO) 0.09 0.0205 0.013 0.059 0.090 g/hp-hr 0.013 0.059



AP-42, Table 3.2-3

68

9,000


8760


No

AP-42, Table 3.2-3

AP-42, Table 3.2-3

AP-42, Table 3.2-3

Mass balance

Manufacturer uncontrolled emission factor

AP-42, Table 3.2-3

Adjusted manufacturer uncontrolled emission factor



MACT Subpart ZZZZ



Yes



Cooler Engine Parameter Adjustment NSPS Subpart IIII

VRG 330

P-5485C

Stratified Charge

Other (Specify)

Arrow

4 Stroke, Rich-Burn

Gas Cooler

6/17/2010








Region 0.33 8605


866.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 1.90 0.0296 0.787 3.449 0.50 0.70 1.00 0.700 g/hp-hr 0.290 1.271

NOx 5.90 2.21 2.445 10.711 1.00 1.00 1.00 1.00 g/hp-hr 0.414 1.815

CO 26.70 3.72 11.066 48.471 1.00 2.00 3.00 1.00 g/hp-hr 0.414 1.815






188

8,605

ENGVRU-01 Catalyst Type NSPS Subpart JJJJ

Cummins MACT Subpart ZZZZ



Yes



VRU Compressor Engine Parameter Adjustment NSPS Subpart IIII

G855

25396293

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Vapor Recovery

8/1/2014


Yes



AP-42, Table 3.2-3

AP-42, Table 3.2-3

AP-42, Table 3.2-3Mass balance

AP-42, Table 3.2-3

AP-42, Table 3.2-3


NRSP emission limit


AP-42, Table 3.2-3






Region 0.33 8605


866.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 1.90 0.0296 0.787 3.449 0.50 0.70 1.00 0.700 g/hp-hr 0.290 1.271

NOx 5.90 2.21 2.445 10.711 1.00 1.00 1.00 1.00 g/hp-hr 0.414 1.815

CO 26.70 3.72 11.066 48.471 1.00 2.00 3.00 1.00 g/hp-hr 0.414 1.815






188

8,605





Yes




G855

25398577

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Vapor Recovery

8/14/2014


Yes



AP-42, Table 3.2-3

AP-42, Table 3.2-3


AP-42, Table 3.2-3

AP-42, Table 3.2-3


NRSP emission limit


AP-42, Table 3.2-3






Region 0.25 8500


650.00 1


Yes/No

EPN NSCR Yes

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.40 0.0296 0.081 0.355 0.70 0.700 g/hp-hr 0.142 0.622

NOx 14.00 2.21 2.840 12.437 1.00 2.80 1.00 g/hp-hr 0.203 0.888

CO 11.00 3.72 2.231 9.772 2.00 4.80 2.00 g/hp-hr 0.406 1.777






92

8,500


GM MACT Subpart ZZZZ



Yes




Vortec 5.7L

27511157

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Vapor Recovery

3/5/2015


Yes



AP-42, Table 3.2-3

AP-42, Table 3.2-3


AP-42, Table 3.2-3

AP-42, Table 3.2-3




AP-42, Table 3.2-3






Region 0.25 8266


604.00 1


Yes/No

EPN NSCR No

Name No No

Manufacturer No Yes

Model Number AFRC

Serial Number

Manufacture Date

Last Rebuild Date

Application

Notes:


Horsepower:



Engine Type:









emission factor

AP-42, Table 3.2-3




factor


NRSP emission limit

Emissions Emissions


VOC (NMNEHC) 0.17 0.0296 0.044 0.194 0.50 0.500 g/hp-hr 0.130 0.570

NOx 11.60 2.21 3.018 13.218 0.50 2.00 2.00 g/hp-hr 0.520 2.279

CO 11.00 3.72 2.862 12.534 0.50 3.00 3.00 g/hp-hr 0.780 3.418






118

8,266





Yes




G8.3

46470205

Stratified Charge

Other (Specify)

8760

4 Stroke, Rich-Burn

Vapor Recovery

3/1/2005


Yes



AP-42, Table 3.2-3

AP-42, Table 3.2-3


AP-42, Table 3.2-3, with 75% catalytic reduction

AP-42, Table 3.2-3


NRSP emission limit

NRSP emission limit

AP-42, Table 3.2-3



Heaters-Boilers Emissions

Heater and Boiler Emission Calculations (fueled by natural gas)

EPN HTR-01

Name Heater Treater

Heater/Boiler rating (MMBtu/hr): 0.500

Rating above is (select from list): below 100 MMBtu/hr, uncontrolled

Operating hours/year: 8760

Fuel Heat Value (Btu/SCF): 1,211

Pollutant Emission Factor (lb/MMBtu) lb/hr tpy

VOC 0.00539 0.003 0.012

NOx 0.098039216 0.049 0.215

CO 0.0824 0.041 0.180

PM total 0.00745 0.004 0.016

PM condensable 0.00559 0.003 0.012

PM filterable 0.00186 0.001 0.004

SO2 0.000588 2.9E-04 0.001

Benzene 0.00000206 1.0E-06 4.5E-06

Formaldehyde 0.0000735 3.7E-05 1.6E-04

Other HAPs* 0.00000333 1.7E-06 7.3E-06

Total HAPs 3.9E-05 1.7E-04

* Other HAPs AP-42 factor is the sum of AP-42 factors from Table 1.4-3 with a rating C or better, excluding Formaldehyde and Benzene.

Fuel H2S content (mol %) = 0.0024 assumptions:

SO2 produced (lb/hr) = 0.0016 SO2 MW 64.06 lb/lb-mole

SO2 produced (tpy) = 0.0072 Ideal Gas Law 385.22 SCF/lb-mole

AP-42 emission factors for HAPs with a rating C or better were used for individual HAPs listed.

Total HAPs = Benzene + Formaldehyde + Other HAPs

HAPs are included in Total VOC.

Fuel H2S content of 24 ppm is conservatively assumed.

Emission Factors from AP-42, Chapter 1, Tables 1.4-1, 1.4-2 and 1.4-3. Modified from lb/MMCF to lb/MMBtu by dividing by 1020 MMBtu/ MMCF (per AP-42 guidance).

SO2 Mass Balance calculation:

If the heater/boiler is fueled by Sour Gas, cannot use emission factors above to calculate SO2 emissions, must use SO2 mass balance:

(assume uncontrolled, unless specifically stated otherwise)

Enter any notes here:





EPN HTR-02

Name Heater Treater






VOC 0.00539 0.003 0.012

NOx 0.098039216 0.049 0.215

CO 0.0824 0.041 0.180

PM total 0.00745 0.004 0.016

PM condensable 0.00559 0.003 0.012

PM filterable 0.00186 0.001 0.004

SO2 0.000588 2.9E-04 0.001

Benzene 0.00000206 1.0E-06 4.5E-06

Formaldehyde 0.0000735 3.7E-05 1.6E-04

Other HAPs* 0.00000333 1.7E-06 7.3E-06



















EPN HTR-03

Name Heater Treater






VOC 0.00539 0.003 0.012

NOx 0.098039216 0.049 0.215

CO 0.0824 0.041 0.180

PM total 0.00745 0.004 0.016

PM condensable 0.00559 0.003 0.012

PM filterable 0.00186 0.001 0.004

SO2 0.000588 2.9E-04 0.001

Benzene 0.00000206 1.0E-06 4.5E-06

Formaldehyde 0.0000735 3.7E-05 1.6E-04

Other HAPs* 0.00000333 1.7E-06 7.3E-06



















EPN HTR-04

Name Heater Treater






VOC 0.00539 0.003 0.012

NOx 0.098039216 0.049 0.215

CO 0.0824 0.041 0.180

PM total 0.00745 0.004 0.016

PM condensable 0.00559 0.003 0.012

PM filterable 0.00186 0.001 0.004

SO2 0.000588 2.9E-04 0.001

Benzene 0.00000206 1.0E-06 4.5E-06

Formaldehyde 0.0000735 3.7E-05 1.6E-04

Other HAPs* 0.00000333 1.7E-06 7.3E-06



















EPN HTR-05

Name Heater Treater






VOC 0.00539 0.003 0.012

NOx 0.098039216 0.049 0.215

CO 0.0824 0.041 0.180

PM total 0.00745 0.004 0.016

PM condensable 0.00559 0.003 0.012

PM filterable 0.00186 0.001 0.004

SO2 0.000588 2.9E-04 0.001

Benzene 0.00000206 1.0E-06 4.5E-06

Formaldehyde 0.0000735 3.7E-05 1.6E-04

Other HAPs* 0.00000333 1.7E-06 7.3E-06



















EPN HTR-06

Name Heater Treater






VOC 0.00539 0.008 0.035

NOx 0.098039216 0.147 0.644

CO 0.0824 0.124 0.541

PM total 0.00745 0.011 0.049

PM condensable 0.00559 0.008 0.037

PM filterable 0.00186 0.003 0.012

SO2 0.000588 0.001 0.004

Benzene 0.00000206 3.1E-06 1.4E-05

Formaldehyde 0.0000735 1.1E-04 4.8E-04

Other HAPs* 0.00000333 5.0E-06 2.2E-05

Total HAPs 1.2E-04 0.001


















EPN HTR-07

Name Heater Treater






VOC 0.00539 0.008 0.035

NOx 0.098039216 0.147 0.644

CO 0.0824 0.124 0.541

PM total 0.00745 0.011 0.049

PM condensable 0.00559 0.008 0.037

PM filterable 0.00186 0.003 0.012

SO2 0.000588 0.001 0.004

Benzene 0.00000206 3.1E-06 1.4E-05

Formaldehyde 0.0000735 1.1E-04 4.8E-04

Other HAPs* 0.00000333 5.0E-06 2.2E-05



















EPN HTR-08

Name Heater Treater






VOC 0.00539 0.008 0.035

NOx 0.098039216 0.147 0.644

CO 0.0824 0.124 0.541

PM total 0.00745 0.011 0.049

PM condensable 0.00559 0.008 0.037

PM filterable 0.00186 0.003 0.012

SO2 0.000588 0.001 0.004

Benzene 0.00000206 3.1E-06 1.4E-05

Formaldehyde 0.0000735 1.1E-04 4.8E-04

Other HAPs* 0.00000333 5.0E-06 2.2E-05



















EPN HTR-09

Name Glycol Unit Reboiler






VOC 0.00539 0.004 0.018

NOx 0.098039216 0.074 0.322

CO 0.0824 0.062 0.271

PM total 0.00745 0.006 0.024

PM condensable 0.00559 0.004 0.018

PM filterable 0.00186 0.001 0.006

SO2 0.000588 4.4E-04 0.002

Benzene 0.00000206 1.5E-06 6.8E-06

Formaldehyde 0.0000735 5.5E-05 2.4E-04

Other HAPs* 0.00000333 2.5E-06 1.1E-05



















EPN HTR-10

Name Line Heater






VOC 0.00539 0.008 0.035

NOx 0.098039216 0.147 0.644

CO 0.0824 0.124 0.541

PM total 0.00745 0.011 0.049

PM condensable 0.00559 0.008 0.037

PM filterable 0.00186 0.003 0.012

SO2 0.000588 0.001 0.004

Benzene 0.00000206 3.1E-06 1.4E-05

Formaldehyde 0.0000735 1.1E-04 4.8E-04

Other HAPs* 0.00000333 5.0E-06 2.2E-05



















EPN CAT-HTR

Name Catalytic Heaters






VOC 0.00539 1.9E-04 0.001

NOx 0.098039216 0.004 0.015

CO 0.0824 0.003 0.013

PM total 0.00745 2.7E-04 0.001

PM condensable 0.00559 2.0E-04 0.001

PM filterable 0.00186 6.7E-05 2.9E-04

SO2 0.000588 2.1E-05 9.3E-05

Benzene 0.00000206 7.4E-08 3.2E-07

Formaldehyde 0.0000735 2.6E-06 1.2E-05

Other HAPs* 0.00000333 1.2E-07 5.3E-07















This source represents potential emissions from up to 12 - 3,000 Btu/hr catalytic heaters operating at the site.



FIN

EPN

Identifier

Glycol Dehydrator Unit Information

Emission Calculation Method:

Type of Glycol Used:

Annual Hours of Operation:

Hours of flaring (if applicable)

Dry Gas Flow Rate (MMSCF/day):

Location at site where gas was sampled:

Date of Sample:

Is sample site-specific or representative?

Wet Gas Temperature (°F):

Wet Gas Pressure (psig):

Lean Glycol Pump Type:

Number of Pump Strokes/Minute (if applicable):

Lean Glycol Flow Rate (gpm)

Flash Tank Temperature (°F)

Flash Tank Pressure (psig)

Glycol Dehydrator EmissionsCalculated Using GRI-GLYCalc or a Process Simulator

DEHY-01

4.08

26

40

110

1250

Flash Tank: FLR-02 Regenerator/Condenser: DEHY-01

gas injection

95

Site-specific

8760

Glycol Unit

Glycol Unit Inlet (ProMax)

ProMax V3.2

TEG

8760

NA

33.00



FIN

EPN

Identifier


DEHY-01


Glycol Unit

Glycol Unit - Flash Tank

Is there a flash tank?

lb/hr tpy

VOC (C3) 5.804 25.420

VOC (C4+) 6.480 28.384

VOC (Total) 12.284 53.804

Benzene 0.041 0.180

HAPs 0.319 1.399H2S 0 0

How are flash tank emissions controlled?

VOC (C3) Control Efficiency (%)

VOC (C4+) Control Efficiency (%)

VOC (Total) Control Efficiency (%)

Benzene and HAPs Control Efficiency (%)

H2S Control Efficiency (%)

VOC (C3) 0.058 0.254

VOC (C4+) 0.130 0.568

VOC (Total) 0.188 0.822

Benzene 0.001 0.004

HAPs 0.006 0.028H2S 0 0

98.0%

Flare

98.0%

98.5%

99.0%

98.0%

Yes

Uncontrolled FlashTank Emissions

Controlled FlashTank Emissions

(FIN/EPN: DEHY-01/FLR-02)



FIN

EPN

Identifier


DEHY-01


Glycol Unit

Glycol Unit - Regenerator/Condenser

lb/hr tpy

VOC (C3) 1.468 6.430

VOC (C4+) 4.690 20.540

VOC (Total) 6.158 26.970

Benzene 0.573 2.509

HAPs 1.372 6.009H2S 0 0

How are Condenser emissions controlled?

VOC (C3) Control Efficiency (%)


VOC (Total) Control Efficiency (%)

Benzene and HAPs Control Efficiency (%)


VOC (C3) 0.029 0.129

VOC (C4+) 0.094 0.411

VOC (Total) 0.123 0.539

Benzene 0.011 0.050

HAPs 0.027 0.120H2S 0 0

98.0%

Reboiler/Glowplug

98.0%

98.0%

98.0%

98.0%

Uncontrolled Condenser Emissions

Reboiler/Glowplug ControlledCondenser Emissions

(FIN/EPN: DEHY-01/DEHY-01)



FIN

EPN

Identifier


DEHY-01


Glycol Unit

Sum of Flash Tank and Regenerator/Condenser Emissions

lb/hr tpy

VOC 0.123 0.539

Benzene 0.011 0.050

Total HAPs 0.027 0.120H2S 0 0

VOC 0.188 0.822

Benzene 0.001 0.004

Total HAPs 0.006 0.028H2S 0 0

Federal Applicability

40 CFR Part 63 - Subpart HH

Is this subpart applicable?

If yes, how will compliance be achieved? If no, please explain why.

Affected source is exempt from control requirements per 40 CFR 63.764 (e)(1)(ii); benzene emissions are less thank 0.90 Mg/yr (1.0 tpy).

Maintenance of records to support determination of exemption are required under §63.774(d)(1)(ii).


All area sources, with TEG dehydration units, will have some requirements under this rule. Emission reduction requirements may apply or only recordkeeping requirements may apply.

Yes

Throughput is 3 MMscf/day or greater AND Uncontrolled Benzene emissions are 1.0 tpy or greater. Emissions reduction requirements of HH apply, but this does not necessarily mean control.

Controlled emissions are emissions after any applied controls. If emissions are totally uncontrolled, then controlled emissions will be equal to uncontrolled emissions

Dehydration Unit Emissions(FIN/EPN: DEHY-01/DEHY-01)

Controlled DehydrationUnit Emissions

(FIN/EPN: DEHY-01/FLR-02)



Tank Emissions - AP-42Breathing Working Losses From Storage Tanks

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Variable Reference Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual

FIN OILTK-01 OILTK-02 OILTK-03 OILTK-04 OILTK-05 OILTK-06 OILTK-07 OILTK-08 OILTK-09 OILTK-10 OILTK-11 OILTK-12 OILTK-13 OILTK-14

Tank contents Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate

Tank Type VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR

Throughput Q gal 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500

Height (VFR) / Length (HFR) HS ft 16 16 16 16 16 16 16 16 16 16 16 16 16 16

Average Liquid Height HL ft 8 8 8 8 8 8 8 8 8 8 8 8 8 8

Diameter D ft 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6

Tank Capacity TCG bbl 500 500 500 500 500 500 500 500 500 500 500 500 500 500

Tank Max Liquid Volume HLX gal 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000

Turnovers N Eq. 7.1-30 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44

Maximum Pump Rate FRM gal/hr 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500

Roof Outage HRO ft 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16

Vapor Space Outage HVO ft 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16

Breather Vent Vacuum Setting psig -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03

Breather Vent Presure Setting psig 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03

Paint Color Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan

Paint Condition Good Good Good Good Good Good Good Good Good Good Good Good Good Good

Paint Solar Absorptance α 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43

Meteorological data city* San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX

Daily Total Solar Insolation Factor I Btu/ft2 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87

Atmospheric Pressure psia 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33

Daily Maximum Ambient Temperature TAX F 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51

Daily Minimum Ambient Temperature TAN F 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73

Daily Ambient Temp. Change ∆TA Eq. 7.1-12 R 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78

Daily Avg. Ambient Temperature TAA Eq. 7.1-27 R 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29

Liquid Bulk Temperature TB Eq. 7.1-28 R 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87

Daily Avg. Liquid Surface Temperature TLA Eq. 7.1-26 R 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50

Daily Max. Avg. Liq. Surf. Temp. TLX Fig. 7.1-17 R 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15

Daily Min. Avg. Liq. Surf. Temp. TLN Fig. 7.1-17 R 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86

Daily Vapor Temperature Range ∆TV Eq. 7.1-8 R 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57

AP-42 Product Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5

Vapor Molecular Wt. MV lb/lb-mole 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00

Vapor Pressure Method AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42True Vapor Pressure @ TLA PVA Tbl. 7.1-2 psia 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62True Vapor Pressure @ TLX PVX Tbl. 7.1-2 psia 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26True Vapor Pressure @ TLN PVN Tbl. 7.1-2 psia 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08

Daily Vapor Pressure Range ∆PV Eq. 7.1-9 psia 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19

Working Loss Product Factor KE Eq. 7.1-7 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17

Vented Vapor Saturation Factor KS Eq. 7-1.20 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39

Turnover Factor KN 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26

Working Loss Product Factor KP 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75

Vapor Space Volume VV Eq. 7.1-3 ft3 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14

Vapor Density WV Eq. 7.1-21 lb/ft3 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03

Percent Reduction for Produced Water Tank Calc. as Oil/Cond. (%) 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0% 0%

Emissions Calculations lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

Breathing 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595

Working 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878

Total 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473

Breathing 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625

Working 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021

Total 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646

THC 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25%

VOC (C3) 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55%

VOC (C4+) 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00%

VOC 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55%

Benzene 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11%

H2S 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01%

Total HAPs† 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37%

VOC (C3) 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822

VOC (C4+) 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568

Benzene 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004

H2S 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04

Total HAPs† 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086

* Meteorological data from Tanks 4.0 database

** Hourly emissions calculated per TCEQ guidance, APDG 6250, September 2014

Parameter Name

† Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC

Uncontrolled Emissions

Tank Vapor weight %s

Total Stream Uncontrolled

Total HC Uncontrolled**

UnitsAP-42

Variable


Tank Emissions - AP-42Breathing Working Losses From Storage Tanks

Variable Reference

FIN

Tank contents

Tank Type

Throughput Q gal

Height (VFR) / Length (HFR) HS ft

Average Liquid Height HL ft

Diameter D ft

Tank Capacity TCG bbl

Tank Max Liquid Volume HLX gal

Turnovers N Eq. 7.1-30

Maximum Pump Rate FRM gal/hr

Roof Outage HRO ft

Vapor Space Outage HVO ft

Breather Vent Vacuum Setting psig

Breather Vent Presure Setting psig

Paint Color

Paint Condition

Paint Solar Absorptance α

Meteorological data city*

Daily Total Solar Insolation Factor I Btu/ft2

Atmospheric Pressure psia

Daily Maximum Ambient Temperature TAX F

Daily Minimum Ambient Temperature TAN F

Daily Ambient Temp. Change ∆TA Eq. 7.1-12 R

Daily Avg. Ambient Temperature TAA Eq. 7.1-27 R

Liquid Bulk Temperature TB Eq. 7.1-28 R

Daily Avg. Liquid Surface Temperature TLA Eq. 7.1-26 R

Daily Max. Avg. Liq. Surf. Temp. TLX Fig. 7.1-17 R

Daily Min. Avg. Liq. Surf. Temp. TLN Fig. 7.1-17 R

Daily Vapor Temperature Range ∆TV Eq. 7.1-8 R

AP-42 Product

Vapor Molecular Wt. MV lb/lb-mole

Vapor Pressure Method True Vapor Pressure @ TLA PVA Tbl. 7.1-2 psiaTrue Vapor Pressure @ TLX PVX Tbl. 7.1-2 psiaTrue Vapor Pressure @ TLN PVN Tbl. 7.1-2 psia

Daily Vapor Pressure Range ∆PV Eq. 7.1-9 psia

Working Loss Product Factor KE Eq. 7.1-7

Vented Vapor Saturation Factor KS Eq. 7-1.20

Turnover Factor KN

Working Loss Product Factor KP

Vapor Space Volume VV Eq. 7.1-3 ft3

Vapor Density WV Eq. 7.1-21 lb/ft3

Percent Reduction for Produced Water Tank Calc. as Oil/Cond. (%)

Emissions Calculations

Breathing

Working

Total

Breathing

Working

Total

THC

VOC (C3)

VOC (C4+)

VOC

Benzene

H2S

Total HAPs†

VOC (C3)

VOC (C4+)

Benzene

H2S

Total HAPs†

* Meteorological data from Tanks 4.0 database

** Hourly emissions calculated per TCEQ guidance, APDG 6250, September 2014

Parameter Name

† Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC


Tank Vapor weight %s

Total Stream Uncontrolled

Total HC Uncontrolled**

UnitsAP-42

Variable

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Drip (Oil/Cond.) Tank


Produced Water Tank

Produced Water Tank

Produced Water Tank

Produced Water Tank

Produced Water Tank

Oil/Condensate Tank

Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual

OILTK-15 OILTK-16 OILTK-17 OILTK-18 OILTK-19 OILTK-20 OILTK-21 OILTK-22 PWTK-01 PWTK-02 PWTK-03 PWTK-04 PWTK-05 OILTK-23

Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Drip (Oil/Cond.) Drip (Oil/Cond.) Produced Water Produced Water Produced Water Produced Water Produced Water Oil/Condensate

VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR VFR

24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 24,500 6,898,500 32 141,803 32 141,803 10,500 10,731,000 10,500 10,731,000 10,500 10,731,000 10,500 10,731,000 10,500 10,731,000 24,500 137,970,000

16 16 16 16 16 16 16 16 16 16 16 16 16 40

8 8 8 8 8 8 8 8 8 8 8 8 8 20

15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 15.6 46.5

500 500 500 500 500 500 500 500 500 500 500 500 500 1000

21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 21000 42000

1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 1.17 328.44 0.00 6.75 0.00 6.75 0.50 510.91 0.50 510.91 0.50 510.91 0.50 510.91 0.50 510.91 0.58 164.22

24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 24500 32.375 32.375 32.375 32.375 10500 10500 10500 10500 10500 10500 10500 10500 10500 10500 24500 24500

0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.16 0.48

8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 8.16 20.48

-0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03 -0.03

0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03 0.03

Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan Tan

Good Good Good Good Good Good Good Good Good Good Good Good Good Good

0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43 0.43

San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX San Antonio, TX

2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87 2173.93 1568.87

14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33 14.33

95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51 95.30 79.51

75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73 75.00 57.73

20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78 20.30 21.78

544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29 544.82 528.29

546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87 546.40 529.87

553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50 553.09 534.50

563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15 563.29 543.15

542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86 542.89 525.86

40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57 40.79 34.57

Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5 Crude oil RVP 5

50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00 50.00

AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42 AP-42

5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62 5.14 3.62

6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26 6.24 4.26

4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08 4.24 3.08

1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19 1.99 1.19

0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17 0.28 0.17

0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.31 0.39 0.15 0.20

1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 0.26 1.00 1.00 1.00 1.00 1.00 0.23 1.00 0.23 1.00 0.23 1.00 0.23 1.00 0.23 1.00 0.35

0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75 0.75

1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 1560.14 34787.12

0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03 0.04 0.03

0% 0% 0% 0% 0% 0% 0% 0% 99% 99% 99% 99% 99% 0%

lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.248 0.595 0.002 0.006 0.002 0.006 0.002 0.006 0.002 0.006 0.002 0.006 2.711 6.906

168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 168.937 2.878 0.223 0.229 0.223 0.229 0.724 0.039 0.724 0.039 0.724 0.039 0.724 0.039 0.724 0.039 168.937 3.896

168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 168.937 3.473 0.248 0.824 0.248 0.824 0.724 0.045 0.724 0.045 0.724 0.045 0.724 0.045 0.724 0.045 168.937 10.802

0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.248 0.595 0.248 0.595 0.003 0.006 0.003 0.006 0.003 0.006 0.003 0.006 0.003 0.006 2.846 7.250

177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 0.223 0.229 0.223 0.229 0.760 0.041 0.760 0.041 0.760 0.041 0.760 0.041 0.760 0.041 177.361 4.091

177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 0.248 0.824 0.248 0.824 0.760 0.047 0.760 0.047 0.760 0.047 0.760 0.047 0.760 0.047 177.361 11.341

95.25% 95.25% 95.25% 95.25% 95.25% 95.25% 100.00% 100.00% 95.25% 95.25% 95.25% 95.25% 95.25% 95.25%

22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 1.63% 1.63% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55%

43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 98.29% 98.29% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00%

65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 99.92% 99.92% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55%

0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.87% 0.87% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11%

0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.00% 0.00% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01%

2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 18.64% 18.64% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37%

39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 39.996 0.822 0.004 0.013 0.004 0.013 0.171 0.011 0.171 0.011 0.171 0.011 0.171 0.011 0.171 0.011 39.996 2.557

76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 76.271 1.568 0.244 0.810 0.244 0.810 0.327 0.020 0.327 0.020 0.327 0.020 0.327 0.020 0.327 0.020 76.271 4.877

0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.199 0.004 0.002 0.007 0.002 0.007 0.001 5.31E-05 0.001 5.31E-05 0.001 5.31E-05 0.001 5.31E-05 0.001 5.31E-05 0.199 0.013

0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 0.021 4.34E-04 2.45E-07 8.14E-07 2.45E-07 8.14E-07 0.009 0.001 0.009 0.001 0.009 0.001 0.009 0.001 0.009 0.001 0.021 0.001

4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 4.207 0.086 0.046 0.154 0.046 0.154 0.018 0.001 0.018 0.001 0.018 0.001 0.018 0.001 0.018 0.001 4.207 0.269



Flash Losses From Storage Tanks

Gas Oil Ratio (GOR) Method

Tank Identifier Drip (Oil/Cond.) Tank Drip (Oil/Cond.) Tank

FIN OILTK-21 OILTK-22

Flash Gas CompositionHeat value(Btu/scf)

MW(lb/lb-mol)

Mol % Wt.% Mol % Wt.%

nitrogen 0 28.01 0.00% 0.00% 0.00% 0.00%CO2 0 44.01 0.14% 0.11% 0.14% 0.11%

H2S 586.8 34.08 0.01% 0.00% 0.01% 0.00%

methane (C1) 909.4 16.04 0.44% 0.12% 0.44% 0.12%

ethane (C2) 1618.7 30.07 6.92% 3.66% 6.92% 3.66%

propane (C3) 2314.9 44.10 27.77% 21.56% 27.77% 21.56%

iso-butane (C4) 3000.4 58.12 13.18% 13.49% 13.18% 13.49%

nor-butane (C4) 3010.8 58.12 26.58% 27.21% 26.58% 27.21%

iso-pentane (C5) 3699 72.15 9.82% 12.48% 9.82% 12.48%

nor-pentane (C5) 3706.9 72.15 8.16% 10.37% 8.16% 10.37%

hexanes (C6) 4403.8 86.17 3.37% 5.11% 3.37% 5.11%

heptanes (C7) 5100 100.20 1.09% 1.93% 1.09% 1.93%

octanes (C8) 5796.1 114.23 0.20% 0.40% 0.20% 0.40%

nonanes (C9) 6493.2 128.26 0.02% 0.04% 0.02% 0.04%

decanes (C10+) 7189.6 142.29 0.00% 0.00% 0.00% 0.00%

n-hexanes 4403.8 86.17 1.89% 2.86% 1.89% 2.86%

2,2,4-trimethylpentane 5559.2 114.23 0.00% 0.00% 0.00% 0.00%

benzene 3590.9 78.11 0.19% 0.26% 0.19% 0.26%

toluene 4273.6 92.14 0.19% 0.30% 0.19% 0.30%

ethylbenzene 4970.5 106.17 0.01% 0.02% 0.01% 0.02%

xylenes (M,P,O) 4958.2 106.17 0.04% 0.08% 0.04% 0.08%

Flash Gas MW lb/lb-mol 56.79 56.79

GOR (scf of flash gas/bbl) scf/bbl 114.7 114.7

Production bbl/hr bbl/yr bbl/hr bbl/yr

Amount of liquid flashed 0.8 3376.3 0.8 3376.3Percent Reduction for Produced Water Tank

Calculation as Oil/Condensate0% 0%

Emissions Calculations lb/hr tpy lb/hr tpyTotal Uncontrolled Emissions

(After % reduction for Produced Water)13.037 28.551 13.037 28.551

VOC (C3) 21.56% 21.56%VOC (C4+) 74.54% 74.54%

VOC 96.10% 96.10%

Benzene 0.26% 0.26%H2S 0.00% 0.00%

Total HAPs* 3.52% 3.52%

VOC (C3) 2.811 6.157 2.811 6.157

VOC (C4+) 9.718 21.282 9.718 21.282

VOC 12.529 27.438 12.529 27.438

Benzene 0.033 0.073 0.033 0.073H2S 4.66E-04 0.001 4.66E-04 0.001

Total HAPs* 0.458 1.004 0.458 1.004

Tank Emissions


Flash Gas Composition(Wt.%)

* Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC



Tank Emissions Summary

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

FIN OILTK-01 OILTK-02 OILTK-03 OILTK-04 OILTK-05 OILTK-06 OILTK-07 OILTK-08 OILTK-09 OILTK-10 OILTK-11 OILTK-12 OILTK-13 OILTK-14

EPN FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02

Tank Contents Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate

CIN VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU

Capture Efficiency % 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%% of time during VRU capture that vapors are

routed to combustion control device100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100%

Downtime (hrs/year) 876 876 876 876 876 876 876 876 876 876 876 876 876 876Hours of VRU capture 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884

Capture Efficiency % 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100%Hours of capture by control device only

(hrs/year)**876 876 876 876 876 876 876 876 876 876 876 876 876 876

VOC (C3) Control Efficiency (%) 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99%VOC (C4+) Control Efficiency (%) 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%

H2S Control Efficiency (%) 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%

Total hours of combustion control 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760

Emissions Calculations lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

Breathing 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625

Working 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021

Flashing 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

Worst case total † 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646

VOC (C3) 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55%

VOC (C4+) 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00%

VOC 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55%

Benzene 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11%H2S 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01%

Total HAPs ‡‡ 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37%

VOC (C3) 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

VOC (C4+) 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

VOC 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

Benzene 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

H2S 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

Total HAPs ‡‡ 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

VOC 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043

Benzene 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05

H2S 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06

Total HAPs ‡‡ 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002

VOC 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039

Benzene 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05H2S 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06

Total HAPs ‡‡ 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002

Notes:

Uncontrolled/Uncaptured Totals

lb/hr tpy

VOC 2.706 2.014

Benzene 0.005 0.005H2S 0.001 0.000

Total HAPs* 0.100 0.078

Post-control Totals

lb/hr tpy

VOC 4.183 1.890

Benzene 0.009 0.005H2S 0.001 0.000

Total HAPs* 0.184 0.085

** Does not include hours that the VRU vapors are routed to the combustion device.† Includes flash emissions and the maximum of breathing and working emissions.†† For total uncaptured losses, the total lb/hr is the sum of breathing losses from all tanks, plus working and flashing emissions from the worst Oil/Condensate tank and worst Produced Water tank.‡ For total uncaptured losses, the total lb/hr is the sum of breathing losses from all tanks, plus working and flashing emissions from tanks OILTK-01, OILTK-21, PWTK-01, OILTK-23.‡‡ Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC.

Post-Combustion Control Device Emissions

(FIN/EPN: Tank FIN/FLR-02)‡

VRU(CIN: VRU)

CombustionControlDevice

Total Uncaptured Emissions (FIN/EPN: Tank FIN/Tank FIN)

††

Total Stream Uncontrolled Emissions (After any % reduction taken for

produced water)

Breathing/Working

Flashing

Stream Composition

(Wt.%)



Tank Emissions Summary

FIN

EPN

Tank Contents

CIN

Capture Efficiency %% of time during VRU capture that vapors are

routed to combustion control deviceDowntime (hrs/year)

Hours of VRU capture

Capture Efficiency %Hours of capture by control device only

(hrs/year)**VOC (C3) Control Efficiency (%)



Total hours of combustion control

Emissions Calculations

Breathing

Working

Flashing

Worst case total †

VOC (C3)

VOC (C4+)

VOC

BenzeneH2S

Total HAPs ‡‡

VOC (C3)

VOC (C4+)

VOC

Benzene

H2S

Total HAPs ‡‡

VOC

Benzene

H2S

Total HAPs ‡‡

VOC

BenzeneH2S

Total HAPs ‡‡

Uncontrolled/Uncaptured Totals

lb/hr tpy

VOC 2.706 2.014

Benzene 0.005 0.005H2S 0.001 0.000

Total HAPs* 0.100 0.078

Post-control Totals

lb/hr tpy

VOC 4.183 1.890

Benzene 0.009 0.005H2S 0.001 0.000

Total HAPs* 0.184 0.085

Post-Combustion Control Device Emissions

(FIN/EPN: Tank FIN/FLR-02)‡

VRU(CIN: VRU)

CombustionControlDevice

Total Uncaptured Emissions (FIN/EPN: Tank FIN/Tank FIN)

††

Total Stream Uncontrolled Emissions (After any % reduction taken for

produced water)

Breathing/Working

Flashing

Stream Composition

(Wt.%)

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank

Oil/Condensate Tank



Produced Water Tank

Produced Water Tank

Produced Water Tank

Produced Water Tank

Produced Water Tank

Oil/Condensate Tank

OILTK-15 OILTK-16 OILTK-17 OILTK-18 OILTK-19 OILTK-20 OILTK-21 OILTK-22 PWTK-01 PWTK-02 PWTK-03 PWTK-04 PWTK-05 OILTK-23

FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02 FLR-02

Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Oil/Condensate Drip (Oil/Cond.) Drip (Oil/Cond.) Produced Water Produced Water Produced Water Produced Water Produced Water Oil/Condensate

VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU VRU

98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%

100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100%

876 876 876 876 876 876 876 876 876 876 876 876 876 8767884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884 7884

100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100% 100%

876 876 876 876 876 876 876 876 876 876 876 876 876 876

99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99% 99%98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%

98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98% 98%

8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760 8760

lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.261 0.625 0.248 0.595 0.248 0.595 0.003 0.006 0.003 0.006 0.003 0.006 0.003 0.006 0.003 0.006 2.846 7.250

177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 177.361 3.021 0.223 0.229 0.223 0.229 0.760 0.041 0.760 0.041 0.760 0.041 0.760 0.041 0.760 0.041 177.361 4.091

0 0 0 0 0 0 0 0 0 0 0 0 13.037 28.551 13.037 28.551 0 0 0 0 0 0 0 0 0 0 0 0

177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 177.361 3.646 13.285 29.376 13.285 29.376 0.760 0.047 0.760 0.047 0.760 0.047 0.760 0.047 0.760 0.047 177.361 11.341

22.55% 22.55% 22.55% 22.55% 22.55% 22.55% 1.63% 1.63% 22.55% 22.55% 22.55% 22.55% 22.55% 22.55%

43.00% 43.00% 43.00% 43.00% 43.00% 43.00% 98.29% 98.29% 43.00% 43.00% 43.00% 43.00% 43.00% 43.00%

65.55% 65.55% 65.55% 65.55% 65.55% 65.55% 99.92% 99.92% 65.55% 65.55% 65.55% 65.55% 65.55% 65.55%

0.11% 0.11% 0.11% 0.11% 0.11% 0.11% 0.87% 0.87% 0.11% 0.11% 0.11% 0.11% 0.11% 0.11%

0.01% 0.01% 0.01% 0.01% 0.01% 0.01% 0.00% 0.00% 0.01% 0.01% 0.01% 0.01% 0.01% 0.01%

2.37% 2.37% 2.37% 2.37% 2.37% 2.37% 18.64% 18.64% 2.37% 2.37% 2.37% 2.37% 2.37% 2.37%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 21.56% 21.56% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 74.54% 74.54% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 96.10% 96.10% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.26% 0.26% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

0.00% 0.00% 0.00% 0.00% 0.00% 0.00% 3.52% 3.52% 0.00% 0.00% 0.00% 0.00% 0.00% 0.00%

2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 2.325 0.043 0.256 0.509 0.256 0.509 0.010 0.001 0.010 0.001 0.010 0.001 0.010 0.001 0.010 0.001 2.325 0.134

0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.004 7.36E-05 0.001 0.001 0.001 0.001 1.71E-05 9.55E-07 1.71E-05 9.55E-07 1.71E-05 9.55E-07 1.71E-05 9.55E-07 1.71E-05 9.55E-07 0.004 2.29E-04

4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 4.23E-04 7.82E-06 9.32E-06 1.84E-05 9.32E-06 1.84E-05 1.81E-04 1.01E-05 1.81E-04 1.01E-05 1.81E-04 1.01E-05 1.81E-04 1.01E-05 1.81E-04 1.01E-05 4.23E-04 2.43E-05

0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.010 0.021 0.010 0.021 3.61E-04 2.02E-05 3.61E-04 2.02E-05 3.61E-04 2.02E-05 3.61E-04 2.02E-05 3.61E-04 2.02E-05 0.084 0.005

1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 1.925 0.039 0.227 0.494 0.227 0.494 0.008 0.001 0.008 0.001 0.008 0.001 0.008 0.001 0.008 0.001 1.925 0.121

0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.004 8.03E-05 0.001 0.002 0.001 0.002 1.71E-05 1.04E-06 1.71E-05 1.04E-06 1.71E-05 1.04E-06 1.71E-05 1.04E-06 1.71E-05 1.04E-06 0.004 2.50E-04

4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 4.23E-04 8.53E-06 9.32E-06 2.00E-05 9.32E-06 2.00E-05 1.81E-04 1.11E-05 1.81E-04 1.11E-05 1.81E-04 1.11E-05 1.81E-04 1.11E-05 1.81E-04 1.11E-05 4.23E-04 2.65E-05

0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.084 0.002 0.010 0.023 0.010 0.023 3.61E-04 2.20E-05 3.61E-04 2.20E-05 3.61E-04 2.20E-05 3.61E-04 2.20E-05 3.61E-04 2.20E-05 0.084 0.005

Notes: ** Does not include hours that the VRU vapors are routed to the combustion device.† Includes flash emissions and the maximum of breathing and working emissions.†† For total uncaptured losses, the total lb/hr is the sum of breathing losses from all tanks, plus working and flashing emissions from the worst Oil/Condensate tank and worst Produced Water tank.‡ For total uncaptured losses, the total lb/hr is the sum of breathing losses from all tanks, plus working and flashing emissions from tanks OILTK-01, OILTK-21, PWTK-01, OILTK-23.‡‡ Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC.



Loading Emissions

Source NameProduced Water

LoadingOil/Condensate Loading

FIN LOAD LOAD

EPN FLR-02 FLR-02

Product Produced Water Oil/Condensate

Number of loadouts per year 12243 2500

Tank Truck Collection Efficiency 70.0% 70.0%

Capture Efficiency % 100.0% 100.0%

VOC (C3) Control Efficiency (%) 99.0% 99.0%

VOC (C4+) Control Efficiency (%) 98.0% 98.0%

H2S Control Efficiency (%) 98.0% 98.0%

Total hours of combustion control 8,760 8,760

Hours Uncontrolled 0 0

Loading Loss Calculation Hourly Annual Hourly Annual

Percent Reduction for Produced Water Calculation as Oil/Condensate 99% 0%

S, Saturation Factor † dimensionless 0.6 0.6

M, Molecular Weight of Vapors †† lb/lb-mole 50 50

P, True vapor pressure of liquid loaded †† psia 6.24 3.62 6.24 3.62

T, Temperature of bulk liquid loaded †† °R 563.29 534.50 563.29 534.50

Loading Loss, LL (lbHC/1000 gal loaded) ‡ lbHC/1000 gal loaded 0.041 0.025 4.138 2.533

Loading Rate gal 5,040 61,704,720 37,800 18,900,000

Emission Calculations lb/hr tpy lb/hr tpy

Total HC Uncontrolled Emissions(After % reduction taken for produced water )

0.209 0.781 156.419 23.934

Total Stream Uncontrolled Emissions(After % reduction taken for produced water )

0.219 0.820 164.219 25.127

VOC (C3) 22.55% 22.55%

VOC (C4+) 43.00% 43.00%

Benzene 0.11% 0.11%

H2S 0.01% 0.01%

Total HAPs ‡‡ 2.37% 2.37%

Produced Water Loading Oil/Condensate Loading Totals

lb/hr tpy lb/hr tpy lb/hr tpy

VOC 0.043 0.161 32.296 4.942 32.339 5.103

Benzene 7.4E-05 2.8E-04 0.055 0.008 0.055 0.009

H2S 0.001 0.003 0.006 0.001 0.007 0.004

Total HAPs ‡‡ 0.002 0.006 1.169 0.179 1.170 0.185

VOC 0.002 0.006 1.248 0.191 1.250 0.197

Benzene 3.4E-06 1.3E-05 0.003 3.9E-04 0.003 4.1E-04

H2S 3.7E-05 1.4E-04 2.7E-04 4.2E-05 3.1E-04 1.8E-04

Total HAPs ‡‡ 7.3E-05 2.7E-04 0.055 0.008 0.055 0.009

† From AP-42, Table 5.2-1

†† From AP-42 Tanks Calculations (MV, TLX, TLA, PVX, PVA)

‡ From AP-42, Chapter 5, Section 5.2-4, LL = 12.46 × S × P × M / T

‡‡ Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC

Combustion Control Device

Stream Composition(Wt.%)

Total Stream Uncaptured Emissions(FIN/EPN: LOAD/LOAD)

Post-Combustion Control Device Emissions(FIN/EPN: LOAD/FLR-02)

Emissions Summary



Flare / Vapor Combustor Reference Page

Emissions Calculation Methods:

[1] • Hourly Stream Flow (lb/hr) = (lb/lb-mol) * (P) * (scf/hr) * / (R) * (T)

• Hourly Flow Rate (using GOR) (scf/hr) = GOR * Max throughput (bbl/hr)

• Annual Stream Flow (tpy) = (lb/lb-mol) * (P) * (scf/yr) * / (R) * (T) * 2000

• Annual Flow Rate (using GOR) (scf/yr) = GOR * Annual hourly throughput (bbl/hr) * Hrs/yr

[2] • Hourly Flow Rate (scf/hr) = Total lb/hr * T * R / P * Stream MW

• Annual Flow Rate (scf/yr) = Total tpy * T * R / P * Stream MW

• NOx/CO (lb/hr) = (scf/hr)*EF (lb/MMBtu) * HV (Btu/scf) / 10^6

• SO2 (lb/hr) = (H2S lb/hr)*(64 lb SO2/lb-mol)/(34.08 lb H2S/lb-mol)

Flare Tip Velocity Calculation Method:

Actual Flare Tip Velocity (ft/sec) = (scf/hr)*(1 hr/3600 sec)/(flare tip area)

Heat Content Requirement Calculation Method:

For SO2, Q = (0.53)*(105)*(lb/hr SO2)

TCEQ Flare Emission FactorsFlare Type Waste Gas NOx (lb/MMBTU) CO (lb/MMBTU)

High BTU (>1000 BTU/scf) 0.0485 0.3503Low Btu (192-1000 BTU/scf) 0.068 0.3465

High Btu (>1000 BTU/scf) 0.138 0.2755Low Btu (192-1000 BTU/scf) 0.0641 0.5496

Technical Guidance for Chemical Sources: Flares & Vapor Oxidizers, October 2000.

EPN FLR-01 FLR-02

Source Name Utility Flare Process FlareFlare Information (If Controlled by Flare)

Flare Steam Assisted (y or n) NO NO

Pilot or Auto-ignitor? Pilot Pilot

Pilot Flow (scf/hr): 50.00 50.00

Stack height (ft): 45 30

Flare Tip Diameter (in): 6 8

C1-C3 Destruction Efficiency (%): 99 99

C4+ Destruction Efficiency (%): 98 98

H2S Conversion Efficiency (%): 98 98

Actual Flare Tip Velocity

Total Gas Volume to Flare (scf/hr): 141,087.736 32,796.211

Flare Tip Diameter (ft) 0.50 0.67

Flare Tip Area (ft2) 0.196 0.349

Flare Tip Velocity (ft/sec): 199.598 26.098

40 CFR 60.18(c)(4) - Max Flare Tip Velocity (ft/sec)

Heating Value of Gas (Btu/scf) 1291 2023

Low BTU Gas (<1,000 Btu/scf) 60 60

High BTU Gas (>1,000 Btu/scf) 400 400

steam-assist

other



Flare / Vapor Combustor Emissions

[1] [1] [1] [1] Calculation Method

Flare PilotCompressors

Blowdowns/StartupsHeater Treaters Gas Separator Gas Totals

Hourly(Normal and AOS)

AnnualHourly(AOS)

AnnualHourly

(Normal)Hourly(AOS)

AnnualHourly

(Normal)Hourly(AOS)

AnnualHourly

(Normal)Hourly(AOS)

Annual

FLR-01 COMP-MSS PROD-GAS PROD-GAS FIN

Yes Yes Yes Yes Routed to Flare?

8,760 312 8,760 8,760 Hours/year Routed to Flare

Fuel Gas Analysis Gas analysis Flash analysis (HT GOR) Gas analysis Analysis Used

VOC (C3) wt% 12.91% 12.65% 20.35% 12.65% wt% VOC (C3)

VOC (C4+) wt% 14.36% 15.90% 29.83% 15.90% wt% VOC (C4+)

Benzene wt% 0.04% 0.05% 0.11% 0.05% wt% Benzene

H2S wt% 0.00% 0.01% 0.01% 0.01% wt% H2S

Total HAPs wt% 0.61% 0.83% 1.72% 0.83% wt% Total HAPs

scf/bbl scf/bbl GOR

lb/lb-mol 22.8 23.0 30.6 23.0 lb/lb-mol Stream MW

BTU/scf 1210.6 1224.1 1588.5 1224.1 1,291 1,290 1,291 BTU/scf

MMBTU 0.061 530 3.060 955 41.360 44.957 179,828 140.766 153.007 612,027 182.187 201.084 793,340 MMBTU

scf 50.00 438,000 2,500.00 780,000 26,037.74 28,301.89 113,207,547 115,000.00 125,000.00 500,000,000 141,087.74 155,851.89 614,425,547 scf Flow Rate

EMISSIONS

lb/hr(Normal and AOS)

tpylb/hr

(AOS)tpy

lb/hr(Normal)

lb/hr(AOS)

tpylb/hr

(Normal)lb/hr

(AOS)tpy

lb/hr(Normal)

lb/hr(AOS)

tpy

2.954 12.940 149.401 23.307 2067.797 2247.605 4495.210 6872.463 7470.068 14940.136 8,943.214 9,870.029 19,471.594Total Stream Flow (after any reduction

taken for PW)

0.381 1.671 18.905 2.949 420.887 457.486 914.972 869.628 945.247 1,890.495 1,290.896 1,422.020 2,810.087 VOC (C3)

0.424 1.858 23.757 3.706 616.767 670.399 1,340.798 1,092.801 1,187.828 2,375.655 1,709.992 1,882.407 3,722.017 VOC (C4+)

0.806 3.529 42.661 6.655 1,037.654 1,127.885 2,255.770 1,962.429 2,133.075 4,266.150 3,000.889 3,304.427 6,532.104 VOC

0.001 0.005 0.081 0.013 2.289 2.488 4.975 3.728 4.053 8.105 6.018 6.623 13.099 Benzene

1.06E-04 4.65E-04 0.014 0.002 0.293 0.319 0.638 0.630 0.685 1.370 0.924 1.018 2.010 H2S

0.018 0.079 1.242 0.194 35.485 38.571 77.141 57.133 62.102 124.203 92.636 101.932 201.617 Total HAPs

0.004 0.017 0.189 0.029 4.209 4.575 9.150 8.696 9.452 18.905 12.909 14.220 28.101 VOC (C3)

0.008 0.037 0.475 0.074 12.335 13.408 26.816 21.856 23.757 47.513 34.200 37.648 74.440 VOC (C4+)

0.012 0.054 0.664 0.104 16.544 17.983 35.966 30.552 33.209 66.418 47.109 51.868 102.541 VOC

2.42E-05 1.06E-04 0.002 2.53E-04 0.046 0.050 0.100 0.075 0.081 0.162 0.120 0.132 0.262 Benzene

2.12E-06 9.30E-06 2.74E-04 4.27E-05 0.006 0.006 0.013 0.013 0.014 0.027 0.018 0.020 0.040 H2S

3.60E-04 0.002 0.025 0.004 0.710 0.771 1.543 1.143 1.242 2.484 1.853 2.039 4.032 Total HAPs

0.008 0.037 0.422 0.066 5.708 6.204 12.408 19.426 21.115 42.230 25.142 27.750 54.740 NOx

0.017 0.073 0.843 0.132 11.395 12.386 24.771 38.781 42.153 84.307 50.193 55.399 109.283 CO

1.99E-04 0.001 0.026 0.004 0.551 0.599 1.197 1.184 1.286 2.573 1.734 1.911 3.775 SO2

Notes: Constants

527.67 T (absolute temperature - Rankine)10.73159 R (universal gas constant) - (psia*ft3)/(lbmolR)

14.7 P (Pressure (psia))

EPN:

Source Name:

H2S

Benzene

VOC

ControlledEmissions

VOC (C4+)

Utility Flare

FLR-01

Flow Rate

Heating Value

Stream MW

GOR

Hours/year Routed to Flare

Routed to Flare?

FIN

Analysis Used

StreamComposition

CO

SO2

VOC (C3)

NOx

Total HAPs

H2S

See Flare / Vapor Combustor Reference Page for calculation methods and equipment detailsHourly and annual individual stream contributions represented in calculations are to determine a worst-case PTE emission rate at EPN: FLR-01 during normal operations. Actual individual flow rates will vary. Encana will monitor total flow rate to the flare to ensure compliance with the standard permit.Annual emissions associated with FIN: PROD-GAS (AOS) are represented under normal operations with FIN/EPN: PROD-GAS/FLR-01.

VOC (C3)

Total Stream Flow (after any reduction taken for PW)


VOC (C4+)

Benzene

Total HAPs

VOC

StreamComposition

Heating Value

ControlledEmissions




Flare / Vapor Combustor Emissions

[1] [2] [2] [2] [2] [2] [2] [2] [1] [1] Calculation Method

Flare PilotTanks (B/W) - Produced

WaterTanks (B/W) -

Oil/CondensateTanks (B/W) - Drip

(Oil/Cond.)Tanks (Flash) - Drip

(Oil/Cond.)Truck Loading - Produced Water

Truck Loading - Oil/Condensate

Glycol UnitVapor Recovery Towers

GasDrip Vapor Recovery

Tower GasTotals

Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly Annual Hourly AnnualFLR-02 Multiple Tanks Multiple Tanks Multiple Tanks Multiple Tanks LOAD LOAD DEHY-01 VRT-GAS DRIPVRT-GAS FIN

Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Routed to Flare?

8,760 8,760 8,760 8,760 8,760 8,760 8,760 8,760 8,760 8,760 Hours/year Routed to Flare

Fuel Gas AnalysisBreathing/Working

AnalysisBreathing/Working

AnalysisDrip Liquid analysis

Flash analysis (DRIP GOR)

Breathing/Working Analysis

Breathing/Working Analysis

Glycol Unit (from ProMax) Flash analysis (VRT GOR)Flash analysis (Drip VRT

GOR) Analysis Used

VOC (C3) wt% 12.91% 22.55% 22.55% 1.63% 21.56% 22.55% 22.55% 18.90% 26.08% 29.20% wt% VOC (C3)

VOC (C4+) wt% 14.36% 43.00% 43.00% 98.29% 74.54% 43.00% 43.00% 21.10% 53.03% 56.36% wt% VOC (C4+)

Benzene wt% 0.04% 0.11% 0.11% 0.87% 0.26% 0.11% 0.11% 0.13% 0.21% 0.16% wt% BenzeneH2S wt% 0.00% 0.01% 0.01% 0.00% 0.00% 0.01% 0.01% 0.00% 0.01% 0.01% wt% H2S

Total HAPs wt% 0.61% 2.37% 2.37% 18.64% 3.52% 2.37% 2.37% 1.04% 3.24% 2.08% wt% Total HAPs

scf/bbl 114.7 48.8 143.4 scf/bbl GOR

lb/lb-mol 22.8 50.0 50.0 50.0 56.8 50.0 50.0 29.1 45.5 48.2 lb/lb-mol Stream MW

BTU/scf 1210.6 1869.3 1869.3 4270.2 2937.4 1869.3 1869.3 1389.8 2341.9 2495.4 2,278 2,023 BTU/scf

MMBTU 0.061 530 0.011 7 5.225 2,383 0.024 107 0.260 2,235 0.002 17 1.656 507 0.564 4,944 66.600 11,710 0.300 2,626 74.702 25,063 MMBTU

scf 50.00 438,000 5.96 3,579 2,795.00 1,274,954 5.54 24,948 88.44 760,778 1.18 8,849 885.65 271,029 406.07 3,557,134 28,438.27 5,000,000 120.11 1,052,182 32,796.21 12,391,452 scf Flow Rate

EMISSIONS

lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy

2.954 12.940 0.773 0.232 362.779 82.742 0.720 1.619 13.037 56.075 0.153 0.574 114.953 17.589 30.711 134.513 3358.947 295.284 15.016 65.772 3,900.044 667.342Total Stream Flow (after any reduction

taken for PW)

0.381 1.671 0.174 0.052 81.809 18.659 0.012 0.026 2.811 12.091 0.035 0.129 25.923 3.966 5.804 25.420 875.881 76.998 4.384 19.204 997.214 158.218 VOC (C3)

0.424 1.858 0.332 0.100 156.008 35.582 0.707 1.591 9.718 41.797 0.066 0.247 49.434 7.564 6.480 28.384 1,781.291 156.593 8.464 37.072 2,012.924 310.787 VOC (C4+)

0.806 3.529 0.507 0.152 237.817 54.241 0.719 1.618 12.529 53.889 0.100 0.376 75.357 11.530 12.284 53.804 2,657.172 233.591 12.848 56.276 3,010.139 469.006 VOC

0.001 0.005 0.001 2.60E-04 0.407 0.093 0.006 0.014 0.033 0.144 1.72E-04 0.001 0.129 0.020 0.041 0.180 7.107 0.625 0.023 0.102 7.749 1.183 Benzene

1.06E-04 4.65E-04 0.009 0.003 0.043 0.010 7.11E-07 1.60E-06 4.66E-04 0.002 0.002 0.007 0.014 0.002 0 0 0.438 0.039 0.001 0.006 0.508 0.069 H2S

0.018 0.079 0.018 0.006 8.606 1.963 0.134 0.302 0.458 1.971 0.004 0.014 2.727 0.417 0.319 1.399 108.725 9.558 0.312 1.368 121.322 17.076 Total HAPs

0.004 0.017 0.002 0.001 0.818 0.187 1.17E-04 2.64E-04 0.028 0.121 3.46E-04 0.001 0.259 0.040 0.058 0.254 8.759 0.770 0.044 0.192 9.972 1.582 VOC (C3)

0.008 0.037 0.007 0.002 3.120 0.712 0.014 0.032 0.194 0.836 0.001 0.005 0.989 0.151 0.130 0.568 35.626 3.132 0.169 0.741 40.258 6.216 VOC (C4+)

0.012 0.054 0.008 0.003 3.938 0.898 0.014 0.032 0.222 0.957 0.002 0.006 1.248 0.191 0.188 0.822 44.385 3.902 0.213 0.933 50.231 7.798 VOC

2.42E-05 1.06E-04 1.73E-05 5.21E-06 0.008 0.002 1.25E-04 2.80E-04 0.001 0.003 3.44E-06 1.29E-05 0.003 3.95E-04 0.001 0.004 0.142 0.012 4.66E-04 0.002 0.155 0.024 Benzene

2.12E-06 9.30E-06 1.84E-04 5.53E-05 0.001 1.97E-04 1.42E-08 3.20E-08 9.31E-06 4.01E-05 3.65E-05 1.37E-04 2.74E-04 4.19E-05 0 0 0.009 0.001 2.83E-05 1.24E-04 0.010 0.001 H2S

3.60E-04 0.002 3.67E-04 1.10E-04 0.172 0.039 0.003 0.006 0.009 0.039 7.27E-05 2.72E-04 0.055 0.008 0.006 0.028 2.175 0.191 0.006 0.027 2.426 0.342 Total HAPs

0.008 0.037 0.002 4.62E-04 0.721 0.164 0.003 0.007 0.036 0.154 3.05E-04 0.001 0.228 0.035 0.078 0.341 9.191 0.808 0.041 0.181 10.309 1.729 NOx

0.017 0.073 0.003 0.001 1.439 0.328 0.007 0.015 0.072 0.308 0.001 0.002 0.456 0.070 0.155 0.681 18.348 1.613 0.083 0.362 20.580 3.452 CO

1.99E-04 0.001 0.017 0.005 0.081 0.019 1.34E-06 3.00E-06 0.001 0.004 0.003 0.013 0.026 0.004 0 0 0.823 0.072 0.003 0.012 0.954 0.129 SO2

Notes: Constants

527.67 T (absolute temperature - Rankine)10.73159 R (universal gas constant) - (psia*ft3)/(lbmolR)

14.7 P (Pressure (psia))


VOC (C3)

VOC (C4+)

VOC

VOC

BenzeneH2S

Total HAPs

NOx

FIN

Total Stream Flow (after any reduction taken for PW)

Hours/year Routed to Flare

Analysis Used

StreamComposition

StreamComposition

GOR

Stream MW

Heating Value Heating Value

Flow Rate

FLR-02

Process Flare

See Flare / Vapor Combustor Reference Page for calculation methods and equipment detailsFlow rate assumptions for the following sources: VRT-GAS = GOR (scf/bbl) x Oil/Condensate Throughput (bbl/hr); DRIPVRT-GAS = GOR (scf/bbl) x Drip Throughput (bbl/hr)

Source Name:

EPN:

Routed to Flare?

BenzeneH2S

Total HAPs

ControlledEmissions

VOC (C3)

ControlledEmissions


VOC (C4+)

COSO2



Planned MSS Emissions - Heater/Boiler Degassing

FIN

Identifier

Calculation Basis:

Constants and Variables: 565.49 (Assume 20' x 6' heater treater = 100 bbl)16.70 (Pressure after well is shut-in and gas is bled to flare) 14.70

100.00

10.73

1

Duration of depressurization (hours): 8 (per heater treater)1 (per heater treater)

16 (conservatively assumed)6.24 (from AP-42 Tanks calculation)

30.59 (from HT gas composition)0.502 (from HT gas composition)0.001 (from HT gas composition)0.017 (from HT gas composition)

1.4E-04 (from HT gas composition)

Emission Calculation - From Depressurizing Vessel:

Total gas vented to atmosphere (lb) = (Pressure Difference x Volume) / (Gas Constant x Temperature [°R]) * MW

= 2.00 psia 565.49 ft3 30.59 lb

10.73 ft3*psi/°R*lb-mol 559.67 ° R lb-mol

Emission Calculation - From Opening Vessel:Total gas vented to atmosphere (lb) = (Pressure Difference x Volume) / (Gas Constant x Temperature [°R]) * MW

= 14.70 psi 565.49 ft3 30.59 lb

10.73 ft3*psi/°R*lb-mol 559.67 ° R lb-mol

From Opening Vessel TOTAL

lb/hr tpy lb/activity tpy lb/hr* tpy

Total Emissions: 0.720 0.046 42.341 0.339 42.341 0.385

VOC: 0.361 0.023 21.247 0.170 21.247 0.193

Benzene: 0.001 5.1E-05 0.047 3.7E-04 0.047 4.3E-04

Total HAPs: 0.012 0.001 0.727 0.006 0.727 0.007H2S: 1.0E-04 6.5E-06 0.006 4.8E-05 0.006 5.5E-05

Notes:

* Depressurizing and opening the vessel are sequential activities; therefore, the total hourly emission rate is the higher of the two activities

The basis of the example emission calculation (such as volume, concentration, pressure) are example conditions and should not be interpreted as representations of a specific facility or activity condition under 116.116(a). Individual activities in this MSS category which are performed may have slight variations in procedure or equipment configuration.

Total HAPs include 2,2,4-trimethylpentane, formaldehyde and BTEX and are included in VOC

This Planned MSS Activity includes the shut in of the well to drop the pressure in the heater treater and then open the vessel to flare to bleed off as much pressure off as possible. Then all valves are closed and the remaining pressure will be opened to atmosphere.

Emissions vented to atmosphere from opening the emptied vessel are calculated using the Ideal Gas Law and are based on the entire tank volume venting to the atmosphere at the opening concentration. It is assumed that only one heater treater would be degassed at a time.

Total Emissions

Total HAPs concentration (wt frac):

Atm Pressure (psia) :

Heater Treater Pressure (psia) :Heater Treater Volume (ft3) :

Activities per year:

Duration of opening of vessel (hours):

Number of heater treaters per activity:Ideal Gas Constant (ft3)(psi)/(lbmol)(°R) :

Max Heater Temperature (oF) :

Depressurizing Vessel

MSS-HTRDEG EPN MSS-HTRDEG

MSS Activity - Heater/Boiler Degassing

H2S Concentration (wt frac):

Benzene Concentration (wt frac):

VOC Concentration (wt frac):

Vapor MW of Flash Gas (lb/lbmol)

Vapor Pressure of Condensate (psia)



Planned MSS Emissions - Vacuum Trucks (Heater/Boiler Cleaning)

FIN EPN

Identifier

Calculation Basis:

LL = 12.46 SPM/T *(SF)

where:LL = loading loss, pounds VOC per 1000 gallons (lb/103 gal) of liquid loaded S = a saturation factorP = true vapor pressure of liquid loaded, pounds per square inch absolute (psia)M = molecular weight of vapors, pounds per pound-mole (lb/lb-mole)T = temperature of bulk liquid loaded, ºR (ºF+459.67)SF = safety factor due to vacuum loading

Heater/Boiler Contents Collected by Vacuum

Truck

Heater/Boiler Volume

(gal)

PercentVolume of

Oil/Condensate

Liquid Heel (% volume of

vessel)

Amount Loaded(gal)

S, Saturation Loss Factor

P, Vapor Pressure(psi)

M, Molecular Weight

(lb/lb-mole)

T, Bulk Loading Temp(ºF)

SF, Safety Factor

Oil/Condensate 4,230 100 3 126.90 0.600 6.236 50.000 100 2

Heater/Boiler Contents Collected by Vacuum

Truck

LL

(lb/1000 gal)Total HC Loss (lbs/activity)

Total Stream Loss (lbs/activity)

Oil/Condensate 8.330 1.057 1.110

Constants and Variables: Number of Vacuum Trucks per year: 2 (conservatively assumed)

Number of activities per hour : 2

Number of Heater Treaters: 8

THC Concentration (wt frac): 0.953 (from breathing/working composition)VOC Concentration (wt frac): 0.656 (from breathing/working composition)

Benzene Concentration (wt frac): 0.001 (from breathing/working composition)Total HAPs Concentration (wt frac): 0.024 (from breathing/working composition)

H2S Concentration (wt frac): 1.2E-04 (from breathing/working composition)

Total Emissions lb/hr tpy

Total Emissions: 2.220 0.009

VOC: 1.455 0.006

Benzene: 0.002 1.0E-05

Total HAPs: 0.053 2.1E-04

H2S: 2.6E-04 1.1E-06

Notes:



MSS-HTRCLN MSS-HTRCLN

MSS Activity - Vacuum Trucks (Heater/Boiler Cleaning)

Emissions from vacuum trucks are estimated using the loading loss method of AP-42, Chapter 5.2: Transportation and Marketing of Petroleum Liquids, 1995. Calculations are performed based on the concentrations of the individual organic species since the wastes contain significant non-volatile content (i.e. water, solids). A truck can be loaded in one hour, therefore the emissions per loading activity reflect the lb/hr emission rate.



Planned MSS Emissions - Vacuum Trucks (Tank Cleaning)

FIN EPN

Identifier

Calculation Basis:

LL = 12.46 SPM/T *(SF)where:

LL = loading loss, pounds VOC per 1000 gallons (lb/103 gal) of liquid loaded S = a saturation factorP = true vapor pressure of liquid loaded, pounds per square inch absolute (psia)M = molecular weight of vapors, pounds per pound-mole (lb/lb-mole)T = temperature of bulk liquid loaded, ºR (ºF+459.67)SF = safety factor due to vacuum loading

Tank Contents Collected by Vacuum

Truck

Tank Volume (gal)

Percent Volumeof Condensate/Oil

Liquid Heel (% volume of tank)

Amount Loaded(gal)

S, Saturation Loss Factor

P, Vapor Pressure(psi)

M, Molecular Weight

(lb/lb-mole)

T, Bulk Loading Temp(ºR)

SF, Safety Factor

Produced Water 21,000 1 3 6.30 0.600 6.236 50.000 563 2

Oil/Condensate 42,000 100 3 1260.00 0.600 6.236 50.000 563 2

Tank Contents Collected by Vacuum

Truck

LL

(lb/1000 gal)Total HC Loss(lbs/activity)

Total Stream Loss(lbs/activity)

Produced Water 4.557 0.029 0.030

Oil/Condensate 4.557 3.764 3.952

Constants and Variables:

Number of activities per year, per tank: 3 (conservatively assumed)Number of activities per hour: 2

Number of Oil/Condensate Tanks: 23

Number of Produced Water Tanks: 5

THC Concentration (wt frac): 0.953 (from breathing/working composition)VOC Concentration (wt frac): 0.656 (from breathing/working composition)

Benzene Concentration (wt frac): 0.001 (from breathing/working composition)0.024 (from breathing/working composition)

H2S Concentration (wt frac): 1.2E-04 (from breathing/working composition)

lb/hr tpy lb/hr tpy lb/hr tpy

Total Emissions: 7.904 0.136 0.060 2.3E-04 7.904 0.137

VOC: 5.181 0.089 0.040 1.5E-04 5.181 0.090

Benzene: 0.009 1.5E-04 6.8E-05 2.5E-07 0.009 1.5E-04

Total HAPs: 0.187 0.003 0.001 5.4E-06 0.187 0.003

H2S: 0.001 1.6E-05 7.2E-06 2.7E-08 0.001 1.6E-05

Notes:



MSS-TNKCLN

Oil/Condensate Tanks Produced Water Tanks TOTAL

Total HAPs Concentration (wt frac):

Emissions from vacuum trucks are estimated using the loading loss method of AP-42, Chapter 5.2: Transportation and Marketing of Petroleum Liquids, 1995. Calculations are performed based on the concentrations of the individual organic species since the wastes contain significant non-volatile content (i.e. water, solids). A truck can be loaded in one hour, therefore the emissions per loading activity reflect the lb/hr emission rate.

MSS-TNKCLN

MSS Activity - Vacuum Trucks (Tank Cleaning)

Total Emissions



Planned MSS Emissions - Pigging

FIN

Identifier

Calculation Basis:

Gas Properties fromConstants and Variables: Separator Gas (ProMax Stream LP Sep Gas):

40.00 Molecular Weight: 23.02 lb/lb mol

6.00 VOC Content : 28.55% Wt. %

0.67 Benzene Content: 0.05% Wt. %

2.09 Total HAPs Content: 0.83% Wt. %

95.00 H2S Content: 0.01% Wt. %

10.73

1

432

Emission Calculation Method:

Total gas vented to atmosphere (lb/activity) = (Pressure x Volume) / (Gas Constant x Temperature [°R]) * MW

= 40.00 psia 2.09 ft3 23.02 lb

10.73 ft3 * psi / °R * lb-mol 555 ° R lb-mol

Total Emissions lb/hr tpyTotal Emissions: 0.324 0.070

VOC: 0.093 0.020

Benzene: 1.8E-04 3.8E-05

Total HAPs: 0.003 0.001

H2S: 3.0E-05 6.4E-06

Notes:



Piping Diameter (ft) :

Piping Length (ft) :

Venting Pressure (psia) :

Number of activities per hour :

Activities per year :

Ideal Gas Constant (ft3)(psi)/(lbmol)(°R) :

Process Temperature (oF) :

Piping Volume (ft3) :

MSS-PIG EPN MSS-PIG

MSS Activity - Pigging

Emissions vented to the atmosphere after opening pipelines are calculated using the Ideal Gas Law and are based on the entire pipe volume venting to the atmosphere at pipeline pressure.



Planned MSS Emissions - Compressor Blowdowns

Vent Gas Stream Composition (Weight % From Gas Analysis)

Molecular Weight VOC (C3) VOC (C4+) Benzene HAPs H2S

23.02 12.65% 15.90% 0.05% 0.83% 0.01%

FIN COMP-MSS EPN FLR-01

Identifier: Compressors Blowdowns/Startups

Venting Volume (scf/event): 2,500

Hourly Blowdown/Startup Events (event/hr): 1

Number of Events Per Year Per Compressor: 52

Total Compressors: 6

Total Annual Events (event/yr): 312

Total Annual Vented Volume (scf/yr): 780,000

Capture Efficiency % 100%

VOC (C3) Control Efficiency (%) 99%

VOC (C4+) Control Efficiency (%) 98%

H2S Control Efficiency (%) 98%

Uncontrolled Emissions lb/hr tpy

Total: 149.401 23.307

VOC (C3): 18.905 2.949

VOC (C4+): 23.757 3.706

Benzene: 0.081 0.013

Total HAPs: 1.242 0.194H2S: 0.014 0.002

Post-Control Emissions lb/hr tpy

VOC (C3): 0.189 0.029

VOC (C4+): 0.475 0.074

Benzene: 0.002 2.53E-04

Total HAPs: 0.025 0.004H2S: 2.74E-04 4.27E-05

Emission Calculation Method:Total Uncontrolled Emissions (lb/hr) = (Volume per Event) x (Events per Hour) x MW / (Constant scf/lb-mol)

= 2,500 scf/event x 1 event/hr x 23.02 lb/lb-mol / 385.22 scf/lb-mol

Notes:

Compressor engine is shutdown at least quarterly for maintenance. Each maintenance event lasts approximately 4 hours where the produced gas is routed to the flare.

Downtime: Venting Volume (scf/hr) is ratio of the permitted daily gas production rate and the compressor with largest HP rating.

Blowdown/Startups: Assume that blowdown/startup for the largest compressor occurs in one hour.

The basis of these emission calculations (i.e. volume, stream composition, frequency) are conditions used to establish a potential to emit and should not be interpreted as representations of a specific activity or condition under 30 TAC 116.116(a). Individual activities performed in this MSS category may have slight variations in procedure or equipment configuration.




APPENDIX B IMPACTS ANALYSES



Impacts AnalysisGeneric Modeling Tables

SO2

WR/G

Benzene

WR/G

H2S

WR/GAlternate OperatingScenarios

SO2 Benzene H2S Distance G valueAlternate Operating

ScenariosAlternate Operating

ScenariosAlternate Operating

Scenarios

1 2 3 lb/hr lb/hr lb/hr ft (µg/m3) / (lb/hr)

1 2 3 1 2 3 1 2 3

FUG FUG Fugitive Emissions X X X X -- 0.019 0.001 57 4,375 -- -- -- -- 8.78E-06 1.01E-05 1.03E-05 1.02E-05 3.36E-06 4.03E-06 3.83E-06 3.83E-06

ENG-01 ENG-01 IP Compressor Engine - Caterpillar G3516B X X X X 0.034 0.005 -- 290 10 0.001 0.001 0.001 0.001 0.001 0.001 0.001 0.001 -- -- -- --

ENG-02 ENG-02 IP Compressor Engine - Waukesha L7044GSI X X X 0.046 0.022 -- 290 7 0.002 0.002 0.002 -- 0.006 0.007 0.007 -- -- -- -- --

ENG-03 ENG-03 IP Compressor Engine - Caterpillar G3516B X X X X 0.034 0.005 -- 290 10 0.001 0.001 0.001 0.001 0.001 0.001 0.001 0.001 -- -- -- --

ENG-04 ENG-04 Flash Compressor Engine - Caterpillar G3516B X X X X 0.034 0.005 -- 290 10 0.001 0.001 0.001 0.001 0.001 0.001 0.001 0.001 -- -- -- --

ENG-05 ENG-05 Flash Compressor Engine - Caterpillar G3516B X X X X 0.034 0.005 -- 290 10 0.001 0.001 0.001 0.001 0.001 0.001 0.001 0.001 -- -- -- --

ENG-06 ENG-06 Flash Compressor Engine - Waukesha L7044GSI X X X 0.043 0.021 -- 290 7 0.002 0.002 -- 0.002 0.006 0.007 -- 0.007 -- -- -- --

ENG-07 ENG-07 Cooler Engine - Arrow VRG 330 X X X X 0.002 0.001 -- 255 93 7.32E-06 7.35E-06 7.03E-06 7.01E-06 2.10E-05 2.42E-05 2.47E-05 2.44E-05 -- -- -- --

ENG-08 ENG-08 Cooler Engine - Arrow VRG 330 X X X X 0.002 0.001 -- 284 93 7.32E-06 7.35E-06 7.03E-06 7.01E-06 2.10E-05 2.42E-05 2.47E-05 2.44E-05 -- -- -- --

ENGVRU-01 ENGVRU-01 VRU Compressor Engine - Cummins G855 X X 0.005 0.003 -- 101 93 1.94E-05 -- -- 1.85E-05 5.55E-05 -- -- 6.44E-05 -- -- -- --

ENGVRU-02 ENGVRU-02 VRU Compressor Engine - Cummins G855 X X 0.005 0.003 -- 101 93 1.94E-05 -- -- 1.85E-05 5.55E-05 -- -- 6.44E-05 -- -- -- --

ENGVRU-03 ENGVRU-03 VRU Compressor Engine - GM Vortec 5.7L X X 0.003 0.001 -- 101 93 9.35E-06 -- -- 8.96E-06 2.68E-05 -- -- 3.11E-05 -- -- -- --

ENGVRU-04 ENGVRU-04 VRU Compressor Engine - Cummins G8.3 X X X X 0.003 0.002 -- 101 93 1.17E-05 1.17E-05 1.12E-05 1.12E-05 3.35E-05 3.85E-05 3.93E-05 3.88E-05 -- -- -- --

HTR-01 HTR-01 Heater Treater X X X X 0.002 1.03E-06 -- 162 90 6.18E-06 6.21E-06 5.94E-06 5.92E-06 2.31E-08 2.66E-08 2.71E-08 2.68E-08 -- -- -- --








HTR-09 HTR-09 Glycol Unit Reboiler X X X X 0.002 1.54E-06 -- 101 469 1.78E-06 1.79E-06 1.71E-06 1.70E-06 6.65E-09 7.65E-09 7.81E-09 7.72E-09 -- -- -- --

HTR-10 HTR-10 Line Heater X X X X 0.005 3.09E-06 -- 120 469 3.56E-06 3.57E-06 3.42E-06 3.41E-06 1.33E-08 1.53E-08 1.56E-08 1.54E-08 -- -- -- --

CAT-HTR CAT-HTR Catalytic Heaters X X X X 1.19E-04 7.41E-08 -- 57 4,375 9.15E-09 9.19E-09 8.80E-09 8.77E-09 3.42E-11 3.94E-11 4.02E-11 3.97E-11 -- -- -- --

DEHY-01 DEHY-01 Glycol Unit (Condenser) X X X X -- 0.011 -- 101 469 -- -- -- -- 4.93E-05 5.68E-05 5.79E-05 5.72E-05 -- -- -- --OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02, PWTK-03, PWTK-04, PWTK-05,

OILTK-23

OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02,

PWTK-03, PWTK-04, PWTK-05, OILTK-23

Uncontrolled/Uncaptured Tanks X X X X -- 0.005 0.001 143 305 -- -- -- -- 3.29E-05 3.79E-05 3.86E-05 3.82E-05 4.76E-05 5.70E-05 5.42E-05 5.42E-05

LOAD LOAD Truck Loading X X X X -- 0.055 0.007 418 1,048 -- -- -- -- 1.07E-04 1.23E-04 1.25E-04 1.24E-04 1.45E-04 1.74E-04 1.65E-04 1.65E-04

Flare Pilot X X X X 1.99E-04 2.42E-05 2.12E-06 2.59E-06 2.60E-06 2.49E-06 2.48E-06 1.88E-06 2.17E-06 2.21E-06 2.19E-06 1.86E-06 2.23E-06 2.12E-06 2.12E-06

Combustion Products from Compressors Blowdowns/Startups X X 0.026 -- -- -- -- 3.21E-04 3.20E-04 -- -- -- -- -- -- -- --

Combustion Products from Produced Gas X X 1.734 -- -- 0.023 0.023 -- -- -- -- -- -- -- -- -- --

Combustion Products from Produced Gas during Compressor Downtime X X 1.885 -- -- -- -- 0.024 0.023 -- -- -- -- -- -- -- --

COMP-MSS Compressors Blowdowns/Startups X X -- 0.002 2.74E-04 -- -- -- -- -- -- 1.48E-04 1.46E-04 -- -- 2.74E-04 2.74E-04

Produced Gas X X -- 0.120 0.018 -- -- -- -- 0.009 0.011 -- -- 0.016 0.019 -- --

Produced Gas during Compressor Downtime X X -- 0.131 0.020 -- -- -- -- -- -- 0.012 0.012 -- -- 0.020 0.020

Flare Pilot X X X X 1.99E-04 2.42E-05 2.12E-06 1.56E-06 1.57E-06 1.50E-06 1.50E-06 1.14E-06 1.31E-06 1.34E-06 1.32E-06 1.13E-06 1.35E-06 1.28E-06 1.28E-06

Combustion Products from Controlled Tanks X X X X 0.099 -- -- 0.001 0.001 0.001 0.001 -- -- -- -- -- -- -- --

Combustion Products from Truck Loading X X X X 0.029 -- -- 2.29E-04 2.30E-04 2.20E-04 2.19E-04 -- -- -- -- -- -- -- --

Combustion Products from Glycol Unit X X X X -- -- -- -- -- -- -- -- -- -- -- -- -- -- --

Combustion Products from Vapor Recovery Towers Gas X X X X 0.823 -- -- 0.006 0.006 0.006 0.006 -- -- -- -- -- -- -- --

Combustion Products from Drip Vapor Recovery Tower Gas X X X X 0.003 -- -- 2.08E-05 2.09E-05 2.00E-05 2.00E-05 -- -- -- -- -- -- -- --OILTK-01, OILTK-02, OILTK-03, OILTK-04, OILTK-05, OILTK-06, OILTK-07, OILTK-08, OILTK-09, OILTK-10, OILTK-11, OILTK-12, OILTK-13, OILTK-14, OILTK-15, OILTK-16, OILTK-17, OILTK-18, OILTK-19, OILTK-20, OILTK-21, OILTK-22, PWTK-01, PWTK-02,

PWTK-03, PWTK-04, PWTK-05, OILTK-23

Controlled Tanks X X X X -- 0.009 0.001 -- -- -- -- 4.20E-04 4.84E-04 4.93E-04 4.88E-04 0.001 0.001 0.001 0.001

LOAD Truck Loading X X X X -- 0.003 3.10E-04 -- -- -- -- 1.21E-04 1.40E-04 1.42E-04 1.41E-04 1.65E-04 1.97E-04 1.88E-04 1.88E-04DEHY-01 Glycol Unit (Flash Tank) X X X X -- 0.001 -- -- -- -- -- 3.85E-05 4.43E-05 4.52E-05 4.47E-05 -- -- -- --VRT-GAS Vapor Recovery Towers Gas X X X X -- 0.142 0.009 -- -- -- -- 0.007 0.008 0.008 0.008 0.005 0.006 0.005 0.005

DRIPVRT-GAS Drip Vapor Recovery Tower Gas X X X X -- 4.66E-04 2.83E-05 -- -- -- -- 2.19E-05 2.52E-05 2.57E-05 2.54E-05 1.50E-05 1.80E-05 1.71E-05 1.71E-05

MSS-HTRDEG MSS-HTRDEG Heater Treater Degassing X -- 0.047 0.006 68 791 -- -- -- -- 1.20E-04 -- -- -- 1.73E-04 -- -- --

MSS-HTRCLN MSS-HTRCLN Vacuum Trucks (Heater Treater Cleanout) X -- 0.002 2.64E-04 68 1,232 -- -- -- -- 4.08E-06 -- -- -- 4.90E-06 -- -- --

MSS-PIG MSS-PIG Pig Launcher Degassing X -- 1.76E-04 2.97E-05 57 4,304 -- -- -- -- 8.25E-08 -- -- -- 1.58E-07 -- -- --

MSS-TNKCLN MSS-TNKCLN Vacuum Trucks (Oil/Condensate Tank Cleanout) X -- 0.009 0.001 316 1,193 -- -- -- -- 1.50E-05 -- -- -- 1.80E-05 -- -- --

MSS-TNKCLN MSS-TNKCLN Vacuum Trucks (Produced Water Tank Cleanout) X -- 6.76E-05 7.18E-06 316 1,193 -- -- -- -- 1.15E-07 -- -- -- 1.37E-07 -- -- --

P, applicable standard (µg/m3) 196 170 108

Alternate Operating Scenarios: EMAX, maximum allowable emission rate (lb/hr) 7.636 7.661 7.371 7.329 5.627 6.421 5.554 5.436 2.376 2.822 2.887 2.887

1. VRU Downtime Site-wide emissions (lb/hr) 2.964 2.950 3.084 3.094 0.495 0.430 0.422 0.427 0.044 0.037 0.038 0.038

2. Flash Compressor Downtine Pass? Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes Yes

3. IP Compressor Downtime

Notes:

Distance indicated is the estimated distance to property line.

EPN FIN Emission Source Name

169

No

rma

l

No

rma

l

No

rma

l

PROD-GAS

Emission rates

= P × [(WREPN1/GEPN1) + (WREPN2/GEPN2) + … + (WREPNn/GEPNn)]

Emax, hourly (lb/hr) = maximum acceptable hourly (lb/hr) emissions for a specific air pollutantP: applicable standard/ESL (µg/m3)

G: applicable generic value from the Generic Modeling Results Tables from 6002 - NON-RULE 2012-NOV-08(m)

WR: weighted ratio of emissons of a specific contaminant for each EPN divided by the sum of total emissions for all EPNs

NOx to NO2 conversion factors determined in accordance with the TCEQ APDG 6232v2 Air Quality Modeling Guidelines (06/2014), and with paragraph (k)(4)(A) of 30 TAC §116.602 – NON RULE 2012-NOV-08 for engines.

FLR-01

FLR-02

26

43

No

rma

l

FLR-01

FLR-02

114


Impacts AnalysisSCREEN3 Modeling

Stack parameters

NO2

µg/m3

Alternate Operating Scenarions

1 2 3 lb/hr lb/hr MMBtu/hr ft ftTemp

(F)Flow(cfm)

ft m(µg/m3) / (lb/hr)

1 2 3

ENG-01 ENG-01 IP Compressor Engine - Caterpillar G3516B X X X X 3.042 0.2 0.608 23.000 1.167 992.000 9,126.000 290 171.000 No 5.679 3.456 3.456 3.456 3.456

ENG-02 ENG-02 IP Compressor Engine - Waukesha L7044GSI X X X 1.852 0.2 0.370 24.000 1.167 1,224.000 8,761.000 290 177.000 No 5.319 1.970 1.970 1.970 --

ENG-03 ENG-03 IP Compressor Engine - Caterpillar G3516B X X X X 3.042 0.2 0.608 22.641 1.333 1,011.000 9,243.000 290 171.000 No 5.646 3.436 3.436 3.436 3.436

ENG-04 ENG-04 Flash Compressor Engine - Caterpillar G3516B X X X X 3.042 0.2 0.608 22.641 1.333 1,011.000 9,243.000 290 171.000 No 5.646 3.436 3.436 3.436 3.436

ENG-05 ENG-05 Flash Compressor Engine - Caterpillar G3516B X X X X 3.042 0.2 0.608 23.000 1.167 992.000 9,126.000 290 171.000 No 5.679 3.456 3.456 3.456 3.456

ENG-06 ENG-06 Flash Compressor Engine - Waukesha L7044GSI X X X 1.852 0.2 0.370 24.167 1.167 1,179.000 8,162.000 290 171.000 No 5.694 2.109 2.109 -- 2.109

ENG-07 ENG-07 Cooler Engine - Arrow VRG 330 X X X X 0.420 0.2 0.084 8.000 0.250 1,238.000 406.000 255 78.000 No 159.200 13.365 13.365 13.365 13.365

ENG-08 ENG-08 Cooler Engine - Arrow VRG 330 X X X X 0.420 0.2 0.084 8.000 0.250 1,238.000 406.000 284 87.000 No 155.700 13.071 13.071 13.071 13.071

ENGVRU-01 ENGVRU-01 VRU Compressor Engine - Cummins G855 X X 0.414 0.2 0.083 8.240 0.333 1,196.000 866.000 101 80.000 No 50.650 4.199 -- -- 4.199

ENGVRU-02 ENGVRU-02 VRU Compressor Engine - Cummins G855 X X 0.414 0.2 0.083 8.240 0.333 1,196.000 866.000 101 80.000 No 50.650 4.199 -- -- 4.199

ENGVRU-03 ENGVRU-03 VRU Compressor Engine - GM Vortec 5.7L X X 0.203 0.2 0.041 8.750 0.250 1,200.000 650.000 101 82.000 No 62.820 2.548 -- -- 2.548

ENGVRU-04 ENGVRU-04 VRU Compressor Engine - Cummins G8.3 X X X X 0.520 0.2 0.104 15.000 0.250 1,374.000 604.000 101 81.000 No 64.210 6.682 6.682 6.682 6.682

HTR-01 HTR-01 Heater Treater X X X X 0.049 0.8 0.039 0.500 30.000 1.000 600.000 169.549 162 128.000 Yes 98.330 2.584 2.584 2.584 2.584





HTR-06 HTR-06 Heater Treater X X X X 0.147 0.8 0.118 1.500 15.000 2.000 900.000 652.649 68 41.000 No 101.400 11.929 11.929 11.929 11.929



HTR-09 HTR-09 Glycol Unit Reboiler X X X X 0.074 0.8 0.059 0.750 15.000 1.000 900.000 326.324 101 62.000 No 123.700 7.276 7.276 7.276 7.276

HTR-10 HTR-10 Line Heater X X X X 0.147 0.8 0.118 1.500 13.000 1.333 900.000 652.649 120 41.000 No 97.960 11.525 11.525 11.525 11.525

CAT-HTR CAT-HTR Catalytic Heaters X X X X 0.004 0.8 0.003 0.036 -- -- -- -- 56.757 105.000 Yes 545.800 1.033 1.033 1.033 1.033

Flare Pilot X X X X 0.008 0.8 0.007 0.001 0.001 0.001 0.001

Combustion Products from Compressors Blowdowns/Startups X X 0.422 0.8 0.338 -- -- 0.058 0.058

Combustion Products from Produced Gas X X 25.133 0.8 20.107 3.439 3.439 -- --

Combustion Products from Produced Gas during Compressor Downtime X X 27.319 0.8 21.855 -- -- 3.738 3.738

Flare Pilot X X X X 0.008 0.8 0.007 0.003 0.003 0.003 0.003

Combustion Products from Controlled Tanks X X X X 0.762 0.8 0.609 0.246 0.246 0.246 0.246

Combustion Products from Truck Loading X X X X 0.229 0.8 0.183 0.074 0.074 0.074 0.074

Combustion Products from Glycol Unit (Flash Tank) X X X X 0.078 0.8 0.062 0.025 0.025 0.025 0.025

Combustion Products from Vapor Recovery Towers Gas X X X X 9.191 0.8 7.353 2.967 2.967 2.967 2.967

Combustion Products from Drip Vapor Recovery Tower Gas X X X X 0.041 0.8 0.033 0.013 0.013 0.013 0.013

137.233 126.288 124.536 135.620

Alternate Operating Scenarios:

1. VRU Downtime 184.233 173.288 171.536 182.620

2. Flash Compressor Downtine

3. IP Compressor Downtime Yes Yes Yes Yes

Notes:

0.403No

No

SCREEN3Ghourly

45.000 114 1,088.000 0.171

Emission rates

FLR-01 FLR-01

74.702 794.000 169

StackDiameter

StackHeight

30.000FLR-02 FLR-02

182.187

SCREEN3 Results [2]

Distanceto max

Closestproperty

lineStack Gas Exit

Normal

Max occuring at

wind speeds ≤

1m/s?

HeatRelease

NO2NOx/NO2

ratio[1]

NOxEPN FIN Emission Source Name

No

rmal

Alternate OperatingScenarios

[1] NOx to NO2 conversion factors determined in accordance with the TCEQ APDG 6232v2 Air Quality Modeling Guidelines (06/2014), and with paragraph (k)(4)(A) of 30 TAC §116.602 – NON RULE 2012-NOV-08 for engines.

[2] Each EPN was modeled in SCREEN3 using a unit emission rate of 1 lb/hr. The Screen3 generic impact, Ghourly (µg/m3) / (lb/hr) was determined for each EPN. Emission rate from each source was multiplied by Ghourly. All maximum impacts were summed for each pollutant and evaluated against the appropriate NAAQS.

47.0

188

ENG-01,05.OUT 11/05/15 15:32:28 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

ENG-01,05

SIMPLE TERRAIN INPUTS: SOURCE TYPE = POINT EMISSION RATE (G/S) = 0.126000 STACK HEIGHT (M) = 7.0104 STK INSIDE DIAM (M) = 0.3557 STK EXIT VELOCITY (M/S)= 43.3428 STK GAS EXIT TEMP (K) = 806.4833 AMBIENT AIR TEMP (K) = 293.1500 RECEPTOR HEIGHT (M) = 0.0000 URBAN/RURAL OPTION = RURAL BUILDING HEIGHT (M) = 0.0000 MIN HORIZ BLDG DIM (M) = 0.0000 MAX HORIZ BLDG DIM (M) = 0.0000

THE REGULATORY (DEFAULT) MIXING HEIGHT OPTION WAS SELECTED. THE REGULATORY (DEFAULT) ANEMOMETER HEIGHT OF 10.0 METERS WAS ENTERED.

BUOY. FLUX = 8.557 M**4/S**3; MOM. FLUX = 21.599 M**4/S**2.

*** FULL METEOROLOGY ***

********************************** *** SCREEN AUTOMATED DISTANCES *** **********************************

*** TERRAIN HEIGHT OF 0. M ABOVE STACK BASE USED FOR FOLLOWING DISTANCES ***

DIST CONC U10M USTK MIX HT PLUME SIGMA SIGMA (M) (UG/M**3) STAB (M/S) (M/S) (M) HT (M) Y (M) Z (M) DWASH ------- ---------- ---- ----- ----- ------ ------ ------ ------ ----- 88. 1.902 3 10.0 10.0 3200.0 17.73 11.27 6.90 NO 100. 2.928 3 10.0 10.0 3200.0 17.73 12.62 7.71 NO 200. 5.472 3 10.0 10.0 3200.0 17.73 23.82 14.36 NO 300. 5.132 4 10.0 10.0 3200.0 17.73 22.82 12.47 NO 400. 4.627 4 8.0 8.0 2560.0 20.41 29.70 15.74 NO 500. 4.065 4 8.0 8.0 2560.0 20.41 36.35 18.69 NO 600. 3.670 4 5.0 5.0 1600.0 28.45 43.15 22.08 NO 700. 3.380 4 5.0 5.0 1600.0 28.45 49.57 24.80 NO 800. 3.091 4 4.5 4.5 1440.0 30.83 55.99 27.63 NO 900. 2.851 4 4.0 4.0 1280.0 33.81 62.36 30.44 NO 1000. 2.644 4 3.5 3.5 1120.0 37.64 68.69 33.26 NO 1100. 2.457 4 3.5 3.5 1120.0 37.64 74.82 35.23 NO 1200. 2.296 4 3.0 3.0 960.0 42.74 81.08 37.51 NO 1300. 2.162 4 3.0 3.0 960.0 42.74 87.12 39.35 NO 1400. 2.034 4 3.0 3.0 960.0 42.74 93.11 41.15 NO 1500. 1.923 4 2.5 2.5 800.0 49.89 99.30 43.43 NO 1600. 1.995 5 1.0 1.0 10000.0 67.81 80.06 33.88 NO 1700. 2.056 5 1.0 1.0 10000.0 67.81 84.38 34.86 NO 1800. 2.105 5 1.0 1.0 10000.0 67.81 88.69 35.83 NO 1900. 2.143 5 1.0 1.0 10000.0 67.81 92.99 36.78 NO 2000. 2.173 5 1.0 1.0 10000.0 67.81 97.26 37.73 NO 2100. 2.183 5 1.0 1.0 10000.0 67.81 101.52 38.57 NO 2200. 2.188 5 1.0 1.0 10000.0 67.81 105.77 39.40 NO 2300. 2.211 6 1.0 1.0 10000.0 57.47 73.70 27.43 NO 2400. 2.253 6 1.0 1.0 10000.0 57.47 76.49 27.90 NO

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ENG-01,05.OUT 2500. 2.290 6 1.0 1.0 10000.0 57.47 79.27 28.36 NO 2600. 2.323 6 1.0 1.0 10000.0 57.47 82.04 28.82 NO 2700. 2.351 6 1.0 1.0 10000.0 57.47 84.80 29.27 NO 2800. 2.375 6 1.0 1.0 10000.0 57.47 87.56 29.71 NO 2900. 2.395 6 1.0 1.0 10000.0 57.47 90.31 30.15 NO 3000. 2.412 6 1.0 1.0 10000.0 57.47 93.05 30.59 NO 3500. 2.403 6 1.0 1.0 10000.0 57.47 106.63 32.37 NO 4000. 2.361 6 1.0 1.0 10000.0 57.47 120.04 34.04 NO 4500. 2.299 6 1.0 1.0 10000.0 57.47 133.28 35.62 NO 5000. 2.227 6 1.0 1.0 10000.0 57.47 146.38 37.12 NO 5500. 2.150 6 1.0 1.0 10000.0 57.47 159.34 38.55 NO 6000. 2.071 6 1.0 1.0 10000.0 57.47 172.18 39.93 NO 6500. 1.992 6 1.0 1.0 10000.0 57.47 184.91 41.25 NO 7000. 1.916 6 1.0 1.0 10000.0 57.47 197.52 42.52 NO 7500. 1.838 6 1.0 1.0 10000.0 57.47 210.03 43.61 NO 8000. 1.764 6 1.0 1.0 10000.0 57.47 222.45 44.67 NO 8500. 1.695 6 1.0 1.0 10000.0 57.47 234.78 45.69 NO 9000. 1.630 6 1.0 1.0 10000.0 57.47 247.03 46.68 NO 9500. 1.569 6 1.0 1.0 10000.0 57.47 259.20 47.64 NO 10000. 1.512 6 1.0 1.0 10000.0 57.47 271.29 48.57 NO 15000. 1.089 6 1.0 1.0 10000.0 57.47 388.69 56.75 NO 20000. 0.8400 6 1.0 1.0 10000.0 57.47 501.16 61.99 NO 25000. 0.6809 6 1.0 1.0 10000.0 57.47 609.92 66.44 NO 30000. 0.5706 6 1.0 1.0 10000.0 57.47 715.73 70.33 NO 40000. 0.4311 6 1.0 1.0 10000.0 57.47 920.34 75.87 NO 50000. 0.3456 6 1.0 1.0 10000.0 57.47 1117.52 80.49 NO

MAXIMUM 1-HR CONCENTRATION AT OR BEYOND 88. M: 171. 5.679 3 10.0 10.0 3200.0 17.73 20.76 12.56 NO

DWASH= MEANS NO CALC MADE (CONC = 0.0) DWASH=NO MEANS NO BUILDING DOWNWASH USED DWASH=HS MEANS HUBER-SNYDER DOWNWASH USED DWASH=SS MEANS SCHULMAN-SCIRE DOWNWASH USED DWASH=NA MEANS DOWNWASH NOT APPLICABLE, X<3*LB

*************************************** *** SUMMARY OF SCREEN MODEL RESULTS *** ***************************************

CALCULATION MAX CONC DIST TO TERRAIN PROCEDURE (UG/M**3) MAX (M) HT (M) -------------- ----------- --------- ------- SIMPLE TERRAIN 5.679 171. 0.

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ENG-02.OUT 11/04/15 15:39:34 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

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ENG-02.OUT 2500. 2.167 6 1.0 1.0 10000.0 58.36 79.30 28.45 NO 2600. 2.201 6 1.0 1.0 10000.0 58.36 82.07 28.90 NO 2700. 2.231 6 1.0 1.0 10000.0 58.36 84.83 29.35 NO 2800. 2.256 6 1.0 1.0 10000.0 58.36 87.59 29.79 NO 2900. 2.279 6 1.0 1.0 10000.0 58.36 90.33 30.23 NO 3000. 2.297 6 1.0 1.0 10000.0 58.36 93.07 30.67 NO 3500. 2.298 6 1.0 1.0 10000.0 58.36 106.65 32.44 NO 4000. 2.266 6 1.0 1.0 10000.0 58.36 120.06 34.11 NO 4500. 2.214 6 1.0 1.0 10000.0 58.36 133.30 35.69 NO 5000. 2.150 6 1.0 1.0 10000.0 58.36 146.40 37.19 NO 5500. 2.080 6 1.0 1.0 10000.0 58.36 159.36 38.62 NO 6000. 2.008 6 1.0 1.0 10000.0 58.36 172.20 39.99 NO 6500. 1.935 6 1.0 1.0 10000.0 58.36 184.92 41.31 NO 7000. 1.864 6 1.0 1.0 10000.0 58.36 197.53 42.58 NO 7500. 1.790 6 1.0 1.0 10000.0 58.36 210.04 43.67 NO 8000. 1.720 6 1.0 1.0 10000.0 58.36 222.46 44.73 NO 8500. 1.655 6 1.0 1.0 10000.0 58.36 234.79 45.75 NO 9000. 1.593 6 1.0 1.0 10000.0 58.36 247.04 46.73 NO 9500. 1.534 6 1.0 1.0 10000.0 58.36 259.20 47.69 NO 10000. 1.479 6 1.0 1.0 10000.0 58.36 271.29 48.62 NO 15000. 1.071 6 1.0 1.0 10000.0 58.36 388.70 56.79 NO 20000. 0.8287 6 1.0 1.0 10000.0 58.36 501.16 62.03 NO 25000. 0.6728 6 1.0 1.0 10000.0 58.36 609.92 66.48 NO 30000. 0.5646 6 1.0 1.0 10000.0 58.36 715.74 70.36 NO 40000. 0.4272 6 1.0 1.0 10000.0 58.36 920.34 75.90 NO 50000. 0.3427 6 1.0 1.0 10000.0 58.36 1117.52 80.52 NO





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ENG-03,04.OUT 11/05/15 15:33:53 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

ENG-03,04








Page 1

ENG-03,04.OUT 2500. 2.265 6 1.0 1.0 10000.0 57.70 79.29 28.41 NO 2600. 2.297 6 1.0 1.0 10000.0 57.70 82.06 28.87 NO 2700. 2.325 6 1.0 1.0 10000.0 57.70 84.82 29.32 NO 2800. 2.350 6 1.0 1.0 10000.0 57.70 87.58 29.76 NO 2900. 2.370 6 1.0 1.0 10000.0 57.70 90.32 30.20 NO 3000. 2.387 6 1.0 1.0 10000.0 57.70 93.06 30.63 NO 3500. 2.379 6 1.0 1.0 10000.0 57.70 106.64 32.41 NO 4000. 2.339 6 1.0 1.0 10000.0 57.70 120.05 34.08 NO 4500. 2.279 6 1.0 1.0 10000.0 57.70 133.29 35.66 NO 5000. 2.209 6 1.0 1.0 10000.0 57.70 146.39 37.16 NO 5500. 2.133 6 1.0 1.0 10000.0 57.70 159.35 38.59 NO 6000. 2.055 6 1.0 1.0 10000.0 57.70 172.19 39.96 NO 6500. 1.978 6 1.0 1.0 10000.0 57.70 184.91 41.28 NO 7000. 1.903 6 1.0 1.0 10000.0 57.70 197.53 42.55 NO 7500. 1.826 6 1.0 1.0 10000.0 57.70 210.04 43.65 NO 8000. 1.753 6 1.0 1.0 10000.0 57.70 222.46 44.70 NO 8500. 1.685 6 1.0 1.0 10000.0 57.70 234.79 45.72 NO 9000. 1.621 6 1.0 1.0 10000.0 57.70 247.03 46.71 NO 9500. 1.560 6 1.0 1.0 10000.0 57.70 259.20 47.67 NO 10000. 1.504 6 1.0 1.0 10000.0 57.70 271.29 48.60 NO 15000. 1.084 6 1.0 1.0 10000.0 57.70 388.70 56.77 NO 20000. 0.8371 6 1.0 1.0 10000.0 57.70 501.16 62.02 NO 25000. 0.6788 6 1.0 1.0 10000.0 57.70 609.92 66.46 NO 30000. 0.5690 6 1.0 1.0 10000.0 57.70 715.73 70.35 NO 40000. 0.4301 6 1.0 1.0 10000.0 57.70 920.34 75.89 NO 50000. 0.3448 6 1.0 1.0 10000.0 57.70 1117.52 80.51 NO





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ENGVRU-01,02.OUT 02/15/16 15:23:47 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

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Page 1

ENGVRU-01,02.OUT 2500. 10.93 6 1.0 1.0 10000.0 28.11 78.24 25.33 NO 2600. 10.60 6 1.0 1.0 10000.0 28.11 81.04 25.84 NO 2700. 10.27 6 1.0 1.0 10000.0 28.11 83.84 26.34 NO 2800. 9.966 6 1.0 1.0 10000.0 28.11 86.63 26.84 NO 2900. 9.670 6 1.0 1.0 10000.0 28.11 89.40 27.32 NO 3000. 9.387 6 1.0 1.0 10000.0 28.11 92.17 27.80 NO 3500. 8.148 6 1.0 1.0 10000.0 28.11 105.87 29.75 NO 4000. 7.160 6 1.0 1.0 10000.0 28.11 119.36 31.56 NO 4500. 6.359 6 1.0 1.0 10000.0 28.11 132.67 33.26 NO 5000. 5.699 6 1.0 1.0 10000.0 28.11 145.83 34.86 NO 5500. 5.149 6 1.0 1.0 10000.0 28.11 158.83 36.38 NO 6000. 4.684 6 1.0 1.0 10000.0 28.11 171.71 37.84 NO 6500. 4.287 6 1.0 1.0 10000.0 28.11 184.46 39.23 NO 7000. 3.945 6 1.0 1.0 10000.0 28.11 197.11 40.56 NO 7500. 3.655 6 1.0 1.0 10000.0 28.11 209.65 41.71 NO 8000. 3.400 6 1.0 1.0 10000.0 28.11 222.09 42.81 NO 8500. 3.175 6 1.0 1.0 10000.0 28.11 234.44 43.88 NO 9000. 2.976 6 1.0 1.0 10000.0 28.11 246.70 44.91 NO 9500. 2.798 6 1.0 1.0 10000.0 28.11 258.88 45.90 NO 10000. 2.638 6 1.0 1.0 10000.0 28.11 270.99 46.87 NO 15000. 1.641 6 1.0 1.0 10000.0 28.11 388.49 55.29 NO 20000. 1.185 6 1.0 1.0 10000.0 28.11 500.99 60.67 NO 25000. 0.9192 6 1.0 1.0 10000.0 28.11 609.79 65.20 NO 30000. 0.7461 6 1.0 1.0 10000.0 28.11 715.62 69.16 NO 40000. 0.5430 6 1.0 1.0 10000.0 28.11 920.25 74.79 NO 50000. 0.4242 6 1.0 1.0 10000.0 28.11 1117.44 79.48 NO





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ENGVRU-03.OUT 02/15/16 15:24:23 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

ENGVRU-03








Page 1

ENGVRU-03.OUT 2500. 11.97 6 1.0 1.0 10000.0 25.98 78.19 25.18 NO 2600. 11.56 6 1.0 1.0 10000.0 25.98 81.00 25.69 NO 2700. 11.18 6 1.0 1.0 10000.0 25.98 83.79 26.19 NO 2800. 10.81 6 1.0 1.0 10000.0 25.98 86.58 26.69 NO 2900. 10.46 6 1.0 1.0 10000.0 25.98 89.36 27.18 NO 3000. 10.13 6 1.0 1.0 10000.0 25.98 92.13 27.66 NO 3500. 8.710 6 1.0 1.0 10000.0 25.98 105.83 29.62 NO 4000. 7.600 6 1.0 1.0 10000.0 25.98 119.33 31.44 NO 4500. 6.711 6 1.0 1.0 10000.0 25.98 132.64 33.14 NO 5000. 5.987 6 1.0 1.0 10000.0 25.98 145.80 34.75 NO 5500. 5.387 6 1.0 1.0 10000.0 25.98 158.81 36.28 NO 6000. 4.885 6 1.0 1.0 10000.0 25.98 171.69 37.73 NO 6500. 4.458 6 1.0 1.0 10000.0 25.98 184.44 39.13 NO 7000. 4.093 6 1.0 1.0 10000.0 25.98 197.09 40.47 NO 7500. 3.784 6 1.0 1.0 10000.0 25.98 209.63 41.61 NO 8000. 3.514 6 1.0 1.0 10000.0 25.98 222.07 42.72 NO 8500. 3.277 6 1.0 1.0 10000.0 25.98 234.42 43.79 NO 9000. 3.067 6 1.0 1.0 10000.0 25.98 246.68 44.82 NO 9500. 2.880 6 1.0 1.0 10000.0 25.98 258.87 45.82 NO 10000. 2.712 6 1.0 1.0 10000.0 25.98 270.97 46.79 NO 15000. 1.674 6 1.0 1.0 10000.0 25.98 388.48 55.22 NO 20000. 1.205 6 1.0 1.0 10000.0 25.98 500.99 60.60 NO 25000. 0.9325 6 1.0 1.0 10000.0 25.98 609.78 65.14 NO 30000. 0.7557 6 1.0 1.0 10000.0 25.98 715.61 69.11 NO 40000. 0.5490 6 1.0 1.0 10000.0 25.98 920.24 74.74 NO 50000. 0.4284 6 1.0 1.0 10000.0 25.98 1117.44 79.43 NO





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ENGVRU-04.OUT 02/15/16 10:44:33 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

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Page 1

ENGVRU-04.OUT 2500. 12.07 6 1.0 1.0 10000.0 25.76 78.18 25.16 NO 2600. 11.66 6 1.0 1.0 10000.0 25.76 80.99 25.68 NO 2700. 11.27 6 1.0 1.0 10000.0 25.76 83.79 26.18 NO 2800. 10.89 6 1.0 1.0 10000.0 25.76 86.58 26.68 NO 2900. 10.54 6 1.0 1.0 10000.0 25.76 89.35 27.17 NO 3000. 10.20 6 1.0 1.0 10000.0 25.76 92.12 27.65 NO 3500. 8.767 6 1.0 1.0 10000.0 25.76 105.83 29.61 NO 4000. 7.643 6 1.0 1.0 10000.0 25.76 119.32 31.43 NO 4500. 6.746 6 1.0 1.0 10000.0 25.76 132.64 33.13 NO 5000. 6.015 6 1.0 1.0 10000.0 25.76 145.80 34.74 NO 5500. 5.411 6 1.0 1.0 10000.0 25.76 158.81 36.27 NO 6000. 4.905 6 1.0 1.0 10000.0 25.76 171.69 37.72 NO 6500. 4.475 6 1.0 1.0 10000.0 25.76 184.44 39.12 NO 7000. 4.107 6 1.0 1.0 10000.0 25.76 197.09 40.46 NO 7500. 3.796 6 1.0 1.0 10000.0 25.76 209.63 41.61 NO 8000. 3.525 6 1.0 1.0 10000.0 25.76 222.07 42.71 NO 8500. 3.287 6 1.0 1.0 10000.0 25.76 234.42 43.78 NO 9000. 3.076 6 1.0 1.0 10000.0 25.76 246.68 44.81 NO 9500. 2.887 6 1.0 1.0 10000.0 25.76 258.86 45.81 NO 10000. 2.719 6 1.0 1.0 10000.0 25.76 270.97 46.78 NO 15000. 1.677 6 1.0 1.0 10000.0 25.76 388.47 55.22 NO 20000. 1.207 6 1.0 1.0 10000.0 25.76 500.99 60.60 NO 25000. 0.9338 6 1.0 1.0 10000.0 25.76 609.78 65.14 NO 30000. 0.7566 6 1.0 1.0 10000.0 25.76 715.61 69.10 NO 40000. 0.5495 6 1.0 1.0 10000.0 25.76 920.24 74.73 NO 50000. 0.4287 6 1.0 1.0 10000.0 25.76 1117.44 79.42 NO





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HTR-01,02,03,04,05.OUT 11/04/15 15:47:01 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

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Page 1

HTR-01,02,03,04,05.OUT 2500. 14.38 6 1.0 1.0 10000.0 21.24 78.03 24.68 NO 2600. 13.80 6 1.0 1.0 10000.0 21.24 80.84 25.20 NO 2700. 13.26 6 1.0 1.0 10000.0 21.24 83.64 25.71 NO 2800. 12.75 6 1.0 1.0 10000.0 21.24 86.44 26.22 NO 2900. 12.27 6 1.0 1.0 10000.0 21.24 89.22 26.72 NO 3000. 11.81 6 1.0 1.0 10000.0 21.24 91.99 27.21 NO 3500. 9.973 6 1.0 1.0 10000.0 21.24 105.71 29.19 NO 4000. 8.575 6 1.0 1.0 10000.0 21.24 119.22 31.04 NO 4500. 7.485 6 1.0 1.0 10000.0 21.24 132.55 32.76 NO 5000. 6.614 6 1.0 1.0 10000.0 21.24 145.71 34.39 NO 5500. 5.905 6 1.0 1.0 10000.0 21.24 158.73 35.93 NO 6000. 5.318 6 1.0 1.0 10000.0 21.24 171.61 37.40 NO 6500. 4.826 6 1.0 1.0 10000.0 21.24 184.38 38.81 NO 7000. 4.407 6 1.0 1.0 10000.0 21.24 197.02 40.16 NO 7500. 4.059 6 1.0 1.0 10000.0 21.24 209.57 41.31 NO 8000. 3.756 6 1.0 1.0 10000.0 21.24 222.01 42.43 NO 8500. 3.492 6 1.0 1.0 10000.0 21.24 234.37 43.50 NO 9000. 3.259 6 1.0 1.0 10000.0 21.24 246.63 44.54 NO 9500. 3.052 6 1.0 1.0 10000.0 21.24 258.82 45.54 NO 10000. 2.867 6 1.0 1.0 10000.0 21.24 270.93 46.52 NO 15000. 1.742 6 1.0 1.0 10000.0 21.24 388.44 55.00 NO 20000. 1.246 6 1.0 1.0 10000.0 21.24 500.96 60.40 NO 25000. 0.9599 6 1.0 1.0 10000.0 21.24 609.76 64.95 NO 30000. 0.7754 6 1.0 1.0 10000.0 21.24 715.60 68.93 NO 40000. 0.5612 6 1.0 1.0 10000.0 21.24 920.23 74.57 NO 50000. 0.4368 6 1.0 1.0 10000.0 21.24 1117.43 79.27 NO





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HTR-06,07,08.OUT 11/04/15 15:48:17 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

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HTR-06,07,08.OUT 2500. 12.60 6 1.0 1.0 10000.0 24.70 78.17 25.13 NO 2600. 12.15 6 1.0 1.0 10000.0 24.70 80.98 25.64 NO 2700. 11.72 6 1.0 1.0 10000.0 24.70 83.78 26.15 NO 2800. 11.32 6 1.0 1.0 10000.0 24.70 86.57 26.64 NO 2900. 10.93 6 1.0 1.0 10000.0 24.70 89.34 27.13 NO 3000. 10.57 6 1.0 1.0 10000.0 24.70 92.11 27.62 NO 3500. 9.042 6 1.0 1.0 10000.0 24.70 105.82 29.58 NO 4000. 7.857 6 1.0 1.0 10000.0 24.70 119.32 31.40 NO 4500. 6.915 6 1.0 1.0 10000.0 24.70 132.63 33.10 NO 5000. 6.153 6 1.0 1.0 10000.0 24.70 145.79 34.71 NO 5500. 5.525 6 1.0 1.0 10000.0 24.70 158.80 36.24 NO 6000. 5.000 6 1.0 1.0 10000.0 24.70 171.68 37.70 NO 6500. 4.556 6 1.0 1.0 10000.0 24.70 184.44 39.09 NO 7000. 4.176 6 1.0 1.0 10000.0 24.70 197.08 40.43 NO 7500. 3.857 6 1.0 1.0 10000.0 24.70 209.62 41.58 NO 8000. 3.579 6 1.0 1.0 10000.0 24.70 222.06 42.69 NO 8500. 3.334 6 1.0 1.0 10000.0 24.70 234.41 43.76 NO 9000. 3.118 6 1.0 1.0 10000.0 24.70 246.68 44.79 NO 9500. 2.926 6 1.0 1.0 10000.0 24.70 258.86 45.79 NO 10000. 2.753 6 1.0 1.0 10000.0 24.70 270.97 46.76 NO 15000. 1.692 6 1.0 1.0 10000.0 24.70 388.47 55.20 NO 20000. 1.216 6 1.0 1.0 10000.0 24.70 500.98 60.58 NO 25000. 0.9399 6 1.0 1.0 10000.0 24.70 609.78 65.12 NO 30000. 0.7610 6 1.0 1.0 10000.0 24.70 715.61 69.09 NO 40000. 0.5523 6 1.0 1.0 10000.0 24.70 920.24 74.72 NO 50000. 0.4306 6 1.0 1.0 10000.0 24.70 1117.44 79.41 NO





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HTR-09.OUT 11/04/15 15:50:41 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

HTR-09








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HTR-09.OUT 2500. 14.47 6 1.0 1.0 10000.0 20.98 78.09 24.87 NO 2600. 13.88 6 1.0 1.0 10000.0 20.98 80.90 25.39 NO 2700. 13.33 6 1.0 1.0 10000.0 20.98 83.70 25.90 NO 2800. 12.81 6 1.0 1.0 10000.0 20.98 86.49 26.40 NO 2900. 12.32 6 1.0 1.0 10000.0 20.98 89.27 26.89 NO 3000. 11.87 6 1.0 1.0 10000.0 20.98 92.04 27.38 NO 3500. 10.01 6 1.0 1.0 10000.0 20.98 105.76 29.36 NO 4000. 8.599 6 1.0 1.0 10000.0 20.98 119.26 31.19 NO 4500. 7.502 6 1.0 1.0 10000.0 20.98 132.58 32.91 NO 5000. 6.627 6 1.0 1.0 10000.0 20.98 145.75 34.53 NO 5500. 5.915 6 1.0 1.0 10000.0 20.98 158.76 36.06 NO 6000. 5.326 6 1.0 1.0 10000.0 20.98 171.64 37.53 NO 6500. 4.832 6 1.0 1.0 10000.0 20.98 184.40 38.93 NO 7000. 4.413 6 1.0 1.0 10000.0 20.98 197.05 40.27 NO 7500. 4.063 6 1.0 1.0 10000.0 20.98 209.59 41.43 NO 8000. 3.760 6 1.0 1.0 10000.0 20.98 222.03 42.54 NO 8500. 3.495 6 1.0 1.0 10000.0 20.98 234.39 43.61 NO 9000. 3.261 6 1.0 1.0 10000.0 20.98 246.65 44.65 NO 9500. 3.054 6 1.0 1.0 10000.0 20.98 258.84 45.65 NO 10000. 2.869 6 1.0 1.0 10000.0 20.98 270.94 46.62 NO 15000. 1.743 6 1.0 1.0 10000.0 20.98 388.46 55.08 NO 20000. 1.247 6 1.0 1.0 10000.0 20.98 500.97 60.48 NO 25000. 0.9602 6 1.0 1.0 10000.0 20.98 609.77 65.02 NO 30000. 0.7756 6 1.0 1.0 10000.0 20.98 715.60 69.00 NO 40000. 0.5613 6 1.0 1.0 10000.0 20.98 920.24 74.64 NO 50000. 0.4369 6 1.0 1.0 10000.0 20.98 1117.43 79.33 NO





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HTR-10.OUT 11/04/15 15:51:36 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

HTR-10








Page 1

HTR-10.OUT 2500. 12.63 6 1.0 1.0 10000.0 24.63 78.17 25.13 NO 2600. 12.18 6 1.0 1.0 10000.0 24.63 80.98 25.64 NO 2700. 11.75 6 1.0 1.0 10000.0 24.63 83.78 26.15 NO 2800. 11.34 6 1.0 1.0 10000.0 24.63 86.57 26.64 NO 2900. 10.96 6 1.0 1.0 10000.0 24.63 89.34 27.13 NO 3000. 10.59 6 1.0 1.0 10000.0 24.63 92.11 27.62 NO 3500. 9.059 6 1.0 1.0 10000.0 24.63 105.82 29.58 NO 4000. 7.870 6 1.0 1.0 10000.0 24.63 119.32 31.40 NO 4500. 6.926 6 1.0 1.0 10000.0 24.63 132.63 33.10 NO 5000. 6.161 6 1.0 1.0 10000.0 24.63 145.79 34.71 NO 5500. 5.532 6 1.0 1.0 10000.0 24.63 158.80 36.24 NO 6000. 5.006 6 1.0 1.0 10000.0 24.63 171.68 37.70 NO 6500. 4.561 6 1.0 1.0 10000.0 24.63 184.44 39.09 NO 7000. 4.181 6 1.0 1.0 10000.0 24.63 197.08 40.43 NO 7500. 3.861 6 1.0 1.0 10000.0 24.63 209.62 41.58 NO 8000. 3.582 6 1.0 1.0 10000.0 24.63 222.06 42.69 NO 8500. 3.337 6 1.0 1.0 10000.0 24.63 234.41 43.76 NO 9000. 3.121 6 1.0 1.0 10000.0 24.63 246.68 44.79 NO 9500. 2.928 6 1.0 1.0 10000.0 24.63 258.86 45.79 NO 10000. 2.755 6 1.0 1.0 10000.0 24.63 270.97 46.76 NO 15000. 1.693 6 1.0 1.0 10000.0 24.63 388.47 55.20 NO 20000. 1.217 6 1.0 1.0 10000.0 24.63 500.98 60.58 NO 25000. 0.9402 6 1.0 1.0 10000.0 24.63 609.78 65.12 NO 30000. 0.7613 6 1.0 1.0 10000.0 24.63 715.61 69.09 NO 40000. 0.5524 6 1.0 1.0 10000.0 24.63 920.24 74.72 NO 50000. 0.4307 6 1.0 1.0 10000.0 24.63 1117.44 79.41 NO





Page 2

CAT-HTR.OUT 02/29/16 12:35:26 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

CAT-HTR

SIMPLE TERRAIN INPUTS: SOURCE TYPE = AREA EMISSION RATE (G/(S-M**2)) = 0.913300E-05 SOURCE HEIGHT (M) = 0.9144 LENGTH OF LARGER SIDE (M) = 167.6400 LENGTH OF SMALLER SIDE (M) = 82.2960 RECEPTOR HEIGHT (M) = 0.0000 URBAN/RURAL OPTION = RURAL THE REGULATORY (DEFAULT) MIXING HEIGHT OPTION WAS SELECTED. THE REGULATORY (DEFAULT) ANEMOMETER HEIGHT OF 10.0 METERS WAS ENTERED.

MODEL ESTIMATES DIRECTION TO MAX CONCENTRATION





DIST CONC U10M USTK MIX HT PLUME MAX DIR (M) (UG/M**3) STAB (M/S) (M/S) (M) HT (M) (DEG) ------- ---------- ---- ----- ----- ------ ------ ------- 17. 364.5 6 1.0 1.0 10000.0 0.91 24. 100. 543.3 6 1.0 1.0 10000.0 0.91 23. 200. 322.8 6 1.0 1.0 10000.0 0.91 23. 300. 224.3 6 1.0 1.0 10000.0 0.91 19. 400. 173.8 6 1.0 1.0 10000.0 0.91 13. 500. 142.3 6 1.0 1.0 10000.0 0.91 1. 600. 119.5 6 1.0 1.0 10000.0 0.91 0. 700. 101.7 6 1.0 1.0 10000.0 0.91 0. 800. 88.06 6 1.0 1.0 10000.0 0.91 0. 900. 77.03 6 1.0 1.0 10000.0 0.91 0. 1000. 67.95 6 1.0 1.0 10000.0 0.91 0. 1100. 60.51 6 1.0 1.0 10000.0 0.91 0. 1200. 54.29 6 1.0 1.0 10000.0 0.91 0. 1300. 49.00 6 1.0 1.0 10000.0 0.91 0. 1400. 44.46 6 1.0 1.0 10000.0 0.91 0. 1500. 40.53 6 1.0 1.0 10000.0 0.91 0. 1600. 37.14 6 1.0 1.0 10000.0 0.91 0. 1700. 34.16 6 1.0 1.0 10000.0 0.91 0. 1800. 31.56 6 1.0 1.0 10000.0 0.91 0. 1900. 29.25 6 1.0 1.0 10000.0 0.91 0. 2000. 27.22 6 1.0 1.0 10000.0 0.91 0. 2100. 25.48 6 1.0 1.0 10000.0 0.91 0. 2200. 23.94 6 1.0 1.0 10000.0 0.91 0. 2300. 22.53 6 1.0 1.0 10000.0 0.91 0. 2400. 21.26 6 1.0 1.0 10000.0 0.91 0. 2500. 20.11 6 1.0 1.0 10000.0 0.91 0. 2600. 19.07 6 1.0 1.0 10000.0 0.91 0. 2700. 18.10 6 1.0 1.0 10000.0 0.91 0. 2800. 17.21 6 1.0 1.0 10000.0 0.91 0.

Page 1

CAT-HTR.OUT 2900. 16.39 6 1.0 1.0 10000.0 0.91 0. 3000. 15.64 6 1.0 1.0 10000.0 0.91 0. 3500. 12.77 6 1.0 1.0 10000.0 0.91 0. 4000. 10.69 6 1.0 1.0 10000.0 0.91 0. 4500. 9.139 6 1.0 1.0 10000.0 0.91 0. 5000. 7.936 6 1.0 1.0 10000.0 0.91 0. 5500. 6.981 6 1.0 1.0 10000.0 0.91 0. 6000. 6.211 6 1.0 1.0 10000.0 0.91 0. 6500. 5.579 6 1.0 1.0 10000.0 0.91 0. 7000. 5.053 6 1.0 1.0 10000.0 0.91 0. 7500. 4.621 6 1.0 1.0 10000.0 0.91 0. 8000. 4.248 6 1.0 1.0 10000.0 0.91 0. 8500. 3.925 6 1.0 1.0 10000.0 0.91 0. 9000. 3.643 6 1.0 1.0 10000.0 0.91 0. 9500. 3.395 6 1.0 1.0 10000.0 0.91 0. 10000. 3.176 6 1.0 1.0 10000.0 0.91 0. 15000. 1.876 6 1.0 1.0 10000.0 0.91 0. 20000. 1.325 6 1.0 1.0 10000.0 0.91 0. 25000. 1.012 6 1.0 1.0 10000.0 0.91 0. 30000. 0.8123 6 1.0 1.0 10000.0 0.91 0. 40000. 0.5837 6 1.0 1.0 10000.0 0.91 0. 50000. 0.4521 6 1.0 1.0 10000.0 0.91 0.

MAXIMUM 1-HR CONCENTRATION AT OR BEYOND 17. M: 105. 545.8 6 1.0 1.0 10000.0 0.91 24.



Page 2

FLR-01.OUT 03/08/16 09:11:15 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

FLR-01

SIMPLE TERRAIN INPUTS: SOURCE TYPE = FLARE EMISSION RATE (G/S) = 0.126000 FLARE STACK HEIGHT (M) = 13.7160 TOT HEAT RLS (CAL/S) = 0.127529E+08 RECEPTOR HEIGHT (M) = 0.0000 URBAN/RURAL OPTION = RURAL EFF RELEASE HEIGHT (M) = 25.0778 BUILDING HEIGHT (M) = 0.0000 MIN HORIZ BLDG DIM (M) = 0.0000 MAX HORIZ BLDG DIM (M) = 0.0000






DIST CONC U10M USTK MIX HT PLUME SIGMA SIGMA (M) (UG/M**3) STAB (M/S) (M/S) (M) HT (M) Y (M) Z (M) DWASH ------- ---------- ---- ----- ----- ------ ------ ------ ------ ----- 35. 0.1374E-13 6 1.0 1.7 10000.0 149.22 17.56 17.52 NO 100. 0.2737E-02 6 1.0 1.7 10000.0 149.22 35.62 35.46 NO 200. 0.4282E-02 5 1.0 1.4 10000.0 184.14 46.91 45.87 NO 300. 0.4716E-02 5 1.0 1.4 10000.0 184.14 48.49 46.27 NO 400. 0.5210E-02 5 1.0 1.4 10000.0 184.14 50.50 46.72 NO 500. 0.1843E-01 1 3.0 3.2 960.0 325.60 125.11 117.59 NO 600. 0.7479E-01 1 3.0 3.2 960.0 325.60 146.02 165.42 NO 700. 0.1167 1 3.0 3.2 960.0 325.60 166.44 223.63 NO 800. 0.1237 1 3.0 3.2 960.0 325.60 186.43 292.36 NO 900. 0.1461 1 1.5 1.6 627.1 626.12 247.70 396.29 NO 1000. 0.1665 1 1.5 1.6 627.1 626.12 269.34 484.73 NO 1100. 0.1710 1 1.5 1.6 627.1 626.12 284.63 581.24 NO 1200. 0.1666 1 1.5 1.6 627.1 626.12 299.24 689.32 NO 1300. 0.1595 1 1.5 1.6 627.1 626.12 314.05 809.26 NO 1400. 0.1523 1 1.5 1.6 627.1 626.12 329.00 940.94 NO 1500. 0.1456 1 1.5 1.6 627.1 626.12 344.07 1084.28 NO 1600. 0.1395 1 1.5 1.6 627.1 626.12 359.23 1239.26 NO 1700. 0.1338 1 1.5 1.6 627.1 626.12 374.44 1405.87 NO 1800. 0.1288 4 20.0 23.0 6400.0 63.98 116.90 48.36 NO 1900. 0.1255 4 20.0 23.0 6400.0 63.98 122.71 49.98 NO 2000. 0.1221 4 20.0 23.0 6400.0 63.98 128.50 51.56 NO 2100. 0.1186 4 20.0 23.0 6400.0 63.98 134.26 53.12 NO 2200. 0.1151 4 20.0 23.0 6400.0 63.98 140.00 54.65 NO 2300. 0.1116 4 20.0 23.0 6400.0 63.98 145.70 56.16 NO 2400. 0.1081 4 20.0 23.0 6400.0 63.98 151.39 57.66 NO 2500. 0.1048 4 20.0 23.0 6400.0 63.98 157.05 59.13 NO 2600. 0.1015 4 20.0 23.0 6400.0 63.98 162.69 60.58 NO

Page 1

FLR-01.OUT 2700. 0.9916E-01 4 15.0 17.2 4800.0 79.32 168.63 62.90 NO 2800. 0.9716E-01 4 15.0 17.2 4800.0 79.32 174.22 64.30 NO 2900. 0.9514E-01 4 15.0 17.2 4800.0 79.32 179.78 65.68 NO 3000. 0.9311E-01 4 15.0 17.2 4800.0 79.32 185.33 67.04 NO 3500. 0.8703E-01 2 1.5 1.6 627.1 626.12 499.29 464.91 NO 4000. 0.8495E-01 2 1.5 1.6 627.1 626.12 554.57 528.85 NO 4500. 0.8026E-01 2 1.5 1.6 627.1 626.12 609.52 594.53 NO 5000. 0.7483E-01 2 1.5 1.6 627.1 626.12 664.06 661.61 NO 5500. 0.7752E-01 5 2.0 2.8 10000.0 151.33 241.13 68.69 NO 6000. 0.8091E-01 5 2.0 2.8 10000.0 151.33 260.28 70.94 NO 6500. 0.8440E-01 5 1.5 2.1 10000.0 164.03 279.77 74.98 NO 7000. 0.8736E-01 5 1.5 2.1 10000.0 164.03 298.59 77.05 NO 7500. 0.9001E-01 5 1.0 1.4 10000.0 184.14 318.04 82.10 NO 8000. 0.9302E-01 5 1.0 1.4 10000.0 184.14 336.55 84.00 NO 8500. 0.9563E-01 5 1.0 1.4 10000.0 184.14 354.94 85.85 NO 9000. 0.9788E-01 5 1.0 1.4 10000.0 184.14 373.22 87.67 NO 9500. 0.9980E-01 5 1.0 1.4 10000.0 184.14 391.39 89.45 NO 10000. 0.1014 5 1.0 1.4 10000.0 184.14 409.45 91.20 NO 15000. 0.1033 5 1.0 1.4 10000.0 184.14 585.15 105.81 NO 20000. 0.9718E-01 5 1.0 1.4 10000.0 184.14 753.69 118.37 NO 25000. 0.8748E-01 5 1.0 1.4 10000.0 184.14 916.79 127.26 NO 30000. 0.7907E-01 5 1.0 1.4 10000.0 184.14 1075.50 135.18 NO 40000. 0.6575E-01 5 1.0 1.4 10000.0 184.14 1382.47 148.96 NO 50000. 0.5683E-01 6 1.0 1.7 10000.0 149.22 1117.99 86.77 NO



*** INVERSION BREAK-UP FUMIGATION CALC. *** CONC (UG/M**3) = 0.2440 DIST TO MAX (M) = 11692.00



INV BREAKUP FUMI 0.2440 11692. --

Page 2

FLR-02.OUT 03/08/16 09:12:24 *** SCREEN3 MODEL RUN *** *** VERSION DATED 13043 ***

FLR-02

SIMPLE TERRAIN INPUTS: SOURCE TYPE = FLARE EMISSION RATE (G/S) = 0.126000 FLARE STACK HEIGHT (M) = 9.1440 TOT HEAT RLS (CAL/S) = 0.522905E+07 RECEPTOR HEIGHT (M) = 0.0000 URBAN/RURAL OPTION = RURAL EFF RELEASE HEIGHT (M) = 16.5634 BUILDING HEIGHT (M) = 0.0000 MIN HORIZ BLDG DIM (M) = 0.0000 MAX HORIZ BLDG DIM (M) = 0.0000






DIST CONC U10M USTK MIX HT PLUME SIGMA SIGMA (M) (UG/M**3) STAB (M/S) (M/S) (M) HT (M) Y (M) Z (M) DWASH ------- ---------- ---- ----- ----- ------ ------ ------ ------ ----- 52. 0.2267E-04 6 1.0 1.3 10000.0 116.08 21.34 21.27 NO 100. 0.1083E-01 5 1.0 1.2 10000.0 140.59 35.96 35.61 NO 200. 0.1212E-01 5 1.0 1.2 10000.0 140.59 37.30 35.98 NO 300. 0.3808E-01 4 20.0 21.6 6400.0 40.93 23.00 12.80 NO 400. 0.1523 4 20.0 21.6 6400.0 40.93 29.89 16.10 NO 500. 0.2738 4 20.0 21.6 6400.0 40.93 36.63 19.23 NO 600. 0.3553 4 20.0 21.6 6400.0 40.93 43.24 22.24 NO 700. 0.3952 4 20.0 21.6 6400.0 40.93 49.74 25.15 NO 800. 0.4035 4 20.0 21.6 6400.0 40.93 56.07 27.80 NO 900. 0.3963 4 20.0 21.6 6400.0 40.93 62.33 30.40 NO 1000. 0.3806 4 20.0 21.6 6400.0 40.93 68.53 32.95 NO 1100. 0.3587 4 20.0 21.6 6400.0 40.93 74.68 34.93 NO 1200. 0.3370 4 20.0 21.6 6400.0 40.93 80.78 36.85 NO 1300. 0.3164 4 15.0 16.2 4800.0 50.57 87.09 39.28 NO 1400. 0.3039 4 15.0 16.2 4800.0 50.57 93.08 41.08 NO 1500. 0.2911 4 15.0 16.2 4800.0 50.57 99.04 42.84 NO 1600. 0.2783 4 15.0 16.2 4800.0 50.57 104.97 44.56 NO 1700. 0.2659 4 15.0 16.2 4800.0 50.57 110.85 46.25 NO 1800. 0.2540 4 15.0 16.2 4800.0 50.57 116.71 47.90 NO 1900. 0.2425 4 15.0 16.2 4800.0 50.57 122.53 49.53 NO 2000. 0.2326 4 10.0 10.8 3200.0 68.77 128.81 52.32 NO 2100. 0.2270 4 10.0 10.8 3200.0 68.77 134.56 53.86 NO 2200. 0.2214 4 10.0 10.8 3200.0 68.77 140.28 55.37 NO 2300. 0.2156 4 10.0 10.8 3200.0 68.77 145.98 56.87 NO 2400. 0.2098 4 10.0 10.8 3200.0 68.77 151.65 58.34 NO 2500. 0.2040 4 10.0 10.8 3200.0 68.77 157.30 59.79 NO 2600. 0.1983 4 10.0 10.8 3200.0 68.77 162.93 61.23 NO

Page 1

FLR-02.OUT 2700. 0.1928 4 10.0 10.8 3200.0 68.77 168.54 62.65 NO 2800. 0.1873 4 10.0 10.8 3200.0 68.77 174.12 64.05 NO 2900. 0.1820 4 10.0 10.8 3200.0 68.77 179.69 65.43 NO 3000. 0.1811 5 2.5 3.0 10000.0 107.95 140.58 49.64 NO 3500. 0.2000 5 2.0 2.4 10000.0 115.01 161.23 54.01 NO 4000. 0.2171 5 1.5 1.8 10000.0 124.91 181.71 58.61 NO 4500. 0.2271 5 1.0 1.2 10000.0 140.59 202.21 63.61 NO 5000. 0.2379 5 1.0 1.2 10000.0 140.59 221.71 66.02 NO 5500. 0.2461 5 1.0 1.2 10000.0 140.59 241.04 68.36 NO 6000. 0.2521 5 1.0 1.2 10000.0 140.59 260.19 70.62 NO 6500. 0.2563 5 1.0 1.2 10000.0 140.59 279.20 72.81 NO 7000. 0.2590 5 1.0 1.2 10000.0 140.59 298.05 74.94 NO 7500. 0.2603 5 1.0 1.2 10000.0 140.59 316.76 77.01 NO 8000. 0.2606 5 1.0 1.2 10000.0 140.59 335.35 79.03 NO 8500. 0.2601 5 1.0 1.2 10000.0 140.59 353.80 81.00 NO 9000. 0.2588 5 1.0 1.2 10000.0 140.59 372.13 82.93 NO 9500. 0.2570 5 1.0 1.2 10000.0 140.59 390.35 84.81 NO 10000. 0.2546 5 1.0 1.2 10000.0 140.59 408.46 86.65 NO 15000. 0.2179 5 1.0 1.2 10000.0 140.59 584.46 101.92 NO 20000. 0.1995 6 1.0 1.3 10000.0 116.08 501.76 66.66 NO 25000. 0.1834 6 1.0 1.3 10000.0 116.08 610.41 70.81 NO 30000. 0.1691 6 1.0 1.3 10000.0 116.08 716.15 74.48 NO 40000. 0.1434 6 1.0 1.3 10000.0 116.08 920.66 79.73 NO 50000. 0.1247 6 1.0 1.3 10000.0 116.08 1117.78 84.14 NO





Page 2


Impacts AnalysisAlternate NO2 background concentration - Monitor Representativeness Justification

Reported emissions within 10 km of the Patton Trust South Production Facility Site Location: 28.8931 -97.8346

Account RN Site Reporting Year County NOx (tpy) Within 10 km? Latitude Longitude Distance (km)KA0018C RN100212612 RED EWALD 2014 Karnes 0 Yes 28.8550 -97.8839 6.41KA0030M RN102743788 BURNELL STATION 2014 Karnes 48.72 No 28.6997 -97.8282 21.52KA0039R RN100218346 MARKET STREET PLANT 2014 Karnes 0 Yes 28.8808 -97.8972 6.25KA0041H RN102318565 RIDDLEVILLE PLANT 2014 Karnes 0 Yes 28.9018 -97.9034 6.77KAA004D RN106106073 FALLS CITY COMPRESSOR STATION 2014 Karnes 12.09 No 28.8983 -98.0217 18.22KAA005E RN106005432 AREA 71 CGP FACILITY 2014 Karnes 103.65 Yes 28.8569 -97.7910 5.85KAA009I RN106248123 TURNBULL 5 & 6 PRODUCTION FACILITY 2014 Karnes 4.19 No 28.8061 -98.0397 22.20KAA010J RN106331515 KENEDY GAS PLANT 2014 Karnes 116.17 No 28.7544 -98.0097 23.00KAA011K RN106615727 TURNBULL 7 15 PRODUCTION FACILITY 2014 Karnes 1.28 No 28.7622 -98.0381 24.59KAA012L RN106173891 JULIE BECK NORTH GATHERING FACILITY 2014 Karnes 0.50 No 28.7817 -98.0727 26.30KAA013M RN106322357 SOUTH SUGARLOAF CENTRAL FACILITY 2014 Karnes 34.55 No 28.7350 -98.0258 25.62KAA014N RN106322647 WEST SUGARLOAF CENTRAL FACILITY 2014 Karnes 51.56 No 28.7906 -97.9939 19.26KAA016P RN107116956 CENTRAL LONGHORN CENTRAL FACILITY 2014 Karnes 19.60 Yes 28.9003 -97.9386 10.16KAA017Q RN106278328 EAST LONGHORN CENTRAL FACILITY 2014 Karnes 23.85 Yes 28.8701 -97.9305 9.69KAA018R RN106322423 EAST SUGARLOAF CENTRAL FACILITY 2014 Karnes 80.84 No 28.8239 -97.9387 12.73

Total reported NOx emissions within 10 km of the site (tpy) 147.09

Reported emissions within 10 km of the Corsicana Airport Monitor Monitor Location: 32.0319 -96.3991

Account RN Site Reporting Year County NOx (tpy) Within 10 km? Latitude Longitude Distance (km)NB0014R RN100221811 GUARDIAN INDUSTRIES CORSICANA 2014 Navarro 2,189.55 Yes 32.0642 -96.4269 4.44NB0024O RN100216266 SUNOCO PIPELINE STATION 2014 Navarro 0.02 Yes 32.0706 -96.4636 7.44NB0037F RN100211283 STREETMAN PLANT 2014 Navarro 664.84 No 31.9143 -96.3478 13.95NB0063E RN100215664 TRAVEL TRAILER MFG 2014 Navarro 0 No 32.1907 -96.4717 18.93NB0089J RN100220896 PACTIV CORSICANA 2014 Navarro 9.69 Yes 32.1028 -96.4394 8.75NB0154A RN102887064 FROST STATION 2014 Navarro 0.77 No 32.0644 -96.8636 43.92

Total reported NOx emissions within 10 km of the Corsicana Airport monitor (tpy) 2,199.26




APPENDIX C GAS AND LIQUID ANALYSES



Where was the sample taken?

Sample type?

Who analyzed the sample? Temperature (F): 92

Date of sample: Pressure (psig): 115

Component mole %Molecular Weight

(grams/mole)grams per 100 moles of gas

weight %

hydrogen 0.000 1.008 0 0.000

helium 0.000 4.003 0 0.000

nitrogen 0.081 28.013 2.258 0.098

CO2 1.454 44.010 63.977 2.779

H2S 0.006 34.082 0.211 0.009

methane (C1) 72.420 16.042 1,161.802 50.467

ethane (C2) 13.851 30.069 416.487 18.092

propane (C3) 6.606 44.096 291.303 12.654

iso-butane (C4) 1.326 58.122 77.077 3.348

nor-butane (C4) 2.253 58.122 130.966 5.689

iso-pentane (C5) 0.720 72.149 51.939 2.256

nor-pentane (C5) 0.599 72.149 43.243 1.878

hexanes (C6) 0.271 86.170 23.345 1.014

heptanes (C7) 0.137 100.200 13.740 0.597

octanes (C8) 0.048 114.230 5.447 0.237

nonanes (C9) 0.009 128.260 1.160 0.050

decanes (C10+) 0.000 142.290 0.005 0.000

n-hexanes 0.163 86.170 14.016 0.609

2,2,4-trimethylpentane 0.000 114.23 0 0.000

benzene 0.016 78.110 1.249 0.054

toluene 0.025 92.140 2.308 0.100

ethylbenzene 0.003 106.170 0.293 0.013

xylenes (M,P,O) 0.012 106.170 1.272 0.055

TOTALS: 100.000 100.000

VOC (Non-methane, Non-ethane hydrocarbons)

VOC content of total sample VOC content of hydrocarbon fraction only

VOC weight% = 28.555 VOC weight% = 29.404

VOC weight fraction = 0.286 VOC weight fraction = 0.294

HYDROGEN SULFIDE Constants:

H2S weight% = 0.0092 453.59237 mol/lb-mol

H2S weight fraction = 9.17E-05 0.06479891 grams/grainH2S ppmV = 61.94356403 SOUR GAS

H2S ppmWT= 91.71 Notes:H2S grains/100 SCF = 3.8363

BENZENE

Benzene content of total sample Benzene content of hydrocarbon fraction only

Benzene weight% = 0.054 Benzene weight% = 0.056

Benzene weight fraction = 0.001 Benzene weight fraction = 0.001

TOTAL HAPS

HAPs content of total sample HAPs content of hydrocarbon fraction only

HAPs weight% = 0.831 HAPs weight% = 0.856

HAPs weight fraction = 0.008 HAPs weight fraction = 0.009

Gas Molecular Weight = 23.02 Constants: 28.97 MWair

Gas Specific Gravity = 0.79 385.22 scf/lb-mol

Gas and Liquid Analyses

Gas Analysis

NA

ProMax Run

Gas

Separator Gas (ProMax Stream LP Sep Gas)

H2S mole fraction from monthly Draeger tube readings


Patton Trust South Production FacilityGas and Liquid Analyses


Sample type?





weight %

hydrogen 0.000 1.008 0 0.000

helium 0.000 4.003 0 0.000

nitrogen 0.000 28.013 1.6E-04 0.000

CO2 0.034 44.010 1.510 0.014

H2S 0.001 34.082 0.029 0.000

methane (C1) 0.075 16.042 1.201 0.011

ethane (C2) 0.674 30.069 20.278 0.184

propane (C3) 2.715 44.096 119.705 1.086

iso-butane (C4) 1.900 58.122 110.447 1.002

nor-butane (C4) 4.838 58.122 281.211 2.550

iso-pentane (C5) 4.253 72.149 306.814 2.783

nor-pentane (C5) 4.735 72.149 341.641 3.098

hexanes (C6) 5.184 86.170 446.667 4.051

heptanes (C7) 10.490 100.200 1,051.103 9.533

octanes (C8) 10.790 114.230 1,232.596 11.179

nonanes (C9) 5.709 128.260 732.252 6.641

decanes (C10+) 37.373 142.290 5,317.823 48.228

n-hexanes 4.231 86.170 364.611 3.307


benzene 0.432 78.110 33.745 0.306

toluene 2.304 92.140 212.310 1.925

ethylbenzene 0.697 106.170 74.031 0.671

xylenes (M,P,O) 3.563 106.170 378.335 3.431

TOTALS: 100.000 100.000





HYDROGEN SULFIDE

H2S weight% = 0.0003

H2S weight fraction = 2.66E-06H2S ppmV = 8.61 Notes:

H2S ppmWT= 2.66

BENZENE




TOTAL HAPS




Liquid Molecular Weight = 110.26 Constants: 28.97 MWair

Liquid Specific Gravity = 3.81 385.22 scf/lb-mol

H2S mole fraction from monthly Draeger tube readings

Liquid Analysis

NA

ProMax Run

Liquid

Sales Oil Liquid (ProMax Stream Outlet Oil)




Sample type?





weight %

hydrogen 0.000 1.008 0 0.000

helium 0.000 4.003 0 0.000

nitrogen 0.000 28.013 8.4E-07 0.000

CO2 0.002 44.010 0.087 0.001

H2S 0.000 34.082 0.008 0.000

methane (C1) 0.002 16.042 0.035 0.000

ethane (C2) 0.225 30.069 6.761 0.080

propane (C3) 3.110 44.096 137.130 1.629

iso-butane (C4) 3.875 58.122 225.248 2.676

nor-butane (C4) 11.536 58.122 670.515 7.965

iso-pentane (C5) 10.672 72.149 769.984 9.147

nor-pentane (C5) 11.932 72.149 860.848 10.226

hexanes (C6) 12.256 86.170 1,056.109 12.546

heptanes (C7) 16.870 100.200 1,690.369 20.080

octanes (C8) 9.798 114.230 1,119.220 13.296

nonanes (C9) 2.423 128.260 310.725 3.691

decanes (C10+) 0.013 142.290 1.892 0.022

n-hexanes 9.576 86.170 825.170 9.802


benzene 0.932 78.110 72.826 0.865

toluene 3.452 92.140 318.052 3.778

ethylbenzene 0.596 106.170 63.262 0.752

xylenes (M,P,O) 2.729 106.170 289.779 3.442

TOTALS: 100.000 100.000





HYDROGEN SULFIDE



H2S ppmWT= 0.99

BENZENE




TOTAL HAPS




Liquid Molecular Weight = 84.18 Constants: 28.97 MWair

Liquid Specific Gravity = 2.91 385.22 scf/lb-mol

H2S mole fraction from monthly Draeger tubes readings

Drip Liquid Analysis

Drip Liquid (ProMax Stream Drip Oil)

Liquid

ProMax Run

NA




Sample type?


Date of sample: Pressure (psig): 1,250



weight %

hydrogen 0.000 1.008 0 0.000

helium 0.000 4.003 0 0.000

nitrogen 0.080 28.013 2.244 0.099

CO2 1.486 44.010 65.417 2.874

H2S 0.002 34.082 0.082 0.004

methane (C1) 72.671 16.042 1,165.815 51.217

ethane (C2) 14.034 30.069 421.976 18.538

propane (C3) 6.665 44.096 293.894 12.911

iso-butane (C4) 1.290 58.122 74.976 3.294

nor-butane (C4) 2.130 58.122 123.812 5.439

iso-pentane (C5) 0.631 72.149 45.530 2.000

nor-pentane (C5) 0.511 72.149 36.903 1.621

hexanes (C6) 0.211 86.170 18.157 0.798

heptanes (C7) 0.095 100.200 9.479 0.416

octanes (C8) 0.030 114.230 3.405 0.150

nonanes (C9) 0.005 128.260 0.656 0.029

decanes (C10+) 0.000 142.290 0.018 0.001

n-hexanes 0.122 86.170 10.528 0.463


benzene 0.012 78.110 0.934 0.041

toluene 0.016 92.140 1.497 0.066

ethylbenzene 0.002 106.170 0.170 0.007

xylenes (M,P,O) 0.007 106.170 0.728 0.032

TOTALS: 100.000 100.000





HYDROGEN SULFIDE



H2S ppmWT= 35.94

BENZENE




TOTAL HAPS




Fuel Molecular Weight = 22.76 Constants: 28.97 MWair

Fuel Specific Gravity = 0.79 385.22 scf/lb-mol

H2S mole fraction from monthly Draeger tubes readings

Fuel Gas Analysis

Fuel Gas (ProMax Stream Outlet Gas)

Gas

ProMax Run

NA


Sales Oil Breathing/Working Vapor Composition

Breathing/Working vapor for: Sales Oil Liquid (ProMax Stream Outlet Oil)

Maximum temperature of bulk liquid (°R): 563.29 (from AP-42 Tanks calculations)

CompoundMolecular Weight

(lb/lb-mol)mol% in liquid A B C D E Vp (mmHg) @ T mol % in vapor wt% in vapor

hydrogen 1.008 0.00% 3.4132 -41.316 1.0947 -6.7E-10 0.000146 1.99E+20 0.00% 0.00%nitrogen 28.013 0.00% 23.8572 -476.68 -8.6689 0.020128 -2.4E-11 1.00E+7 3.82% 2.88%CO2 44.010 0.03% 35.0169 -1511.9 -11.334 0.009337 1.71E-09 66,691.2 1.56% 1.85%H2S 34.082 0.00% 18.6383 -1344.6 -4.1034 3.18E-09 2.47E-06 22,042.9 0.01% 0.01%methane (C1) 16.042 0.07% 14.6667 -570.97 -3.3373 2.2E-09 1.31E-05 625,962.7 32.05% 13.84%ethane (C2) 30.069 0.67% 20.6973 -1134.1 -5.2514 -9.9E-11 6.73E-06 42,457.9 19.58% 15.85%propane (C3) 44.096 2.71% 21.4469 -1462.7 -5.261 3.28E-11 3.73E-06 10,231.9 18.99% 22.55%iso-butane (C4) 58.122 1.90% 31.2541 -1953.2 -8.806 8.92E-11 5.75E-06 3,987.5 5.18% 8.11%nor-butane (C4) 58.122 4.84% 27.0441 -1904.9 -7.1805 -6.7E-11 4.22E-06 2,828.0 9.36% 14.64%iso-pentane (C5) 72.149 4.25% 29.2963 -2176.2 -7.883 -4.7E-11 3.9E-06 1,128.2 3.28% 6.37%nor-pentane (C5) 72.149 4.74% 33.3239 -2422.7 -9.2354 9.02E-11 4.11E-06 866.1 2.80% 5.45%hexanes (C6) 86.170 5.18% 30.7477 -2488.8 -8.2295 -2.4E-11 3.24E-06 376.4 1.33% 3.10%heptanes (C7) 100.200 10.49% 65.0257 -3818.8 -21.684 0.010387 1.02E-14 91.5 0.66% 1.77%octanes (C8) 114.230 10.79% 29.0948 -3011.4 -7.2653 -2.3E-11 1.47E-06 30.6 0.23% 0.69%nonanes (C9) 128.260 5.71% 8.8817 -2804.2 1.5262 -0.01046 5.8E-06 10.5 0.04% 0.14%decanes (C10+) 142.290 37.37% 26.5125 -3358.4 -6.1174 -3.3E-10 4.86E-07 3.7 0.09% 0.36%n-hexanes 86.170 4.23% 69.7378 -3627.8 -23.927 0.01281 -1.7E-13 278.6 0.81% 1.87%2,2,4-trimethylpentane 114.230 0.00% 50.3422 -3278.9 -16.111 0.007426 -9.2E-14 96.4 0.00% 0.00%benzene 78.110 0.43% 31.7718 -2725.4 -8.4443 -5.4E-09 2.72E-06 180.5 0.05% 0.11%toluene 92.140 2.30% 34.0775 -3037.9 -9.1635 1.03E-11 2.7E-06 58.5 0.09% 0.23%ethylbenzene 106.170 0.70% 36.1998 -3340.2 -9.797 -1.1E-11 2.58E-06 21.4 0.01% 0.03%xylenes (M,P,O) 106.170 3.56% 34.6803 -3298.1 -9.257 -4.4E-10 2.41E-06 18.9 0.05% 0.13%

Benzene wt% = 0.001

H2S wt% = 0.000

HAPs wt% = 0.024

Vapor MW (lb/lb-mol) = 36.07

Notes:

Vapor pressure calculation methodology and factors from Chapter 7 "Vapor Pressure" of "Chemical Properties Handbook - Physical, Thermodynamic, Environmental, Transport, Safety, and Health Related Properties for Organic and Inorganic Chemicals", Carl L. Yaws, McGraw-Hill.

log10(Vp) = A + B/T + C log10(T) + D T + E T2

Vp = Vapor Pressure (mmHg)A, B, C, D, E = regeression coefficients for chemical compoundsT = Maximum temperature of bulk liquid (K, from AP-42 Tanks Calculations)


Gas Oil Ratio (GOR) Method - Flash AnalysisTanks GOR calculator

Gas Oil Ratio: 0.0

Pollutant mole %molecular

weight (grams/mole)

grams per 100

moles of gas

weight %

nitrogen 100.000 28.01 2801.348 100.000 0.000

CO2 0.000 44.01 0.000 0.000 0.000

H2S 0.000 34.08 0.000 0.000 0.000

methane (C1) 0.000 16.04 0.000 0.000 HAPs wt% = 0.000

ethane (C2) 0.000 30.07 0.000 0.000 Flash Gas MW = 28.013

propane (C3) 0.000 44.10 0.000 0.000

iso-butane (C4) 0.000 58.12 0.000 0.000

nor-butane (C4) 0.000 58.12 0.000 0.000

iso-pentane (C5) 0.000 72.15 0.000 0.000

nor-pentane (C5) 0.000 72.15 0.000 0.000

hexanes (C6) 0.000 86.18 0.000 0.000

heptane (C7+) 0.000 100.20 0.000 0.000

octane (C8+) 0.000 114.23 0.000 0.000

nonane (C9+) 0.000 128.26 0.000 0.000

decane (C10+) 0.000 142.29 0.000 0.000

n-hexane 0.000 86.18 0.000 0.000

2,2,4-trimethylpentane 0.000 114.23 0.000 0.000

benzene 0.000 78.11 0.000 0.000

toluene 0.000 92.14 0.000 0.000

ethylbenzene 0.000 106.17 0.000 0.000

xylenes (M, P, O) 0.000 106.17 0.000 0.000

TOTALS: 100.000 100.000

GOR Calculator:

Sample Pressure (psig):

VOC wt% =

H2S wt% =

Flash Gas Speciation:

Benzene wt% =


Patton Trust South PF - Oil Tank Flash (ProMax) - Flash Analysis

Oil Tank Flash (ProMax Stream Tank Flash)

Promax Run

NA

This table can be used to calculate the flash gas molecular weight and the component weight percents if needed, if the flash gas mole percents are entered.

75Sample Temperature (F):

Date of sample:

Who analyzed the sample?


in standard cubic feet of flash gas per barrel (SCF/bbl) of produced oil/condensate


Gas Oil Ratio (GOR) Method - Flash AnalysisTanks GOR calculator

Gas Oil Ratio: 114.7


weight (grams/mole)

grams per 100

moles of gas

weight %

nitrogen 0.000 28.01 0.001 0.000 96.101

CO2 0.139 44.01 6.131 0.108 0.256

H2S 0.006 34.08 0.203 0.004 0.004

methane (C1) 0.436 16.04 6.995 0.123 HAPs wt% = 3.515


propane (C3) 27.769 44.10 1224.492 21.563

iso-butane (C4) 13.176 58.12 765.846 13.486

nor-butane (C4) 26.580 58.12 1544.892 27.205

iso-pentane (C5) 9.821 72.15 708.602 12.478

nor-pentane (C5) 8.164 72.15 589.055 10.373

hexanes (C6) 3.369 86.18 290.330 5.113

heptane (C7+) 1.093 100.20 109.560 1.929

octane (C8+) 0.200 114.23 22.856 0.402

nonane (C9+) 0.016 128.26 2.044 0.036

decane (C10+) 0.000 142.29 0.000 0.000

n-hexane 1.886 86.18 162.573 2.863


benzene 0.186 78.11 14.535 0.256

toluene 0.186 92.14 17.102 0.301

ethylbenzene 0.011 106.17 1.118 0.020

xylenes (M, P, O) 0.040 106.17 4.294 0.076

TOTALS: 100.000 100.000


VOC wt% =

Benzene wt% =H2S wt% =




GOR Calculator: Patton Trust South PF - Drip Tank Flash (ProMax) - Flash Analysis

Sample Temperature (F): 75

Where was the sample taken? Drip Tank Flash (ProMax Stream Drip Tank Flash)

Who analyzed the sample? Promax Run

Date of sample: NA



Gas Oil Ratio (GOR) Method - Flash AnalysisVRT GOR calculator

Gas Oil Ratio: 48.8


weight (grams/mole)

grams per 100

moles of gas

weight %

nitrogen 0.003 28.01 0.074 0.002 79.107

CO2 1.627 44.01 71.585 1.573 0.212

H2S 0.017 34.08 0.593 0.013 0.013

methane (C1) 12.931 16.04 207.439 4.559 HAPs wt% = 3.237


propane (C3) 26.906 44.10 1186.455 26.076

iso-butane (C4) 7.622 58.12 443.004 9.736

nor-butane (C4) 14.019 58.12 814.817 17.908

iso-pentane (C5) 5.021 72.15 362.237 7.961

nor-pentane (C5) 4.307 72.15 310.754 6.830

hexanes (C6) 2.046 86.18 176.301 3.875

heptane (C7+) 1.064 100.20 106.594 2.343

octane (C8+) 0.374 114.23 42.692 0.938

nonane (C9+) 0.072 128.26 9.189 0.202

decane (C10+) 0.000 142.29 0.044 0.001

n-hexane 1.242 86.18 106.999 2.352


benzene 0.123 78.11 9.627 0.212

toluene 0.198 92.14 18.203 0.400

ethylbenzene 0.022 106.17 2.320 0.051

xylenes (M, P, O) 0.095 106.17 10.129 0.223

TOTALS: 100.000 100.000


GOR Calculator:

NA

Patton Trust South PF - VRT Gas (ProMax) - Flash Analysis

VRT Gas (ProMax Stream VRT Gas)

VOC wt% =



5

104


Sample Temperature (F):

Date of sample:



Promax Run




Gas Oil Ratio (GOR) Method - Flash AnalysisDrip VRT GOR calculator

Gas Oil Ratio: 143.4


weight (grams/mole)

grams per 100

moles of gas

weight %

nitrogen 0.001 28.01 0.029 0.001 85.562

CO2 0.769 44.01 33.846 0.703 0.155

H2S 0.013 34.08 0.453 0.009 0.009

methane (C1) 6.471 16.04 103.813 2.156 HAPs wt% = 2.080


propane (C3) 31.889 44.10 1406.165 29.198

iso-butane (C4) 10.131 58.12 588.814 12.226

nor-butane (C4) 18.315 58.12 1064.487 22.103

iso-pentane (C5) 5.749 72.15 414.769 8.612

nor-pentane (C5) 4.608 72.15 332.454 6.903

hexanes (C6) 1.745 86.18 150.345 3.122

heptane (C7+) 0.522 100.20 52.314 1.086

octane (C8+) 0.090 114.23 10.321 0.214

nonane (C9+) 0.007 128.26 0.864 0.018

decane (C10+) 0.000 142.29 0.000 0.000

n-hexane 0.952 86.18 82.068 1.704


benzene 0.096 78.11 7.470 0.155

toluene 0.089 92.14 8.179 0.170

ethylbenzene 0.005 106.17 0.508 0.011

xylenes (M, P, O) 0.018 106.17 1.929 0.040

TOTALS: 100.000 100.000

GOR Calculator: Drip VRT - Flash Analysis

Where was the sample taken? Drip VRT Gas (ProMax Stream Drip VRT Gas)

Who analyzed the sample? Promax Run

Date of sample: NA

Sample Temperature (F): 60

Sample Pressure (psig): 4




VOC wt% =




Gas Oil Ratio (GOR) Method - Flash AnalysisHT GOR calculator

Gas Oil Ratio: 68.0


weight (grams/mole)

grams per 100

moles of gas

weight %

nitrogen 0.025 28.01 0.703 0.023 50.182

CO2 2.086 44.01 91.806 3.001 0.111

H2S 0.013 34.08 0.434 0.014 0.014

methane (C1) 47.958 16.04 769.361 25.149 HAPs wt% = 1.716


propane (C3) 14.121 44.10 622.690 20.354

iso-butane (C4) 3.121 58.12 181.406 5.930

nor-butane (C4) 5.443 58.12 316.372 10.342

iso-pentane (C5) 1.811 72.15 130.658 4.271

nor-pentane (C5) 1.539 72.15 111.011 3.629

hexanes (C6) 0.723 86.18 62.317 2.037

heptane (C7+) 0.386 100.20 38.692 1.265

octane (C8+) 0.140 114.23 15.975 0.522

nonane (C9+) 0.028 128.26 3.535 0.116

decane (C10+) 0.000 142.29 0.022 0.001

n-hexane 0.440 86.18 37.929 1.240


benzene 0.043 78.11 3.386 0.111

toluene 0.071 92.14 6.550 0.214

ethylbenzene 0.008 106.17 0.860 0.028

xylenes (M, P, O) 0.036 106.17 3.774 0.123

TOTALS: 100.000 100.000


VOC wt% =


Patton Trust South PF - HT Gas (ProMax) - Flash Analysis

HT Gas (ProMax Stream 11)

Promax Run

GOR Calculator:


Sample Temperature (F):

Date of sample:




50

110


NA





APPENDIX D GRAPHICS: AREA MAP, PROCESS FLOW DIAGRAM

Encana Oil & Gas (USA) Inc.Karnes County, Texas

Drafted By:J. Knowles

Project No.:014344.026

Reviewed By:C. Cros

Datum: GCS NAD 1983UTM Zone 14Map Sources: ESRI- Streets Basemap& 2014 NAIP TX Imageryq

AREA MAPPatton Trust South Production Facility

Patton Trust South Production Facility28.893137°N, 97.83456°W

!. Facility Location1/4 Mile RadiusPad Boundary

!(

Date: 8/11/2015

H:\Encana Oil & Gas\014344 Eagleford Air Permitting\000b - GIS\ArcMap\AreaMaps\PattonTrustSouthPF.mxd

0 0.5 1Miles

0 0.5 1Kilometers

1:24,000Scale

Process Flow Diagram


Drafted By:

B. Au

Encana Oil & Gas (USA) Inc. - Karnes County, TexasReviewed By:

C. Cros

Project No:

016056

Date:

3/8/2016

Oil/Condensate

Sour Gas

Full Well Stream

Sweet Gas

Produced Water

Vapors

FIN: VRT-GAS,

DRIPVRT-GAS

Utility Flare

FLR-01

Gas Sales

and Gas Lift

Gas Cooler Engines

ENG-07 – ENG-08

Gas

Sweetening

Unit

Scrubber

Process Flare

FLR-02

VRU Compressor

Engines

ENGVRU-01 –

ENGVRU-03

Flash Compressor

Engine

ENG-04 - ENG-06

Production VRTs

Drip VRT

Oil Heater Treaters

HTR-01 – HTR-04

HTR-06 – HTR-08

IP Compressor

Engines

ENG-01 – ENG-03

Inlet

Separators

Production

Wells

Produced Water Tanks

PWTK-01 – PWTK-05

Water Heater Treater

HTR-05

Oil

Sales

Pipeline

Truck Loading

LOAD

Oil/Condensate Tanks

OILTK-01 – OILTK-22LACT

FIN

: P

RO

D-G

AS

Dehydration Unit

HTR-09, DEHY-01

LP Drip

Scrubber

Line Heater

HTR-10

Fuel System

Fuel Conditioning

Unit

VRU Compressor

Engine

ENGVRU-04

Oil/Condensate

Tank

OILTK-23

Storage at Patton

Trust North PF

Blower

Process

Liquids




APPENDIX E SUPPORTING DOCUMENTS

Apr 07, 2015

Re: Engine Pedigree for Exterran Compressor Unit 805949, Engine Serial Number JEF03175

In order to better assist your company with any of its state and federal permitting needs, Exterran submits the

following information in regards to the engine of the above-referenced compressor unit, which Exterran is currently

utilizing to provide your company contract compression services. This letter should provide information necessary to

answer questions pertaining to, but not limited to, the New Source Performance Standards (NSPS) for Stationary

Spark Ignition Internal Combustion Engines, Subpart JJJJ. This information is current as of Apr 07, 2015.

Exterran

QHSE and Operations Services

16666 Northchase Drive

Houston, Texas 77060 U.S.A.

Main 281.836.7000

Fax 281.836.8161

www.exterran.com

Brendan Haigney

EXTERRAN

1600 Broadway Suite 500Denver, CO 80202

Engine Make: CATERPILLAR

Engine Model: G3516B

Engine Serial Number: JEF03175

Engine Type: 4 Stroke LB

Engine Category: New

Engine Subcategory: Non Certified

Engine NSPS Status*: Non-Exempt

Engine Speed: 1400.00

OEM Rated HP: 1380.00

Engine Manufacture Date: Nov 19, 2014

Last Overhaul Date:

Reconstruction %: 0.00 %

NSPS Startup Date:

Customer: N/A

Business Unit: N/A

Exterran Unit Number: 805949

Customer Lease Name: N/A

Please contact Kyle Poycker with any questions at or [email protected].

* The "Engine NSPS Status" herein is based on Exterran's present knowledge of the engine in question and its

reading of U.S. EPA's regulations and guidance pursuant to 40 C.F.R. Part 60, Subpart JJJJ. Any change in law or

in the federal, state, or local interpretation of existing law could result in this engine being subject to additional or

different legal requirements. These conclusions are Exterran's and are not offered as legal opinions or advice to

your company. Additionally, any reconstruction or modification respecting this engine (as those terms are defined in

the applicable regulations) could result in the applicability of Subpart JJJJ or other legal requirements to this engine

and create legal compliance responsibilities for your company.

G3516B GAS ENGINE SITE SPECIFIC TECHNICAL DATAGAS COMPRESSION APPLICATION

PREPARED BY:Data generated by Gas Engine Rating Pro Version 4.01.00Ref. Data Set DM8800-05-001, Printed 05Jan2012 Page 1 of 4

ENGINE SPEED (rpm): 1400 FUEL SYSTEM: CAT WIDE RANGECOMPRESSION RATIO: 8:1 WITH AIR FUEL RATIO CONTROLAFTERCOOLER - STAGE 2 INLET (°F): 130 SITE CONDITIONS:AFTERCOOLER - STAGE 1 INLET (°F): 201 FUEL: Nat GasJACKET WATER OUTLET (°F): 210 FUEL PRESSURE RANGE(psig): 7.0-50.0ASPIRATION: TA FUEL METHANE NUMBER: 84.8COOLING SYSTEM: JW+OC+1AC, 2AC FUEL LHV (Btu/scf): 905IGNITION SYSTEM: ADEM3 ALTITUDE(ft): 500EXHAUST MANIFOLD: DRY MAXIMUM INLET AIR TEMPERATURE(°F): 77COMBUSTION: Ultra Lean Burn STANDARD RATED POWER: 1380 bhp@1400rpmNOx EMISSION LEVEL (g/bhp-hr NOx): 0.5SET POINT TIMING: 30

MAXIMUMRATING

SITE RATING AT MAXIMUMINLET AIR TEMPERATURE

RATING NOTES LOAD 100% 100% 75% 50% ENGINE POWER (WITHOUT FAN) (1) bhp 1380 1380 1035 690

INLET AIR TEMPERATURE °F 77 77 77 77

ENGINE DATA FUEL CONSUMPTION (LHV) (2) Btu/bhp-hr 7443 7443 7972 8562

FUEL CONSUMPTION (HHV) (2) Btu/bhp-hr 8256 8256 8843 9498

AIR FLOW (77°F, 14.7 psia) (WET) (3)(4) scfm 3126 3126 2452 1715

AIR FLOW (WET) (3)(4) lb/hr 13862 13862 10874 7602

INLET MANIFOLD PRESSURE (5) in Hg(abs) 94.6 94.6 76.8 54.0

EXHAUST TEMPERATURE - ENGINE OUTLET (6) °F 992 992 986 1006

EXHAUST GAS FLOW (@engine outlet temp, 14.5 psia) (WET) (7)(4) ft3/min 9126 9126 7138 5065

EXHAUST GAS MASS FLOW (WET) (7)(4) lb/hr 14380 14380 11290 7900

EMISSIONS DATA - ENGINE OUT NOx (as NO2) (8)(9) g/bhp-hr 0.50 0.50 0.50 0.50

CO (8)(9) g/bhp-hr 2.43 2.43 2.61 2.56

THC (mol. wt. of 15.84) (8)(9) g/bhp-hr 4.77 4.77 5.11 5.19

NMHC (mol. wt. of 15.84) (8)(9) g/bhp-hr 0.72 0.72 0.77 0.78

NMNEHC (VOCs) (mol. wt. of 15.84) (8)(9)(10) g/bhp-hr 0.48 0.48 0.51 0.52

HCHO (Formaldehyde) (8)(9) g/bhp-hr 0.44 0.44 0.43 0.42

CO2 (8)(9) g/bhp-hr 474 474 506 549

EXHAUST OXYGEN (8)(11) % DRY 9.0 9.0 8.7 8.3

HEAT REJECTION HEAT REJ. TO JACKET WATER (JW) (12) Btu/min 23412 23412 21533 19930

HEAT REJ. TO ATMOSPHERE (12) Btu/min 6110 6110 5092 4074

HEAT REJ. TO LUBE OIL (OC) (12) Btu/min 4475 4475 3978 3363

HEAT REJ. TO A/C - STAGE 1 (1AC) (12)(13) Btu/min 10046 10046 8308 2813


COOLING SYSTEM SIZING CRITERIA TOTAL JACKET WATER CIRCUIT (JW+OC+1AC) (13)(14) Btu/min 41672

TOTAL AFTERCOOLER CIRCUIT (2AC) (13)(14) Btu/min 5626

A cooling system safety factor of 0% has been added to the cooling system sizing criteria.

CONDITIONS AND DEFINITIONSEngine rating obtained and presented in accordance with ISO 3046/1, adjusted for fuel, site altitude and site inlet air temperature. 100% rating at maximum inlet air temperature is the maximum enginecapability for the specified fuel at site altitude and maximum site inlet air temperature. Max. rating is the maximum capability for the specified fuel at site altitude and reduced inlet air temperature.Lowest load point is the lowest continuous duty operating load allowed. No overload permitted at rating shown.

For notes information consult page three.


Engine Power vs. Inlet Air TemperatureData represents temperature sweep at 500 ft and 1400 rpm

Max Continuous Power vs.Speed Capabilityfor Site Conditions

No Rating AvailableRange for Site Conditions

Continuous OperatingRange for Site Conditions

Low Load IntermittentOperating Range

Air Temperature, °FAir Temperature, °FAir Temperature, °FAir Temperature, °F30303030 40404040 50505050 60606060 70707070 80808080 90909090 100100100100 110110110110 120120120120 130130130130

EE EEnn nn

gg ggii iinn nn

ee eePP PP

oo ooww ww

ee eerr rr,, ,,

bb bbhh hh

pp pp

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

Engine Power vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF





Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)1050105010501050 1100110011001100 1150115011501150 1200120012001200 1250125012501250 1300130013001300 1350135013501350 1400140014001400

EE EEnn nn

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ee eePP PP

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bb bbhh hh

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0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

Engine Torque vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF

Max Continuous Torque vs.Speed Capabilityfor Site Conditions





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ee eeTT TT

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0000

500500500500

1000100010001000

1500150015001500

2000200020002000

2500250025002500

3000300030003000

3500350035003500

4000400040004000

4500450045004500

5000500050005000

5500550055005500

0000

500500500500

1000100010001000

1500150015001500

2000200020002000

2500250025002500

3000300030003000

3500350035003500

4000400040004000

4500450045004500

5000500050005000

5500550055005500

Note: At site conditions of 500 ft and 77°F inlet air temp., constant torque can be maintained down to 1050 rpm.The minimum speed for loading at these conditions is 1050 rpm.



NOTES1. Engine rating is with two engine driven water pumps. Tolerance is ± 3% of full load.

2. Fuel consumption tolerance is ± 3.0% of full load data.

3. Air flow value is on a 'wet' basis. Flow is a nominal value with a tolerance of ± 5 %.

4. Inlet and Exhaust Restrictions must not exceed A&I limits based on full load flow rates from the standard technical data sheet.

5. Inlet manifold pressure is a nominal value with a tolerance of ± 5 %.

6. Exhaust temperature is a nominal value with a tolerance of (+)63°F, (-)54°F.

7. Exhaust flow value is on a "wet" basis. Flow is a nominal value with a tolerance of ± 6 %.

8. Emissions data is at engine exhaust flange prior to any after treatment.

9. Emission values are based on engine operating at steady state conditions. Fuel methane number cannot vary more than ± 3. Values listed are higher than nominal levels to allowfor instrumentation, measurement, and engine-to-engine variations. They indicate "Not to Exceed" values. THC, NMHC, and NMNEHC do not include aldehydes. An oxidationcatalyst may be required to meet Federal, State or local CO or HC requirements.

10. VOCs - Volatile organic compounds as defined in US EPA 40 CFR 60, subpart JJJJ

11. Exhaust Oxygen level is the result of adjusting the engine to operate at the specified NOx level. Tolerance is ± 0.5.

12. Heat rejection values are nominal. Tolerances, based on treated water, are ± 10% for jacket water circuit, ± 50% for radiation, ± 20% for lube oil circuit, and ± 5% for aftercoolercircuit.

13. Aftercooler heat rejection includes an aftercooler heat rejection factor for the site elevation and inlet air temperature specified. Aftercooler heat rejection values at part load arefor reference only. Do not use part load data for heat exchanger sizing.

14. Cooling system sizing criteria are maximum circuit heat rejection for the site, with applied tolerances.


Constituent Abbrev Mole % NormWater Vapor H2O 0.0000 0.0000Methane CH4 92.2700 92.2700Ethane C2H6 2.5000 2.5000Propane C3H8 0.5000 0.5000Isobutane iso-C4H1O 0.0000 0.0000Norbutane nor-C4H1O 0.2000 0.2000Isopentane iso-C5H12 0.0000 0.0000Norpentane nor-C5H12 0.1000 0.1000Hexane C6H14 0.0500 0.0500Heptane C7H16 0.0000 0.0000Nitrogen N2 3.4800 3.4800Carbon Dioxide CO2 0.9000 0.9000Hydrogen Sulfide H2S 0.0000 0.0000Carbon Monoxide CO 0.0000 0.0000Hydrogen H2 0.0000 0.0000Oxygen O2 0.0000 0.0000Helium HE 0.0000 0.0000Neopentane neo-C5H12 0.0000 0.0000Octane C8H18 0.0000 0.0000Nonane C9H20 0.0000 0.0000Ethylene C2H4 0.0000 0.0000Propylene C3H6 0.0000 0.0000TOTAL (Volume %) 100.0000 100.0000

Fuel Makeup: Nat Gas

Unit of Measure: English

Calculated Fuel PropertiesCalculated Fuel PropertiesCalculated Fuel PropertiesCalculated Fuel Properties

Caterpillar Methane Number: 84.8

Lower Heating Value (Btu/scf): 905

Higher Heating Value (Btu/scf): 1004

WOBBE Index (Btu/scf): 1168

THC: Free Inert Ratio: 21.83

Total % Inerts (% N2, CO2, He): 4.38%

RPC (%) (To 905 Btu/scf Fuel): 100%

Compressibility Factor: 0.998

Stoich A/F Ratio (Vol/Vol): 9.45

Stoich A/F Ratio (Mass/Mass): 15.75

Specific Gravity (Relative to Air): 0.600

Specific Heat Constant (K): 1.313

CONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCaterpillar Methane Number represents the knock resistance of a gaseous fuel. It should be used with the Caterpillar Fuel Usage Guide for the engine and rating to determine the rating for the fuelspecified. A Fuel Usage Guide for each rating is included on page 2 of its standard technical data sheet.

RPC always applies to naturally aspirated (NA) engines, and turbocharged (TA or LE) engines only when they are derated for altitude and ambient site conditions.

Project specific technical data sheets generated by the Caterpillar Gas Engine Rating Pro program take the Caterpillar Methane Number and RPC into account when generating a site rating.

Fuel properties for Btu/scf calculations are at 60F and 14.696 psia.

Caterpillar shall have no liability in law or equity, for damages, consequently or otherwise, arising from use of program and related material or any part thereof.

FUEL LIQUIDSFUEL LIQUIDSFUEL LIQUIDSFUEL LIQUIDSField gases, well head gases, and associated gases typically contain liquid water and heavy hydrocarbons entrained in the gas. To prevent detonation and severe damage to the engine, hydrocarbonliquids must not be allowed to enter the engine fuel system. To remove liquids, a liquid separator and coalescing filter are recommended, with an automatic drain and collection tank to preventcontamination of the ground in accordance with local codes and standards.

To avoid water condensation in the engine or fuel lines, limit the relative humidity of water in the fuel to 80% at the minimum fuel operating temperature.

QUO-14241-J6B9Prepared For: QUOTE:

EXTERRANKyle Poycker

Engine: G3516BHorsepower: 1380RPM: 1400Compression Ratio: 8.0Exhaust Flow Rate: 9126 CFMExhaust Temperature: 992 °FReference: DM8800-04Fuel: Natural GasAnnual Operating Hours: 8760


INFORMATION PROVIDED BY CATERPILLAR

g/bhp-hr Lb/Hr Tons/Year

POST CATALYST EMISSIONS

O2: 9.00 %

NOx: Unaffected by Oxidation Catalyst

g/bhp-hr Lb/Hr Tons/YearNOx: 0.50 1.52 6.66CO: 2.43 7.39 32.38THC: 4.77 14.51 63.56NMHC 0.72 2.19 9.59NMNEHC: 0.48 1.46 6.40HCHO: 0.44 1.34 5.86

CO: <2.00 <6.08 <26.65VOC: <0.70 <2.13 <9.33HCHO: <0.11 <0.32 <1.41

Catalyst HousingModel: ELS-3050-1416F-3CE0-242Manufacturer: EMIT Technologies, IncElement Size: Rectangle 24" x 15" x 3.5"Housing Type: 3 Element CapacityCatalyst Installation: Accessible HousingConstruction: 10 gauge Carbon SteelSample Ports: 6 (0.5" NPT)Inlet Connections: 14" Flat Face FlangeOutlet Connections: 16" Flat Face FlangeConfiguration: End In / Side OutSilencer: IntegratedSilencer Grade: CriticalInsertion Loss: 25-30 dBA

Catalyst ElementModel: RT-2415-ZCatalyst Type: Oxidation, Standard Precious Group MetalsSubstrate Type: BRAZEDManufacturer: EMIT Technologies, IncElement Quantity: 2Element Size: Rectangle 24" x 15" x 3.5"

CONTROL EQUIPMENT

The information in this quotation, and any files transmitted with it, is confidential and may be legally privileged. It is intended only for the use of individual(s) within the company named above. If you are the intended recipient, be aware that your use of any confidential or personal information may be restricted by state and federal privacy laws

www.emittechnologies.com

10497 Town & Country Way, Ste. 940Houston, TX 77024

Office: 307.673.0883 | Direct: [email protected]

EMIT Technologies, Inc. warrants that the goods supplied will be free from defects in workmanship by EMIT Technologies, Inc. for a period of two (2) years from date of shipment. EMIT Technologies, Inc. will not be responsible for any defects which result from improper use, neglect, failure to properly maintain or which are attributable to defects, errors or omissions in any drawings, specifications, plans or descriptions, whether written or oral, supplied to EMIT Technologies, Inc. by Buyer.

Catalyst performance using an EMIT Air/Fuel ratio controller is dependent upon properly defined set-points, variable with engine and fuel gas composition. Air/fuel ratio controller performance is guaranteed, but not limited, to fuel gas with a HHV content of 1400 BTU/SCF.

Catalyst performance will be guaranteed for a period of 1 year from installation, or 8760 operating hours, whichever comes first. The catalyst shall be operated with an automatic air/fuel ratio controller. The performance guarantee shall not cover the effects of excessive ash masking due to operation at low load, improper engine maintenance, or inappropriate lubrication oil. The performance guarantee shall not cover the effects of continuous engine misfires (cylinder or ignition) exposing the catalyst to excessive exothermic reaction temperatures. In most cases, excluding thermal deactivation, catalyst performance is redeemable by means of proper washing (refer to EMIT Catalyst/Silencer Housing Manual for element wash information, or contact a local EMIT Sales representative).

The exhaust temperature operating range at the converter inlet is a minimum of 600°F for oxidation catalyst and 750 ˚F for NSCR catalyst, and a maximum of 1250°F.

If a properly functioning, high temperature shut down switch is not installed, thermal deactivation of catalyst at sustained temperatures above 1250˚F is not covered. If excessive exposure to over oxygenation of NSCR catalyst occurs due to improperly functioning or non-existent Air/Fuel ratio control, then deactivation of catalyst is not warranted.

The catalyst conversion efficiencies (% reduction) will be guaranteed for engine loads of 50 to 100 percent. Standard Oxidation Catalyst conversion efficiencies (% reduction) will be guaranteed for fuel gas containing less than 1.5% mole fraction of non-methane, non-ethane hydrocarbons. Applications where fuel gas exceeds this level will require a Premium Oxidation Catalyst to maintain guaranteed VOC conversion efficiencies.

Engine lubrication oil shall contain less than 0.5 wt% Sulfated Ash with a maximum allowable specific oil consumption of 0.7 g/bhp-hr. The catalyst shall be limited to a maximum ash loading of 0.022 lb/ft3. Phosphorous and zinc additives are limited to 0.03 wt%. New or Reconstructed engines must operate for a minimum of 50 hours prior to catalyst installation, otherwise the warranty is void.

The catalyst must not be exposed to the following know poisoning agents, including: antimony, arsenic, chromium, copper, iron, lead, lithium, magnesium, mercury, nickel, phosphorous, potassium, silicon, sodium, sulfur, tin, and zinc. Total poison concentrations in the fuel gas must be limited to 0.25 ppm or less for catalyst to function properly.

Shipment - Promised shipping dates are approximate lead times from the point of manufacture and are not guaranteed. EMIT Technologies, Inc. will not be liable for any loss, damage or delay in manufacture or delivery resulting from any cause beyond its control including, but not limited to a period equal to the time lost by reason of that delay. All products will be crated as per best practice to prevent any damage during shipment. Unless otherwise specified, Buyer will pay for any special packing and shipping requirements. Acceptance of goods by common carrier constitutes delivery to Buyer. EMIT Technologies, Inc. shall not be responsible for goods damaged or lost in transit.

Terms: Credit is extended to purchaser for net 30 time period. If payment is not received in the net 30 timeframe, interest on the unpaid balance will accrue at a rate of 1.5% per month from the invoice date.

Order Cancellation Terms: Upon cancellation of an order once submittal of a Purchase Order has occurred, the customer will pay a 25% restocking fee for Catalyst Housings, Catalyst Elements, and Air/Fuel Ratio Controllers; 50% restocking fee for Cooler Top Solutions, Exhaust System Accessories, and other Custom Built Products; 100% of all associated shipping costs incurred by EMIT; 100% of all project expenses incurred by EMIT for Field Services.

WARRANTY





G3516B GAS ENGINE SITE SPECIFIC TECHNICAL DATA

GAS COMPRESSION APPLICATION Encana-PTS IP (less H2S)

PREPARED BY: Brandon Immenhauser, CDM Resource ManagementData generated by Gas Engine Rating Pro Version 5.01.01Ref. Data Set DM8800-07-001, Printed 12Mar2015 Page 1 of 4

ENGINE SPEED (rpm): 1400 RATING STRATEGY: STANDARDCOMPRESSION RATIO: 8:1 RATING LEVEL: CONTINUOUSAFTERCOOLER TYPE: SCAC FUEL SYSTEM: CAT WIDE RANGEAFTERCOOLER - STAGE 2 INLET (°F): 130 WITH AIR FUEL RATIO CONTROLAFTERCOOLER - STAGE 1 INLET (°F): 201 SITE CONDITIONS:JACKET WATER OUTLET (°F): 210 FUEL: Gas AnalysisASPIRATION: TA FUEL PRESSURE RANGE(psig): 7.0-40.0COOLING SYSTEM: JW+OC+1AC, 2AC FUEL METHANE NUMBER: 54.4CONTROL SYSTEM: ADEM3 FUEL LHV (Btu/scf): 1154EXHAUST MANIFOLD: DRY ALTITUDE(ft): 500COMBUSTION: LOW EMISSION MAXIMUM INLET AIR TEMPERATURE(°F): 110NOx EMISSION LEVEL (g/bhp-hr NOx): 0.5 STANDARD RATED POWER: 1380 bhp@1400rpmSET POINT TIMING: 28

MAXIMUM

RATING

SITE RATING AT MAXIMUM

INLET AIR TEMPERATURE

RATING NOTES LOAD 100% 100% 75% 50%

ENGINE POWER (WITHOUT FAN) (1) bhp 1380 1380 1035 690


ENGINE DATA

FUEL CONSUMPTION (LHV) (2) Btu/bhp-hr 7425 7425 7952 8541


AIR FLOW (@inlet air temp, 14.7 psia) (WET) (3)(4) ft3/min 3336 3339 2620 1831

AIR FLOW (WET) (3)(4) lb/hr 13949 13949 10943 7650

FUEL FLOW (60ºF, 14.7 psia) scfm 148 148 119 85



EXHAUST GAS FLOW (@engine outlet temp, 14.5psia)

(WET) (7)(4) ft3/min 9243 9243 7228 5128


EMISSIONS DATA - ENGINE OUT

NOx (as NO2) (8)(9) g/bhp-hr 0.50 0.50 0.50 0.50

CO (8)(9) g/bhp-hr 2.97 2.97 3.18 3.12





CO2 (8)(9) g/bhp-hr 512 512 547 594


HEAT REJECTION

HEAT REJ. TO JACKET WATER (JW) (12) Btu/min 22158 22158 20639 19267





COOLING SYSTEM SIZING CRITERIA

TOTAL JACKET WATER CIRCUIT (JW+OC+1AC) (13)(14) Btu/min 42898



CONDITIONS AND DEFINITIONSEngine rating obtained and presented in accordance with ISO 3046/1, adjusted for fuel, site altitude and site inlet air temperature. 100% rating at maximum inlet air temperature is the maximum enginecapability for the specified fuel at site altitude and maximum site inlet air temperature. Maximum rating is the maximum capability at the specified aftercooler inlet temperature for the specified fuel atsite altitude and reduced inlet air temperature. Lowest load point is the lowest continuous duty operating load allowed. No overload permitted at rating shown.












9. Emission values are based on engine operating at steady state conditions. Fuel methane number cannot vary more than ± 3. Values listed are higher than nominallevels to allow for instrumentation, measurement, and engine-to-engine variations. They indicate "Not to Exceed" values. THC, NMHC, and NMNEHC do not includealdehydes. An oxidation catalyst may be required to meet Federal, State or local CO or HC requirements.



12. Heat rejection values are nominal. Tolerances, based on treated water, are ± 10% for jacket water circuit, ± 50% for radiation, ± 20% for lube oil circuit, and ± 5% foraftercooler circuit.

13. Aftercooler heat rejection includes an aftercooler heat rejection factor for the site elevation and inlet air temperature specified. Aftercooler heat rejection values atpart load are for reference only. Do not use part load data for heat exchanger sizing.



Constituent Abbrev Mole % Norm

Water Vapor H2O 0.0000 0.0000

Methane CH4 75.9103 75.9681

Ethane C2H6 13.4259 13.4361

Propane C3H8 5.4855 5.4897

Isobutane iso-C4H1O 0.9899 0.9907

Norbutane nor-C4H1O 1.4519 1.4530

Isopentane iso-C5H12 0.4030 0.4033

Norpentane nor-C5H12 0.3120 0.3122

Hexane C6H14 0.2160 0.2162

Heptane C7H16 0.1010 0.1011

Nitrogen N2 0.0850 0.0851

Carbon Dioxide CO2 1.5429 1.5441

Hydrogen Sulfide H2S 0.0005 0.0005

Carbon Monoxide CO 0.0000 0.0000

Hydrogen H2 0.0000 0.0000

Oxygen O2 0.0000 0.0000

Helium HE 0.0000 0.0000

Neopentane neo-C5H12 0.0000 0.0000

Octane C8H18 0.0000 0.0000

Nonane C9H20 0.0000 0.0000

Ethylene C2H4 0.0000 0.0000

Propylene C3H6 0.0000 0.0000

TOTAL (Volume %) 99.9239 100.0001

Fuel Makeup: Gas Analysis























QUO-17197-M6F4

December 04, 2015

Prepared For: QUOTE:

Expires:CDM RESOURCE MANAGEMENT, LTDTony Wallace

Engine: G3516BHorsepower: 1380RPM: 1400Compression Ratio: 8.0Exhaust Flow Rate: 9243 CFMExhaust Temperature: 1011 °FReference: DM8800-07-001Fuel: Natural GasAnnual Operating Hours: 8760



g/bhp-hr


O2: 9.00 %



CO: <2.00VOC: <0.70HCHO: <0.05

Catalyst ElementModel: RT-2415-HCatalyst Type: Oxidation, Premium Precious Group MetalsSubstrate Type: BRAZEDManufacturer: EMIT Technologies, IncElement Quantity: 3Element Size: Rectangle 24" x 15" x 3.5"Estimated Lead Time: 7-10 Business Days to Ship

CONTROL EQUIPMENT



2585 Heartland Dr.Sheridan, WY 82801

Office: | Direct: +1 (307) [email protected]












WARRANTY



2585 Heartland Dr.Sheridan, WY 82801

Office: | Direct: +1 (307) [email protected]

Apr 07, 2015

Re: Engine Pedigree for Exterran Compressor Unit 805808, Engine Serial Number JEF02817





Spark Ignition Internal Combustion Engines, Subpart JJJJ. This information is current as of Apr 07, 2015.

Exterran




Main 281.836.7000

Fax 281.836.8161

www.exterran.com

Brendan Haigney

EXTERRAN


Engine Make: CATERPILLAR

Engine Model: G3516B

Engine Serial Number: JEF02817

Engine Type: 4 Stroke LB






Engine Manufacture Date: Jun 02, 2014

Last Overhaul Date:


NSPS Startup Date:

Customer: REV LNG LLC

Business Unit: N/A


Customer Lease Name: TROUT RUN LNG FACILITY #2











ENGINE SPEED (rpm): 1400 FUEL SYSTEM: CAT WIDE RANGECOMPRESSION RATIO: 8:1 WITH AIR FUEL RATIO CONTROLAFTERCOOLER - STAGE 2 INLET (°F): 130 SITE CONDITIONS:AFTERCOOLER - STAGE 1 INLET (°F): 201 FUEL: Nat GasJACKET WATER OUTLET (°F): 210 FUEL PRESSURE RANGE(psig): 7.0-50.0ASPIRATION: TA FUEL METHANE NUMBER: 84.8COOLING SYSTEM: JW+OC+1AC, 2AC FUEL LHV (Btu/scf): 905IGNITION SYSTEM: ADEM3 ALTITUDE(ft): 500EXHAUST MANIFOLD: DRY MAXIMUM INLET AIR TEMPERATURE(°F): 77COMBUSTION: Ultra Lean Burn STANDARD RATED POWER: 1380 bhp@1400rpmNOx EMISSION LEVEL (g/bhp-hr NOx): 0.5SET POINT TIMING: 30

MAXIMUMRATING

SITE RATING AT MAXIMUMINLET AIR TEMPERATURE

RATING NOTES LOAD 100% 100% 75% 50% ENGINE POWER (WITHOUT FAN) (1) bhp 1380 1380 1035 690


ENGINE DATA FUEL CONSUMPTION (LHV) (2) Btu/bhp-hr 7443 7443 7972 8562


AIR FLOW (77°F, 14.7 psia) (WET) (3)(4) scfm 3126 3126 2452 1715

AIR FLOW (WET) (3)(4) lb/hr 13862 13862 10874 7602



EXHAUST GAS FLOW (@engine outlet temp, 14.5 psia) (WET) (7)(4) ft3/min 9126 9126 7138 5065


EMISSIONS DATA - ENGINE OUT NOx (as NO2) (8)(9) g/bhp-hr 0.50 0.50 0.50 0.50

CO (8)(9) g/bhp-hr 2.43 2.43 2.61 2.56





CO2 (8)(9) g/bhp-hr 474 474 506 549


HEAT REJECTION HEAT REJ. TO JACKET WATER (JW) (12) Btu/min 23412 23412 21533 19930





COOLING SYSTEM SIZING CRITERIA TOTAL JACKET WATER CIRCUIT (JW+OC+1AC) (13)(14) Btu/min 41672



CONDITIONS AND DEFINITIONSEngine rating obtained and presented in accordance with ISO 3046/1, adjusted for fuel, site altitude and site inlet air temperature. 100% rating at maximum inlet air temperature is the maximum enginecapability for the specified fuel at site altitude and maximum site inlet air temperature. Max. rating is the maximum capability for the specified fuel at site altitude and reduced inlet air temperature.Lowest load point is the lowest continuous duty operating load allowed. No overload permitted at rating shown.



Engine Power vs. Inlet Air TemperatureData represents temperature sweep at 500 ft and 1400 rpm





Air Temperature, °FAir Temperature, °FAir Temperature, °FAir Temperature, °F30303030 40404040 50505050 60606060 70707070 80808080 90909090 100100100100 110110110110 120120120120 130130130130

EE EEnn nn

gg ggii iinn nn

ee eePP PP

oo ooww ww

ee eerr rr,, ,,

bb bbhh hh

pp pp

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

Engine Power vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF






EE EEnn nn

gg ggii iinn nn

ee eePP PP

oo ooww ww

ee eerr rr,, ,,

bb bbhh hh

pp pp

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

0000

200200200200

400400400400

600600600600

800800800800

1000100010001000

1200120012001200

1400140014001400

Engine Torque vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF

Max Continuous Torque vs.Speed Capabilityfor Site Conditions





EE EEnn nn

gg ggii iinn nn

ee eeTT TT

oo oorr rrqq qq

uu uuee ee

,, ,,ff fftt tt

-- --ll llbb bb

0000

500500500500

1000100010001000

1500150015001500

2000200020002000

2500250025002500

3000300030003000

3500350035003500

4000400040004000

4500450045004500

5000500050005000

5500550055005500

0000

500500500500

1000100010001000

1500150015001500

2000200020002000

2500250025002500

3000300030003000

3500350035003500

4000400040004000

4500450045004500

5000500050005000

5500550055005500












9. Emission values are based on engine operating at steady state conditions. Fuel methane number cannot vary more than ± 3. Values listed are higher than nominal levels to allowfor instrumentation, measurement, and engine-to-engine variations. They indicate "Not to Exceed" values. THC, NMHC, and NMNEHC do not include aldehydes. An oxidationcatalyst may be required to meet Federal, State or local CO or HC requirements.



12. Heat rejection values are nominal. Tolerances, based on treated water, are ± 10% for jacket water circuit, ± 50% for radiation, ± 20% for lube oil circuit, and ± 5% for aftercoolercircuit.

13. Aftercooler heat rejection includes an aftercooler heat rejection factor for the site elevation and inlet air temperature specified. Aftercooler heat rejection values at part load arefor reference only. Do not use part load data for heat exchanger sizing.



Constituent Abbrev Mole % NormWater Vapor H2O 0.0000 0.0000Methane CH4 92.2700 92.2700Ethane C2H6 2.5000 2.5000Propane C3H8 0.5000 0.5000Isobutane iso-C4H1O 0.0000 0.0000Norbutane nor-C4H1O 0.2000 0.2000Isopentane iso-C5H12 0.0000 0.0000Norpentane nor-C5H12 0.1000 0.1000Hexane C6H14 0.0500 0.0500Heptane C7H16 0.0000 0.0000Nitrogen N2 3.4800 3.4800Carbon Dioxide CO2 0.9000 0.9000Hydrogen Sulfide H2S 0.0000 0.0000Carbon Monoxide CO 0.0000 0.0000Hydrogen H2 0.0000 0.0000Oxygen O2 0.0000 0.0000Helium HE 0.0000 0.0000Neopentane neo-C5H12 0.0000 0.0000Octane C8H18 0.0000 0.0000Nonane C9H20 0.0000 0.0000Ethylene C2H4 0.0000 0.0000Propylene C3H6 0.0000 0.0000TOTAL (Volume %) 100.0000 100.0000

Fuel Makeup: Nat Gas






















QUO-14241-J6B9Prepared For: QUOTE:


Engine: G3516BHorsepower: 1380RPM: 1400Compression Ratio: 8.0Exhaust Flow Rate: 9126 CFMExhaust Temperature: 992 °FReference: DM8800-04Fuel: Natural GasAnnual Operating Hours: 8760





O2: 9.00 %



CO: <2.00 <6.08 <26.65VOC: <0.70 <2.13 <9.33HCHO: <0.11 <0.32 <1.41


Catalyst ElementModel: RT-2415-ZCatalyst Type: Oxidation, Standard Precious Group MetalsSubstrate Type: BRAZEDManufacturer: EMIT Technologies, IncElement Quantity: 2Element Size: Rectangle 24" x 15" x 3.5"

CONTROL EQUIPMENT
















WARRANTY





Jun 02, 2015

Re: Engine Pedigree for Exterran Compressor Unit 806383, Engine Serial Number 5283703759





Spark Ignition Internal Combustion Engines, Subpart JJJJ. This information is current as of Jun 02, 2015.

Exterran




Main 281.836.7000

Fax 281.836.8161

www.exterran.com

Brendan Haigney

EXTERRAN


Engine Make: WAUKESHA

Engine Model: L7044GSI

Engine Serial Number: 5283703759

Engine Type: 4 Stroke RB






Engine Manufacture Date: May 20, 2014

Last Overhaul Date:


NSPS Startup Date:

Customer: N/A

Business Unit: N/A


Customer Lease Name: N/A









L7044GSIVHP® Series Four® Gas Engine

1120 - 1680 BHP (835 - 1253 kWb)

Cylinders: V12

Piston Displacement: 7040 cu. in. (115 L)

Bore & Stroke: 9.375” x 8.5” (238 x 216 mm)

Compression Ratio: 8:1

Jacket Water System Capacity: 100 gal. (379 L)

Lube Oil Capacity: 190 gal. (719 L)

Starting System: 125 - 150 psi air/gas 24V electric

Dry Weight: 21,000 lb. (9,525 kg)

Specifi cations

Standard Equipment

AIR CLEANER – Two, 3" dry type fi lter with hinged rain shield and service

indicator.

AIR FUEL RATIO CONTROL (AFR) – Integrated ESM® - AFR catalyst rich-burn

control, main fuel gas regulator actuators, exhaust O2 sensor(s), and post

turbocharger exhaust thermocouple. Factory mounted and tested. AFR maintains

emissions through load and speed changes. The ESM AFR meets Canadian

Standards Association Class 1, Division 2, Group A, B, C & D (Canada & US)

hazardous location requirements. Note: For dual fuel applications, ESM AFR

system will control the primary fuel source only.

BARRING DEVICE – Manual.

BATTERY BOX – Ship loose battery box designed to accommodate two series 31

12 VDC batteries. Includes power disconnect switch and 20 foot (6.1 m) cable for

connection to ESM Power Distribution Box.

BEARINGS – Heavy duty, replaceable, precision type.

BREATHER – Self regulating, closed system.

CONNECTING RODS – Drop forged steel, rifl e drilled.

CONTROL SYSTEM – Waukesha Engine System Manager (ESM) integrates

spark timing control, speed governing, detonation detection, start-stop control,

diagnostic tools, fault logging and engine safeties. Engine Control Unit (ECU) is

central brain of the control system and main customer interface. Interface with

ESM is through 25 foot (7.6 m) harness to local panel, through MODBUS RTU

slave connection RS-485 multidrop hardware, and through the Electronic Service

Program (ESP). Customer connections are only required to the local panel, fuel

valve, and 24V DC power supply. Compatible with Woodward load sharing module.

ESM meets Canadian Standards Association Class I, Division 2, Group A, B, C & D

(Canada & US) hazardous location requirements.

CRANKCASE – Integral crankcase and cylinder frame. Main bearing caps drilled

and tapped for temperature sensors. Does not include sensors.

CRANKSHAFT – Forged steel, seven main bearings, counterweighted and

dynamically balanced.

CYLINDERS – Removable wet bainitic cast iron type cylinder liners, chrome

plated on outer diameter.

CYLINDER HEADS – Twelve interchangeable. Four valves per cylinder, with water

cooled exhaust valve seats. Roller valve lifters and hydraulic push rods. Flange

mounted ignition coils.

ELECTRONIC SERVICE PROGRAM (ESP) – Microsoft® Windows-based

program provided on CD-ROM for programming and interface to ESM. Includes

E-Help for troubleshooting any ESM faults. Serial harness is provided for

connection of a customer supplied laptop to the ECU RS-232 port.

ENGINE MONITORING DEVICES – Factory mounted and wired sensors for

lube oil pressure and temperature; intake manifold temperature and pressure;

overspeed; and jacket water temperature; all accessible through ESM®. ESM

continually monitors combustion performance through accelerometers to provide

detonation protection. Dual magnetic pick-ups are used for accurate engine speed

monitoring. ESM provides predictive spark plug diagnostics as well as advanced

diagnostics of engine and all ESM sensors and logs any faults into non-volatile

fl ash memory. Sensors meet Canadian Standards Association Class 1, Division 2,

Group A, B, C, & D (Canada & US) hazardous location requirements.

ENGINE ROTATION – Counterclockwise when facing fl ywheel.

EXHAUST OUTLET – Single vertical at rear. Flexible stainless steel connection

with 8" (203 mm) pipe fl ange.

FLYWHEEL – Approx. WR2 = 155000 lb-in2; with ring gear (208 teeth), machined

to accept two drive adapters: 31.88" (810 mm) pilot bore, 30.25" (768 mm) bolt

circle, (12) 0.75" - 10 tapped holes; or 28.88" (734 mm) pilot bore, 27.25" (692

mm) bolt circle, (12) 0.625"-11 tapped holes and (12) 0.75"-10 tapped holes.

FLYWHEEL HOUSING – No. 00 SAE.

FUEL SYSTEM – Single 3" ANSI fl ange fuel inlet connection. Two natural gas,

4" (102 mm) updraft carburetors and two mounted Fisher 99, 2" (51 mm) gas

regulators, 30-60 psi (207-414 kPa) fuel inlet pressure required. 10 foot (3 m)

harness provided for ESM control of customer supplied fuel shutoff valve

GOVERNOR – Electric throttle actuator controlled by ESM with throttle position

feedback. Governor tuning is performed using ESP. ESM includes option of a load-

coming feature to improve engine response to step loads.

IGNITION SYSTEM – Ignition Power Module (IPM) controlled by ESM, with

spark timing optimized for any speed-load condition. Dual voltage energy levels

automatically controlled by ESM to maximize spark plug life. Shielded ignition

components meet Canadian Standard Association Class 1, Division 2, Group A, B,

C & D (Canada & US) hazardous location requirements.

INTERCOOLER – Air-to-water.

LEVELING BOLTS

LIFTING EYES – Requires 9.5 ton Working Load Limit (W.L.L.) anchor shackles.

LUBRICATION – Full pressure, gear type pump. Engine mounted full fl ow lube oil

micro-fi berglass fi lters with mounted differential pressure gauge. MICROSPIN®

bypass fi lter, engine mounted. Air/gas motor driven prelube pump, requires fi nal

piping.

MANIFOLDS – Exhaust, (2) water cooled.

OIL COOLER – Shell and tube type, with thermostatic temperature controller and

pressure regulating valve. Factory mounted.

OIL PAN – Deep sump type. 190 gallon (719 L) capacity, including fi lter and

cooler.

PAINT – Oilfi eld orange primer.

PISTONS – Aluminum with fl oating pin. Oil cooled. 8:1 compression ratio.

SHIPPING SKID – For domestic truck or rail.

TURBOCHARGERS – (2) with water-cooled bearing housing and adjustable

wastegates.

VIBRATION DAMPER – Viscous type.

WATER CIRCULATING SYSTEM, AUXILIARY CIRCUIT – Belt driven water

circulating high capacity pump for intercooler and lube oil cooler. See S6543-36

performance curve for use with standard 10" diameter crankshaft pulley.

WATER CIRCULATING SYSTEM, ENGINE JACKET – Belt driven water

circulating pump. Cluster type thermostatic temperature regulating valve, full fl ow

bypass type with 165° - 170° F (74° - 77° C) start to open thermostats. Flange

connections and mating fl anges for (2) 4" (102 mm) inlets and (1) 5" (127 mm)

outlet.

Image may not be an accurate representation of this model

© 2010 Dresser, Inc. All rights reserved. Waukesha, VHP, ESM, Microspin, and WKI are

trademarks/registered trademarks of Dresser, Inc., Dresser Waukesha

Bulletin 7045 1210

POWER RATINGS: L7044GSI VHP Series Four Gas Engines

www.dresser.com/waukesha

Dresser, Inc.

Dresser Waukesha

1101 West St. Paul Avenue

Waukesha, WI 53188-4999

T. 262 547 3311

F. 262 549 2795

85"(2159 mm)

97.83"(2485 mm)

147"(3734 mm)

Model C.R. Bore & Stroke in. (mm)

Displ. cu.

in. (litres)

Brake Horsepower (kWb Output)

130°F (54°C) I.C. Water Temperature

1200 RPM 1000 RPM 900 RPM 800 RPM

C I C I C I C I

L7044GSI 8:1 9.375’’ x 8.5’’ (238 x 216) 7040 (115) 1680 1680 1400 1400 1260 1260 1120 1120

(1253) (1253) (1044) (1044) (940) (940) (835) (835)

Consult your local Waukesha representative for system application assistance. The manufacturer reserves the right to change or modify without notice, the design or

equipment specifi cations as herein set forth without incurring any obligation either with respect to equipment previously sold or in the process of construction except

where otherwise specifi cally guaranteed by the manufacturer.

Typical heat data is shown, however no guarantee is expressed or implied. Consult your Dresser Waukesha Application Engineering Department for system application assistance.

All natural gas engine ratings are based on a fuel of 900 Btu/ft3 (35.3 MJ/nm3) SLHV, with a 91 WKI®. For conditions or fuels other than standard, consult the Dresser Waukesha Application Engineering Department.

Data based on standard conditions of 77°F (25°C) ambient temperature, 29.53 inches Hg (100kPa) barometric pressure, 30% relative humidity (0.3 inches HG / 1 kPa water vapor pressure).

Fuel consumption based on ISO3046/1-1995 with a tolerance of +5% for commercial quality natural gas having a 900 BTU/ft3 (35.3 MJ/nm3) SLHV.Heat data based on fuel consumption +2%.Heat rejection based on cooling exhaust temperature to 77°F (25°C).Rating Standard: All models - Ratings are based on ISO 3046/1-1986 with mechanical effi ciency of 90% and Tcra (clause 10.1) as specifi ed above limited to

± 10° F (5° C). Ratings are also valid for SAE J1349, BS5514, DIN6271 and AP17B-11C standard atmospheric conditions.C = ISO Standard Power/Continuous Power Rating: The highest load and speed which can be applied 24 hours per day, seven days per week, 365 days

per year except for normal maintenance. It is permissible to operate the engine at up to 10% overload, or a maximum load indicated by the intermittent rating, whichever is lower, for two hours in every 24 hour period.

I = Intermittent Service Rating: The highest load and speed that can be applied in variable speed mechanical system application only. Operation at this rating is limited to a maximum of 3500 hours per year.

1200 rpm 1000 rpm

Power bhp (kWb) 1680 (1253) 1400 (1044)BSFC (LHV) Btu/bhp-hr (kJ/kWh) 7744 (10955) 7559 (10693)Fuel Consumption Btu/hr x 1000 (kW) 13010 (3813) 10583 (3101)

Em

issio

ns NOx g/bhp-hr (mg/nm3 @ 5% O2) 13.30 (4922) 12.90 (4782)

CO g/bhp-hr (mg/nm3 @ 5% O2) 11.20 (4140) 9.40 (3477)THC g/bhp-hr (mg/nm3 @ 5% O2) 2.40 (873) 2.30 (844)NMHC g/bhp-hr (mg/nm3 @ 5% O2) 0.35 (131) 0.34 (127)

He

at

Ba

lan

ce

Heat to Jacket Water Btu/hr x 1000 (kW) 3849 (1128) 3227 (946)Heat to Lube Oil Btu/hr x 1000 (kW) 567 (166) 462 (135)Heat to Intercooler Btu/hr x 1000 (kW) 179 (53) 122 (36)Heat to Radiation Btu/hr x 1000 (kW) 724 (212) 642 (188)Total Exhaust Heat Btu/hr x 1000 (kW) 3900 (1143) 2962 (868)

Inta

ke

/

Exh

au

st

Syste

m Induction Air Flow scfm (Nm3/hr) 2424 (3651) 1972 (2970)Exhaust Flow lb/hr (kg/hr) 11273 (5113) 9171 (4160)Exhaust Temperature °F (°C) 1179 (637) 1112 (600)

QUO-14377-R8W6Prepared For: QUOTE:


Engine: L7044GSIHorsepower: 1680RPM: 1200Compression Ratio: 8.0Exhaust Flow Rate: 8162 CFMExhaust Temperature: 1179 °FReference: N/AFuel: Natural GasAnnual Operating Hours: 8760


INFORMATION PROVIDED BY WAUKESHA



O2: 0.30 %


NOx: <1.00 <3.70 <16.22CO: <2.00 <7.41 <32.45VOC: <0.70 <2.59 <11.36HCHO: <0.01 <0.04 <0.19


Catalyst ElementModel: RT-2415-TCatalyst Type: NSCR, Standard Precious Group MetalsSubstrate Type: BRAZEDManufacturer: EMIT Technologies, IncElement Quantity: 3Element Size: Rectangle 24" x 15" x 3.5"

CONTROL EQUIPMENT
















WARRANTY





Engine Performance DataCummins Inc

Columbus, Indiana 47202-3005

http://www.cummins.com

Industrial

G855FR10523

Configuration

D251006CX02

188 BHP (140 kW) @ 1800 RPM548 lb-ft (743 N-m) @ 1800 RPM

CPL Code

8749Revision

15-Feb-2005

Compression Ratio: 10:1 Displacement: 855 in3 (14.0 L)Fuel System: Catalyst or Standard, Dry Processed Gas and Field Gas Aspiration: Naturally AspiratedEmission Certification: Non-certified

All data is based on the engine operating with fuel system, water pump, and 8 in H2O (1.991 kPa) inlet air restriction with 5 in (127 mm) inner diameter, and with 1.1 in Hg (4 kPa) exhaust restriction with 4 in (102 mm) inner diameter; not included are alternator, fan, optional equipment and driven components. Coolant flows and heat rejection data based on coolants as 50% ethylene glycol/50% water. All data is subject to change without notice.

Rating Type: Continuous/WMR

Torque OutputRPM lb-ft N-m1,000 548 743

1,100 548 743

1,200 548 743

1,300 548 743

1,400 548 743

1,500 548 743

1,600 548 743

1,700 548 743

1,800 548 743

Power OutputRPM hp kW1,000 104 78

1,100 115 86

1,200 125 93

1,300 136 101

1,400 146 109

1,500 157 117

1,600 167 125

1,700 177 132

1,800 188 140

Fuel Consumption @ 1,800 RPMhp kW % Load BTU/hp-hr MJ/kW-hr188 140 100 8,605 12.17

169 126 90 8,978 12.7

150 112 80 9,483 13.42

132 98 70 10,525 14.89

113 84 60 11,674 16.52

94 70 50 12,720 18

75 56 40 13,906 19.67

56 42 30 15,319 21.67

38 28 20 18,819 26.62

19 14 10 31,950 45.2

Data represents gross engine capabilities obtained and corrected in accordance with SAE J1995 and ISO 3046 conditions of 29.61 in Hg (100 kPa) barometric pressure [500 ft (152 m) altitude], 77 °F (25 °C) inlet air temperature and 0.30 in Hg (1 kPa) water vapor pressure using dry processed natural gas fuel with 930 BTU per standard cubic foot lower heating value. Deration may be required due to altitude, temperature and type of fuel. Consult Cummins Customer Engineering for operation above this altitude.

STATUS FOR CURVES AND DATA: Limited-(measured data) CHIEF ENGINEER: TOLERANCE: Within +/- 5 % Alfred S Weber

Cummins Confidential

FR10523 (Continued) Page: 2

Intake Air SystemMaximum allowable air temperature rise over ambient at Intake Manifold

(Naturally Aspirated Engines) or Turbo Compressor inlet (Turbo-charged Engines): (This parameter impacts emissions, LAT and/or altitude capability) 15 8.3delta deg F delta deg C

Exhaust SystemMaximum exhaust back pressure: 2 6.8in-Hg kPa

Recommended exhaust piping size (inner diameter): 4 101.6in mm

Lubrication SystemNominal operating oil pressure

@ minimum low idle 15 103psi kPa

@ maximum rated speed 60 414psi kPa

Minimum engine oil pressure for engine protection devices


Fuel SystemMaximum fuel inlet pressure: 20" H2O 5 kPa

Performance DataEngine low idle speed: 900 RPM

Maximum low idle speed: 1,980 RPM

Minimum low idle speed: 850 RPM

Engine high idle speed 1,800 RPM

Governor break speed:

Maximum torque available at closed throttle low idle speed: 0 0lb-ft N-m

100% Load 75% Load 50% Load

Engine Speed 1,800 RPM 1,800 RPM 1,800 RPM

Output Power 188 140hp kW 141 105hp kW 94 70hp kW

Torque 549 744lb-ft N-m 411 557lb-ft N-m 274 371lb-ft N-m

Intake Manifold Pressure -1.5 - 4.6in-Hg kPa -4.2 -14in-Hg kPa -6.7 -22in-Hg kPa

Turbo Comp. Outlet Pressure

Turbo Comp. Outlet Temperature

Inlet Air Flow 260 123ft3/min L/s 224 106ft3/min L/s 180 85ft3/min L/s

Charge Air Flow

Exhaust Gas Flow 866 409ft3/min L/s 734 346ft3/min L/s 584 276ft3/min L/s

Exhaust Gas Temperature 1,196 647deg F deg C 1,154 623deg F deg C 1,115 602deg F deg C

Heat Rejection to Coolant 8,154 143.38BTU/min kW 7,412 130.33BTU/min kW 6,684 117.53BTU/min kW

Heat Rejection to Ambient 2,762 48.57BTU/min kW 3,135 55.13BTU/min kW 3,219 56.6BTU/min kW

Heat Rejection to Exhaust 5,674 99.77BTU/min kW 4,681 82.31BTU/min kW 3,627 63.78BTU/min kW

Fuel Consumption 8,605 12.174BTU/hp-hr MJ/kW-hr 9,870 13.964BTU/hp-hr MJ/kW-hr 12,720 17.996BTU/hp-hr MJ/kW-hrAir Fuel Ratio (dry) 14.4 vol/vol 14.3 vol/vol 13.8 vol/volIgnition timing (BTDC) 24 24deg deg 24 24deg deg 24 24deg degTotal Hydrocarbons 1.9 g/hp-hr 2.5 g/hp-hr 3.4 g/hp-hrNonMethane HydrocarbonsNOx 5.9 7.91g/hp-hr g/kW-hr 2.9 3.89g/hp-hr g/kW-hr 1 1.34g/hp-hr g/kW-hrCO 26.7 35.81g/hp-hr g/kW-hr 52.4 70.27g/hp-hr g/kW-hr 63.5 85.15g/hp-hr g/kW-hrCO2 423 567g/hp-hr g/kW-hr 451 605g/hp-hr g/kW-hr 498 668g/hp-hr g/kW-hrO2 0.54 % 0.47 % 0.49 %

Cranking System (Cold Starting Capability)Unaided Cold Start:

Minimum cranking speed: 150 RPM

Minimum ambient temperature

Cranking torque at minimum unaided cold start temperature: 375 508lb-ft N-m

Cold starting aids available None


FR10523 (Continued) Page: 3

Aftercooler Heat Rejection - Heat Load on AftercoolerBTU/min (kW)

Ambient Temp deg F (deg C)

120 (49) 110 (43) 100 (38) 90 (32) 80 (27) 70 (21)

0 (0) (.0) (.0) (.0) (.0) (.0) (.0)

1000 (305) (.0) (.0) (.0) (.0) (.0) (.0)

2000 (610) (.0) (.0) (.0) (.0) (.0) (.0)

3000 (914) (.0) (.0) (.0) (.0) (.0) (.0)

4000 (1219) (.0) (.0) (.0) (.0) (.0) (.0)

Altitude 5000 (1524) (.0) (.0) (.0) (.0) (.0) (.0)

ft (m) 6000 (1829) (.0) (.0) (.0) (.0) (.0) (.0)

7000 (2134) (.0) (.0) (.0) (.0) (.0) (.0)

8000 (2438) (.0) (.0) (.0) (.0) (.0) (.0)

9000 (2743) (.0) (.0) (.0) (.0) (.0) (.0)

10000 (3048) (.0) (.0) (.0) (.0) (.0) (.0)

End of Report


EMIT Technologies, IncP.O. Box 6785Sheridan, WY 82801307-673-0883307-673-0886 [email protected]

PREPARED FOR:

Fluid Compressor Partners

A. INFORMATION PROVIDED BY CUMMINSEngine: G855C188DIM Sheet: FR10523Compression Ratio: 10.0:1Load: 100%RPM: 1800Horsepower: 188Fuel: Natural GasPiping size: 5"Annual Operating Hours: 8760Exhaust Flow: 866 CFMExhaust Temperature: 1196 °FAllowable Engine Backpressure: 27" WC

Emission DataNOx: 5.90 g/bhp-hrCO: 26.70 g/bhp-hrTHC: 1.90 g/bhp-hrOxygen: 0.54 %

B. POST CATALYST EMISSIONS TO BE ACHIEVED BY EMISSION CONTROL EQUIPMENTSINGLE ELEMENT PERFORMANCE

NOx: <1.0 g/bhp-hrCO: <1.0 g/bhp-hrVOC: <0.5 g/bhp-hr

1 of 3

C. CONTROL EQUIPMENTCATALYTIC CONVERTER/SILENCER UNITModel EAH-1125-0500-DCatalyst Type NSCR, Precious group metalsManufacturer EMIT Technologies, Inc.Element Size 11.25 x 3.5Catalyst Elements 1Housing Type Dual bedCatalyst Installation Accessible housingConstruction 10 ga SteelSample Ports 8Flange Size 5" Series 125 LW flat face flangesConfiguration Assume end in/ end outSilencer IntegratedSilencer Grade HospitalInsertion Loss 35-40 dBAAdditional Features Outlet gussets, drain plugsDelivery 1-2 weeks dependent on production load

AIR FUEL RATIO CONTROLLERPart Number ENG-S-150Manufacturer EMIT Technologies, Inc.Description

Digital Power Valve Size 1.50" NPTDelivery Stock

EDGE NG Additional EquipmentET 258 Type K thermocouple 20' lead Optional / 2 per EDGE NG

MODEL EDGE NG CSA certified AFR controller kit complete with: EDGE NG Air Fuel Ratio Controller enclosure featuring: graphical display of oxygen sensor voltage, position of the digital power valve and thermocouple temperatures. Multiscreen digital display of controller and engine parameters. Integrated high temperature shutdown, Modbus enabled, 4 wire heated O2 sensor, O2 weldment, 25' Wiring harnesses, Digital power valve, Operations manualSINGLE BANK ENGINE

2 of 3

E. WARRANTY

The exhaust temperature operating range at the converter inlet is 600°F minimum for oxidation catalyst and 750 oF for NSCR catalyst and 1250°F maximum.

Shipment - Promised shipping dates are approximate and are not guaranteed and are from the point of manufacture. EMIT Technologies,Inc. will not be liable for any loss, damage or delay in manufacture or delivery resulting from any cause beyond its control including, but not limited to a period equal to the time lost by reason of that delay. All products will be crated as per best practice to prevent any damage during shipment. Unless otherwise specified, Buyer will pay for any special packing and shipping requirements. Acceptance of goods by common carrier constitutes delivery to Buyer. EMIT Technologies,Inc. shall not be responsible for goods damaged or lost in transit.


If a high temperature shut down switch is not installed, thermal deactivation of catalyst at temperatures above 1300 oF is not covered.

The catalyst conversion efficiencies (% reduction) will be guaranteed for engine loads of 50 to 100 percent.

Engine lubrication oil shall contain less than 0.6% ash (by weight) with a maximum allowable specific oil consumption of 0.01 gal/bhp-hr. The maximum ash loading on the catalyst shall be limited to 350 g/m3. Phosphorous and zinc additives are limited to 0.03% (by weight).

The catalyst must not be exposed to the following know poisoning agents, including: iron, nickel, sodium, chromium, arsenic, zinc, lead, phosphorous, silicon, potassium, magnesium, copper, tin, and mercury. Total poison concentrations in the gas are limited to 0.3 ppm.

EMIT Technologies,Inc. warrants that the goods supplied will be free from defects in workmanship by EMIT Technologies, Inc. for a period of one (1) year from date of shipment. EMIT Technologies, Inc. will not be responsible for any defects which result from improper use, neglect, failure to properly maintain or which are attributable to defects, errors or omissions in any drawings, specifications, plans or descriptions, whether written or oral, supplied to EMIT Technologies, Inc. by Buyer.

Catalyst performance will be guaranteed for a period of 1 year from installation, or 8760 operating hours, whichever comes first. The catalyst shall be operated with an automatic air/fuel ratio controller. The performance guarantee shall not cover the effects of excessive ash masking due to operation at low load, improper engine maintenance, or inappropriate lubrication oil. The performance guarantee shall not cover the effects of continuous engine misfires (cylinder or ignition) exposing the catalyst to excessive exothermic reaction temperatures.

3 of 3

Applications Industrial, Agriculture Construction & Oilfield

Pumps – Irrigation, Industrial, Hydraulic, Sludge and Trash

Compressors – Natural Gas and Air

Generators – Prime Power, Standby and Co-Gen

Industrial Drives – Forklifts, Manlifts, Street Sweepers, Wood Chippers, Chillers and Fans Oil and Gas Production –

Gas Compressors, Pump Jacks, Vapor Recovery

Wind Machines

Numerous Re-Power & Custom Applications

Available Factory Installed Options

Natural Gas and LPG

Fuel Systems

Ignition Systems

Belt and Pulley Accessory

Drives

Starters and Alternators

Exhaust Headers and

Manifolds

Mufflers

SAE 3 Flywheel Housing and

Direct Drives

PTOs: Side Load and In-Line

Instrument Panel w/Gauges

and Safety Shutdowns

Governors: Electronic and

Mechanical

Engine Mounting Frames and

Enclosures

Three Way Catalyst

Three way catalyst and closed loop fuel

system for EPA/CARB emission certified engines

Designed for propane and natural gas fuel

Intake manifold is standard on the engine

Hydraulic roller lifter camshaft is optimized

for maximum performance

Composite front cover for noise reduction

Nodular iron crankshaft for increased

strength and durability

High Energy Ignition (HEI) distributor and

coil are standard

Main Office: 20 N. McCormick Oklahoma City, OK 73127 405-601-1000

515 North I-27 Lubbock, TX 79403 806-762-0455

4452 Canyon Dr. Amarillo, TX 79109 806-355-8228

Induction-hardened inlet valve seats and

sintered powder metal exhaust valve seat inserts for maximum durability

World-class engine sealing system uses

composite cylinder head gasket with steel cores, a one piece main crankshaft seal, a one piece oil pan seal and molded rocker cover seals

Positive inlet valve stem seals to control oil

consumption

Common GM Powertrain industrial engine rear

face for easy housing installation

GM Powertrain takes its expertise in designing outstanding Vortec truck and SUV engines and leverages it to make sophisticated yet extremely durable industrial engines.

VortecTM 5.7L 8 Cylinder - 350 Cubic Inches

POWERTRAIN

Industrial Eng ines

Features & Benefits

Buck’s Engines combines over 50 years of engine application experience with General Motors’ expertise in designing outstanding Vortec engines and utilizes this partnership to manufacture extremely durable industrial engines.

UE Powertrain Buck’s Engines

Specifications and Materials Type: 90

o 5.7L V8

Displacement: 350 cld (5736 cc)

Compression Ratio: 9.4:1

Valve Configuration: Overhead/Pushrod Actuated

Valve Lifters: Overhead/Pushrod Actuated

Bore x Stroke: 4.00 x 3.48 in (101.60 x 88.39 mm)

Main Bearing Caps:

2-Bolt

Balance Method: External

Intake Manifold: Four Barrel

Firing Order: 1-8-4-3-6-5-7-2

Oil Pan Capacity: 5 qt without oil filter

Fuel Type: Propane or Natural Gas

Engine Rotation: Clockwise (from the front)

Paint Protection: Component Painted

Shipping Weight: 434 lb (197 kg)

Block: Cast Iron

Cylinder Head: Cast Iron

Intake Manifold:

Cast Aluminum

Final Assembly: Oklahoma City, OK USA

Manufactured with US, North American and Global Sourced Content Information may vary by model and application. All specifications, options and product availability based upon the latest information

available at time of publication. To ensure our customers have access to the highest quality products available we reserve the right to make product improvements and changes anytime without prior notice. and Vortec™ trademarks are property of General Motors Corporation. ©2010 10/10

VortecTM 5.7L 8 Cylinder — 350 Cubic Inches

CONTINUOUS BRAKE HORSEPOWER

GEARHEAD 1x1 6x5 5x4

ENGINE RPM 1760 2112 2200

BHP 73 87 92

POWERTRAIN

Industrial Eng ines

Power and torque values provided by Buck’s Engines per SAE1349. Actual power levels may vary depending on fuel selection and quality, calibration, application, altitude and ambient air temperatures.

CONFIDENTIAL

MIRATECH Emissions Control Equipment Specification Summary

Proposal Number: TJ-12-2475

Engine DataNumber of Engines: 1

Application: Gas Compression

Engine Manufacturer: General Motors

Model Number: Vortec 5.7L NA

Power Output: 92 bhp

0.6 wt% sulfated ash or lessLubrication Oil:

Type of Fuel: Natural Gas

650 acfm (cfm)Exhaust Flow Rate:

Exhaust Temperature: 1,200°F

System DetailsHousing Model Number: VXCI-1005-3.5-HSG

Element Model Number: VX-RE-05XC

Number of Catalyst Layers: 1

Number of Spare Catalyst Layers: 1

System Pressure Loss: 4.0 inches of WC (Fresh)

Sound Attenuation: 28-32 dBA insertion loss

Exhaust Temperature Limits: 750 – 1250°F (catalyst inlet); 1350°F (catalyst outlet)

NSCR Housing & Catalyst DetailsModel Number: VXCI-1005-3.5-XC1

Material: Carbon Steel

Inlet Pipe Size & Connection: 3.5 inch FF Flange, 150# ANSI standard bolt pattern

Outlet Pipe Size & Connection: 3.5 inch FF Flange, 150# ANSI standard bolt pattern

Overall Length: 43 inches

Weight Without Catalyst: 98 lbs

Weight Including Catalyst: 104 lbs

Instrumentation Ports: 1 inlet/1 outlet (1/2" NPT)

Emission Requirements

Engine Outputs

(g/ bhp-hr)

Requested

Emissions Targets

Warranted

Converter Outputs

(g/ bhp-hr)Reduction (%)Exhaust Gases

1.00 1 g/bhp-hr 93%NOx 14.00

2.00 2 g/bhp-hr 82%CO 11.00

0.70 .7 g/bhp-hr 0%NMNEHC 0.40

Oxygen 0.5%

MIRATECH warrants the performance of the converter, as stated above, per the MIRATECH General Terms and Conditions of Sale.

MIRATECH Catalyzer (TM) 8/17/2012

Engine Performance DataCummins Inc

Columbus, Indiana 47202-3005

http://www.cummins.com

Industrial

G8.3FR 92224

Configuration

D551013CX03

118 BHP (88 kW) @ 1800 RPM345 lb-ft (468 N-m) @ 1800 RPM

CPL Code

2474

Revision

13-Sep-2006

Compression Ratio: 10.5:1 Displacement: 505 in3 (8.3 L)Fuel System: Dry Process Gas, Field Gas and Propane Aspiration: Naturally Aspirated (Dry Exhaust)Emission Certification: Non-certified, Catalyst

All data is based on the engine operating with fuel system, water pump, and 6 in H2O (152 mm H2O) inlet air restriction with 3 in (76 mm) inner diameter, and with 1 in Hg (25 mm Hg) exhaust restriction with 3 in (76 mm) inner diameter; not included are alternator, fan, optional equipment and driven components. Coolant flows and heat rejection data based on coolants as 50% ethylene glycol/50% water. All data is subject to change without notice.

Rating Type: Continuous/WMR

Torque OutputRPM lb-ft N-m1,000 345 468

1,100 345 468

1,200 345 468

1,300 345 468

1,400 345 468

1,500 345 468

1,600 345 468

1,700 345 468

1,800 345 468

Power OutputRPM hp kW1,000 66 49

1,100 72 54

1,200 79 59

1,300 85 63

1,400 92 69

1,500 99 74

1,600 105 78

1,700 112 84

1,800 118 88

Fuel Consumption @ hp kW % Load BTU/hp-hr MJ/kW-hr118 88 100 8,266 11.69

106 79 90 8,350 11.81

94 70 80 8,553 12.1

83 62 70 9,211 13.03

71 53 60 9,790 13.85

59 44 50 10,383 14.69

47 35 40 11,155 15.78

35 26 30 12,424 17.58

24 18 20 13,689 19.37

12 9 10 15,047 21.29

Data represents gross engine capabilities obtained and corrected in accordance with SAE J1995 and ISO 3046 conditions of 29.61 in Hg (100 kPa) barometric pressure [500 ft (152 m) altitude], 77 °F (25 °C) inlet air temperature and 0.30 in Hg (1 kPa) water vapor pressure using dry processed natural gas fuel with 935 BTU per standard cubic foot lower heating value (LHV). Deration may be required due to altitude, temperature and type of fuel. Consult Cummins Customer Engineering for operation above this altitude.

STATUS FOR CURVES AND DATA: Limited-(measured data) CHIEF ENGINEER: TOLERANCE: Within +/- 5 % Al Weber


FR 92224 (Continued) Page: 2

Intake Air SystemMaximum allowable air temperature rise over ambient at Intake Manifold

(Naturally Aspirated Engines) or Turbo Compressor inlet (Turbo-charged Engines): (This parameter impacts LAT and altitude capability) 15 8.3delta deg F delta deg C

Exhaust SystemMaximum exhaust back pressure: 2 50.7in-Hg mm Hg

Recommended exhaust piping size (inner diameter): 3 76.2in mm

Lubrication SystemNominal operating oil pressure


@ maximum rated speed 50 345psi kPa

Minimum engine oil pressure for engine protection devices


Fuel SystemMaximum fuel inlet pressure: 20 " H20 5 kPa

Performance DataEngine low idle speed: 900 RPM

Maximum low idle speed: 1,800 RPM

Minimum low idle speed: 800 RPM

Engine high idle speed 1,800 RPM

Governor break speed:

Maximum torque available at closed throttle low idle speed: 50 68lb-ft N-m

100% Load 75% Load 50% Load

Engine Speed 1,800 RPM 1,800 RPM 1,800 RPM

Output Power 118 88hp kW 89 66hp kW 59 44hp kW

Torque 344 466lb-ft N-m 260 353lb-ft N-m 172 233lb-ft N-m

Intake Manifold Pressure -1 -23in-Hg mm Hg -2 -61in-Hg mm Hg -4 -101in-Hg mm Hg

Turbo Comp. Outlet Pressure

Turbo Comp. Outlet Temperature

Inlet Air Flow 170 80ft3/min L/s 142 67ft3/min L/s 111 52ft3/min L/s

Charge Air Flow

Exhaust Gas Flow 604 285ft3/min L/s 501 236ft3/min L/s 383 181ft3/min L/s

Exhaust Gas Temperature 1,374 746deg F deg C

Heat Rejection to Coolant 4,034 70.93BTU/min kW 3,717 65.36BTU/min kW 3,309 58.19BTU/min kW

Heat Rejection to Ambient 1,301 22.88BTU/min kW 820 14.42BTU/min kW 638 11.22BTU/min kW

Heat Rejection to Exhaust (Dry) 4,183 73.55BTU/min kW 3,438 60.45BTU/min kW 2,602 45.75BTU/min kW

Fuel ConsumptionAir Fuel Ratio (dry) 16.2 vol/vol 16.2 vol/vol 16.2 vol/volIgnition timing (BTDC) 26 26deg deg 26 26deg deg 26 26deg degTotal Hydrocarbons 2.75 g/hp-hr 3.19 g/hp-hr 4.37 g/hp-hrNonMethane Hydrocarbons 0.17 g/hp-hr 0.2 g/hp-hr 0.27 g/hp-hrNOx 11.6 15.56g/hp-hr g/kW-hr 11 14.75g/hp-hr g/kW-hr 8 10.73g/hp-hr g/kW-hrCO 11 14.75g/hp-hr g/kW-hr 2.9 3.89g/hp-hr g/kW-hr 2.3 3.08g/hp-hr g/kW-hrO2 0.52 % 0.61 % 0.66 %CO2 435 583g/hp-hr g/kW-hr 496 665g/hp-hr g/kW-hr 583 782g/hp-hr g/kW-hr

Cranking System (Cold Starting Capability)Unaided Cold Start:

Minimum cranking speed: 250 RPM

Minimum ambient temperature

Cranking torque at minimum unaided cold start temperature: 480 651lb-ft N-m

Cold starting aids available Block Heater


EMIT Technologies, Inc772 Airfield LaneSheridan, WY 82801307.673.0883 Office307.673.0886 [email protected]

PREPARED FOR:Natural Gas Services Group

A. INFORMATION PROVIDED BY CUMMINSEngine: G8.3C118DIM Sheet: FR 92224Compression Ratio: 10.5:1RPM: 1800Horsepower: 118Fuel: Natural GasPiping size: 3"Annual Operating Hours: 8760Exhaust Flow: 604 CFMExhaust Temperature: 1374 °FAllowable Engine Backpressure: 27" WC

Emission DataNOx: 11.60 g/bhp-hr

CO: 11.00 g/bhp-hrTHC: 2.75 g/bhp-hr

1 of 2

g pNMHC: 0.17 g/bhp-hrHCHO: N/A g/bhp-hrOxygen: 0.52 %

B. POST CATALYST EMISSIONS TO BE ACHIEVED BY EMISSION CONTROL EQUIPMENTNOx: <0.5 g/bhp-hr

CO: <0.5 g/bhp-hrVOC: <0.5 g/bhp-hr

1 of 2

C. CONTROL EQUIPMENTCATALYTIC CONVERTER/SILENCER UNIT

Model EAS-1200T-0303F-D1S4ECatalyst Type NSCR, Precious group metalsManufacturer EMIT Technologies, Inc.Element Size 12" x 3.5"Catalyst Elements 1Housing Type Dual BedCatalyst Installation Accessible HousingConstruction 10 ga 304 Stainless SteelSample Ports 6 (0.5" NPT)Inlet Connections 3" flat face flangeOutlet Connections 3" flat face flangeConfiguration Assume Side In / End OutSilencer IntegratedSilencer Grade CriticalInsertion Loss 20-25 dBA

AIR FUEL RATIO CONTROLLERPart Number ENG-S-075Manufacturer EMIT Technologies, Inc.Description MODEL EDGE NG CSA certified AFR controller kit complete with:

EDGE NG Air Fuel Ratio Controller enclosure featuring: graphical display of oxygen sensor voltage, position of the digital power valve and thermocouple temperatures. Multiscreen digital display of controller and engine parameters. Integrated high temperature shutdown, Modbus enabled, 4 wire heated O2 sensor, O2

2 of 2

Digital Power Valve Size 0.75" NPT

D. WARRANTY

shutdown, Modbus enabled, 4 wire heated O2 sensor, O2 weldment, 25' Wiring harnesses, Digital power valve, Operations manualSINGLE BANK ENGINE

EMIT Technologies,Inc. warrants that the goods supplied will be free from defects in workmanship by EMIT Technologies, Inc. for a period of one (1) year from date of shipment. EMIT Technologies, Inc. will not be responsible for any defects which result from improper use, neglect, failure to properly maintain or which are attributable to defects, errors or omissions in any drawings, specifications, plans or descriptions, whether written or oral, supplied to EMIT Technologies, Inc. by Buyer.

Catalyst performance will be guaranteed for a period of 1 year from installation, or 8760 operating hours, whichever comes first. The catalyst shall be operated with an automatic air/fuel ratio controller. The performance guarantee shall not cover the effects of excessive ash masking due to operation at low load, improper engine maintenance, or inappropriate lubrication oil. The performance guarantee shall not cover the effects of continuous engine misfires (cylinder or ignition) exposing the catalyst to excessive exothermic reaction temperatures.

The exhaust temperature operating range at the converter inlet is 600°F minimum for oxidation catalyst and 750 oF for NSCR catalyst and 1250°F maximum.

If a high temperature shut down switch is not installed, thermal deactivation of catalyst at temperatures above 1300 oF is not covered.

The catalyst conversion efficiencies (% reduction) will be guaranteed for engine loads of 50 to 100 percent.

Engine lubrication oil shall contain less than 0.6% ash (by weight) with a maximum allowable specific oil consumption of 0.01 gal/bhp-hr. The maximum ash loading on the catalyst shall be limited to 350 g/m3. Phosphorous and zinc additives are limited to 0.03% (by weight).

The catalyst must not be exposed to the following know poisoning agents, including: iron, nickel, sodium, chromium, arsenic, zinc, lead, phosphorous, silicon, potassium, magnesium, copper, tin, and mercury. Total poison concentrations in the gas are limited to 0.3 ppm.

2 of 2

FUTURE OPERATIONS

Client Name: EncanaLocation: PTS PF

Job: FUTURE OPERATIONS

ProMax Filename: S:\EHS-Regulatory\Air\EFS\_Facilities\Patton Trust South\1.0 Permit\1.7 Modeling\ProMax\PTS PF_Dehy_2016.02.08.pmxProMax Version: 3.2.15289.0

Simulation Initiated: 02/08/2016 4:21:39 PM

A question mark (?) after a value, throughout the report, denotes an extrapolated or approximate value.

Office: (979) 776-5220FAX: (979) 776-4818

mailto:[email protected]://www.bre.com/

Report Navigator can be activated via the ProMax Navigator Toolbar.An asterisk (*), throughout the report, denotes a user specified value.

Simulation Report

Project: PTS PF_Dehy_2016.02.08.pmx

Licensed to EnCana Oil & Gas (USA) Inc. and Affiliates

Bryan Research & Engineering, Inc.Chemical Engineering ConsultantsP.O. Box 4747 Bryan, Texas 77805

FUTURE OPERATIONS

FUTURE OPERATIONS

Process Streams Condenser Vapor* Dry Basis Gas* Flash Sep Gas* Outlet Gas* Water Vapor*

Composition Status: Solved Solved Solved Solved Solved

Phase: Total From Block: Condenser DVDR-1 Flash Sep Gas/Glycol HEX Glycol RegeneratorTo Block: -- Saturator -- Outlet Gas To Drip Station Condenser

% % % % %

0.000741720 0.0794964 0.0166776 0.0795161 4.24153E-0514.8258 1.48360 7.34543 1.48111 0.856461

0 0 0 0 09.38602 72.2600 49.2347 72.2673 0.53742214.6252 14.1128 20.6069 14.1103 0.84367218.4315 6.85716 12.7340 6.85453 1.082143.58227 1.35240 2.08934 1.35200 0.22062310.6920 2.22488 4.33174 2.22367 0.6812914.87101 0.636541 1.20324 0.636064 0.3512275.08316 0.510180 1.08833 0.509661 0.3920252.08213 0.204908 0.394268 0.204663 0.211784

0.891433 0.0909965 0.143843 0.0908020 0.1990290.142201 0.0284733 0.0338558 0.0283978 0.0821398

0.0123565 0.00482207 0.00397834 0.00480588 0.01823321.27773 0.118342 0.225276 0.118174 0.152441

0 0 0 0 04.00536 0.0116019 0.0475268 0.0110360 0.6138262.92030 0.0156365 0.0443517 0.0146975 1.02879

0.109695 0.00152922 0.00282666 0.00144439 0.09335390.433472 0.00654564 0.0115493 0.00616089 0.4236726.62757 0 0.441954 0.00546255 92.2068

1.04527E-08 0 0.000221574 5.80836E-05 0.003153201.11638E-06 0.000118727 8.14258E-06 0.000116999 0.00183156

Process Streams Condenser Vapor* Dry Basis Gas* Flash Sep Gas* Outlet Gas* Water Vapor*

Properties Status: Solved Solved Solved Solved Solved

Phase: Total From Block: Condenser DVDR-1 Flash Sep Gas/Glycol HEX Glycol RegeneratorTo Block: -- Saturator -- Outlet Gas To Drip Station Condenser

Property Units

Temperature °F 100* 94.8852 114.820 96.0516 209.442Pressure psig 0* 1249.5 40 1240 0.29Std Vapor Volumetric Flow MMSCFD 0.00170593 32.9891 0.00977389 32.9789 0.0298464Std Liquid Volumetric Flow sgpm 0.0305405 455.688 0.148310 455.499 0.157047Mole Fraction Vapor % 100 100 100 100 100

TolueneEthylbenzenem-XyleneWaterTriethylene GlycolC10+

HeptaneOctaneNonanen-Hexane2,2,4-TrimethylpentaneBenzene

PropaneIsobutanen-ButaneIsopentanen-Pentane2-Methylpentane

Mole Fraction

NitrogenCarbon DioxideHydrogen SulfideMethaneEthane

FUTURE OPERATIONS

FUTURE OPERATIONS

Process Streams Combined VRT Gas* Drip Oil* Drip Tank Flash* Drip VRT Gas* DS Drip Return* HP Inlet Gas*

Composition Status: Solved Solved Solved Solved Solved Solved

Phase: Total From Block: MIX-103 Drip Tank Drip Tank Drip VRT -- --To Block: VRU Compr -- -- RCYL-1 MIX-101 MIX-106

% % % % % %

0.00190836 6.40590E-09 4.08991E-06 0.000478946 0.0202112* 0.084*1.15406 0.000281189 0.0198996 0.252198 1.16023* 1.551*

0.0128400 3.65087E-05 0.000908854 0.00422971 0* 0.0075*9.45410 0.000434233 0.0818120 2.76258 34.9354* 77.7045*17.7684 0.0546230 1.64631 9.08310 17.3075* 13.004*26.9779 1.65551 14.5739 27.1659 15.6502* 4.838*9.81192 4.14701 14.1728 14.0011 4.85962* 0.781*18.9995 15.7301 35.6768 28.5152 9.66826* 1.182*6.30199 16.5570 15.1191 8.74802 4.24808* 0.301*5.04292 17.5040 11.9447 6.44569 3.91358* 0.242*1.93822 13.6415 3.77297 1.73237 2.52888* 0.125*

0.798167 10.7790 0.707762 0.290869 2.01058* 0.073*0.258657 4.88776 0.100787 0.0388569 0.959595* 0.018*

0.0479722 1.17486 0.00778786 0.00277117 0.241182* 0.004*1.09617 9.33049 1.85451 0.818169 1.70224* 0.066*

0 0 0 0 0* 0*0.109639 0.883053 0.184391 0.0836206 0.149957* 0.006*0.145212 2.05187 0.110701 0.0452586 0.348978* 0.009*

0.0150351 0.287605 0.00520886 0.00201679 0.0514551* 0*0.0651971 1.29322 0.0196383 0.00751441 0.232114* 0.003*

0.000202013 0.0216277 6.00188E-08 1.58133E-08 0.0118919* 0.001*

Process Streams Combined VRT Gas* Drip Oil* Drip Tank Flash* Drip VRT Gas* DS Drip Return* HP Inlet Gas*

Properties Status: Solved Solved Solved Solved Solved Solved

Phase: Total From Block: MIX-103 Drip Tank Drip Tank Drip VRT -- --To Block: VRU Compr -- -- RCYL-1 MIX-101 MIX-106

Property Units

Temperature °F 87.3946 74.83 74.83* 60* 85* 92*Pressure psig 4 0 0* 4* 1200* 1250*Std Vapor Volumetric Flow MMSCFD 0.741979 0.235131 0.0757491 0.255276 0.320730 4.90318*Std Liquid Volumetric Flow sgpm 15.0139 6.25239 1.73288 5.44366 5.83333* 65.2624Mole Fraction Vapor % 99.9995 0 100 100 1.31395 100

TolueneEthylbenzenem-XyleneC10+



Mole Fraction


FUTURE OPERATIONS

Process Streams

Composition Status:

Phase: Total From Block:To Block:

Process Streams

Properties Status:


Property Units

Temperature °FPressure psigStd Vapor Volumetric Flow MMSCFDStd Liquid Volumetric Flow sgpmMole Fraction Vapor %




Mole Fraction


HP Inlet Oil* HP Sep Gas* HP Sep Oil* HT Gas* HT Oil* LP Drip Gas* LP Inlet Gas* LP Inlet Oil*

Solved Solved Solved Solved Solved Solved Solved Solved

-- HP Separator HP Separator Heater Treater Heater Treater LP Scrubber -- --MIX-106 MIX-105 Heater Treater MIX-100 VRT RCYL-3 MIX-104 MIX-104

% % % % % % % %

0.0131900* 0.0879992 0.0145992 0.0251234 0.000176626 0.0203096 0.084* 0.0131900*0.291870* 1.47308 1.28142 2.08405 0.137009 1.34099 1.551* 0.291870*

0* 0.00633634 0.0104210 0.0126760 0.00192215 0.00846552 0.0075* 0*7.75988* 78.8934 27.0225 48.0095 0.906046 36.3022 77.7045* 7.75988*7.71780* 12.4526 13.3234 21.9935 2.07036 21.4025 13.004* 7.71780*9.39482* 4.39609 10.4984 14.0986 4.27003 21.6619 4.838* 9.39482*3.36064* 0.693397 2.93338 3.11667 2.26653 5.76784 0.781* 3.36064*7.19633* 1.05634 5.69162 5.43652 5.42449 9.46463 1.182* 7.19633*4.33994* 0.305000 2.75747 1.81016 4.30032 2.05111 0.301* 4.33994*4.44131* 0.246569 2.79335 1.53810 4.70607 1.42446 0.242* 4.44131*4.01224* 0.124842 2.51514 0.723061 4.98075 0.320698 0.125* 4.01224*7.28290* 0.0928080 4.37606 0.386240 9.88425 0.0529929 0.073* 7.28290*7.33908* 0.0458904 4.33708 0.139895 10.1217 0.00749328 0.018* 7.33908*3.84264* 0.0126276 2.30742 0.0275725 5.34692 0.000548498 0.004* 3.84264*3.18543* 0.0776457 1.90785 0.440164 4.03880 0.147726 0.066* 3.18543*

0* 0 0 0 0 0 0* 0*0.324920* 0.00677818 0.196974 0.0433522 0.412118 0.0158018 0.006* 0.324920*1.60128* 0.0146565 0.951018 0.0711033 2.16886 0.00838847 0.009* 1.60128*

0.476230* 0.00231846 0.277690 0.00809885 0.653939 0.000396119 0* 0.476230*2.41826* 0.0108018 1.43694 0.0355610 3.34074 0.00149794 0.003* 2.41826*25.0012* 0.000841672 15.3673 0.000151870 34.9690 6.98785E-09 0.001* 25.0012*

HP Inlet Oil* HP Sep Gas* HP Sep Oil* HT Gas* HT Oil* LP Drip Gas* LP Inlet Gas* LP Inlet Oil*

Solved Solved Solved Solved Solved Solved Solved Solved

-- HP Separator HP Separator Heater Treater Heater Treater LP Scrubber -- --MIX-106 MIX-105 Heater Treater MIX-100 VRT RCYL-3 MIX-104 MIX-104

92* 97.0352 97.0352 110* 110 70 105* 105*1250* 1249.5 1249.5 50* 50 75 115* 115*

0.439490 4.62760 0.715076 0.708614 7.54842 0.970110 24.5828* 10.117514.8661* 61.2515 18.8770 11.2981 301.275 16.4272 327.202 342.230*

0 100 0 100 0 100 99.9988 12.3897

FUTURE OPERATIONS

Process Streams

Composition Status:


Process Streams

Properties Status:


Property Units





Mole Fraction


LP Scrubber Drip* LP Sep Gas* LP Sep Oil* Outlet Gas* Outlet Oil* Tank Flash* VRT Drip*

Solved Solved Solved Solved Solved Solved Solved

LP Scrubber IP Separator IP Separator MIX-105 Tank(s) Tank(s) Drip VRTSplitter IP Compr - 1st/2nd Stg Heater Treater Outlet Gas -- -- Drip Tank

% % % % % % %

0.000227663 0.0806276 0.00115309 0.0794912 5.61059E-06 1.00139E-060.119122 1.45393 0.211440 1.48350 0.0343155 0.00506141

0.00205970 0.00619815 0.00212674 0.00651703 0.000858552 0.0002490641.31333 72.4334 2.85553 72.2553 0.0750692 0.02026274.49996 13.8475 2.87533 14.1119 0.674609 0.44245415.4499 6.60086 4.60295 6.85671 2.71173 4.8032210.2347 1.32485 2.28318 1.35231 1.89799 6.5899024.7483 2.25112 5.40029 2.22473 4.83304 20.590312.8513 0.719378 4.21263 0.636500 4.25074 16.206611.6578 0.599003 4.58977 0.510146 4.73360 16.14946.62569 0.270852 4.81448 0.204894 5.18299 11.23694.21551 0.137122 9.51410 0.0909906 10.4921 8.325061.83058 0.0476815 9.73226 0.0284715 10.7934 3.72137

0.446280 0.00904687 5.13532 0.00482175 5.71047 0.8904934.21474 0.162627 3.90273 0.118334 4.23155 7.50889

0 0 0 0 0 00.402446 0.0159858 0.397869 0.0116011 0.432024 0.7128170.789309 0.0250513 2.08722 0.0156355 2.30470 1.578880.107287 0.00275625 0.628932 0.00152912 0.697499 0.2187960.481971 0.0119821 3.21070 0.00654521 3.56439 0.982902

0.00954112 3.81297E-05 33.5420 0.000118719 37.3789 0.0163579

LP Scrubber Drip* LP Sep Gas* LP Sep Oil* Outlet Gas* Outlet Oil* Tank Flash* VRT Drip*

Solved Solved Solved Solved Solved Solved Solved

LP Scrubber IP Separator IP Separator MIX-105 Tank(s) Tank(s) Drip VRTSplitter IP Compr - 1st/2nd Stg Heater Treater Outlet Gas -- -- Drip Tank

70 91.9383 91.9383 94.8852 74.83 74.83* 6075 114.5 114.5 1249.5 0 0* 4

0.506005 27.1583 7.54196 32.9913 7.06176 0 0.31088011.9206 375.736 293.696 455.708 291.705 0 7.98528

0 100 0 100 0 0

FUTURE OPERATIONS

Process Streams

Composition Status:


Process Streams

Properties Status:


Property Units





Mole Fraction


VRT Gas* VRT Oil* 11*

Solved Solved Solved

VRT VRT MIX-100MIX-103 Tank(s) MIX-107

% % %

0.00265813 5.61059E-06 0.02234311.62713 0.0343155 1.65464

0.0173554 0.000858552 0.010241212.9639 0.0750692 41.246022.3233 0.674609 21.652126.8816 2.71173 18.46747.61428 1.89799 4.6483814.0067 4.83304 7.764185.01974 4.25074 1.949584.30667 4.73360 1.472562.04607 5.18299 0.4905471.06435 10.4921 0.193637

0.373974 10.7934 0.06337250.0716858 5.71047 0.0119539

1.24201 4.23155 0.2711570 0 0

0.123285 0.432024 0.02743030.197657 2.30470 0.0348567

0.0218651 0.697499 0.003647020.0954595 3.56439 0.0158741

0.000307982 37.3789 6.41004E-05

VRT Gas* VRT Oil* 11*

Solved Solved Solved

VRT VRT MIX-100MIX-103 Tank(s) MIX-107

103.949 103.949 83.86955* 5 50

0.486668 7.06176 1.678999.56954 291.705 27.7294

100 0 100




END OF APPLICATION