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Peyto 2017 Aggregated Project for Methane Emission Reductions from Pneumatic

Devices

March 2019

Version 2.0 Report Template – July 2018

Offset Project Report Form

Peyto 2017 Aggregated Project for Methane Emission Reductions from Pneumatic Devices

Project Developer:

Peyto Exploration and Development Corp

Prepared by:

North Shore Environmental Consultants

Reporting Period:

January 1, 2017 to October 31, 2018

Date:

March 5, 2019


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Greenhouse Gas Assertion

Project Developer:

Peyto Exploration and Development Corporation

Ivan Butynets

300-600 3rd Ave SW

Calgary, Alberta T2P 0G5

403-710-3717

Peyto.com

[email protected]

Project Documents:


Peyto 2017 Aggregated Project for Methane Emission Reductions from Pneumatic Devices, Offset

Project Plan, December 2017

Quantification Protocol for Greenhouse Gas Emission Reductions from Pneumatic Devices, Version

2.0, January 25, 2017

Project Identification:



This project achieves GHG reductions at well sites through both the capture of gas from pneumatic

devices for use in building heating and the conversion of chemical injection pumps from gas to

electric via a solar power system. This reduces the amount of methane vented directly to the

atmosphere through destruction in building heaters, and through elimination and reduction in

pump and device conversions.

All subprojects are executed in Alberta, and are located at remote wellsite locations. This project

includes GHG reductions from approximately 1,253 locations for the described project conditions.

The exact locations of all subprojects are provided in the Aggregated Project Reporting Sheet.

Emission Reduction or Sequestration Assertion:

Vintage Gas Type Quantity (tCO2e)

Vintage year: 2017

Reporting period date range:

January 1, 2017 to December

31, 2017

CO2

CH4

N2O

-3,379

28,141

-26

Vintage year: 2018

Reporting period date range:

January 1, 2018 to October 31,

2018

CO2

CH4

N2O

-3,223

36,249

-25


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Total Quantity 57,737


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Version 2.0 Report Form – July 2018

Project Developer Signature:

I am a duly authorized corporate officer of the project developer mentioned above and have personally examined and am familiar with the information submitted in this greenhouse gas assertion, the accompanying project report on which it is based. Based upon reasonable investigation, including my inquiry of those individuals responsible for obtaining the information, I hereby warrant that the submitted information is true, accurate and complete to the best of my knowledge and belief, and that all matters affecting the validity of the emission reduction claim or the protocol(s) upon which it is based have been fully disclosed. I understand that any false statement made in the submitted information may result in de-registration of credits and may be punishable as a criminal offence in accordance with provincial or federal statutes.

The project developer has executed this offset project report as of the 08 day of February, 2019.

Signature: _ _______________________________________

Name: Todd Burdick, P.Eng

Title: VP Production, Peyto Exploration & Development Corp.


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Table of Contents

Greenhouse Gas Assertion ..................................................................................................... 2 1.0 Contact Information .............................................................................................. 6 2.0 Project Scope and Site Description .......................................................................... 6

2.1 Project Implementation .......................................................................................... 7 2.2 Protocol ............................................................................................................... 7 2.3 Risks ................................................................................................................... 8

3.0 Project Quantification ............................................................................................ 8 3.1 Summary Table Non-Levied Emissions ..................................................................... 8 3.1 Summary Table Levied Emissions and Biogenic CO2 ................................................... 9 3.2 Calculations .......................................................................................................... 9

4.0 References ......................................................................................................... 16 Appendix A: Supporting Information ..................................................................................... 17

List of Tables

Table 1: Project Contact Information ...................................................................................... 6 Table 2: Project Information .................................................................................................. 6


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1.0 Contact Information

Table 1: Project Contact Information

Project Developer Contact Information Additional Contact Information

Peyto Exploration and Development

Corporation

Ivan Butynets

300-600 3rd Avenue SW

Calgary, Alberta, T2P 0G6

403-710-3717

www.peyto.com

[email protected]

Authorized Project Contact (if applicable)

North Shore Environmental Consultants

Hillary Yeung

134-12143 40th St SE

Calgary, Alberta, T2Z 4E6

403-226-3095

www.northshoreenv.com

[email protected]

2.0 Project Scope and Site Description

Table 2: Project Information

Project title Peyto 2017 Aggregated Project for Methane Emission Reductions from

Pneumatic Devices

Project purpose and

objectives

The objective of this project is to reduce methane emissions from

venting from pneumatic devices at 1,253 well sites throughout Alberta

through a combination of vent gas capture and solar pump

electrifications.

Activity start date January 1, 2016

Offset start date January 1, 2017

Offset crediting

period

January 1, 2017 – December 31, 2024

Reporting period

covered by the

project


Actual emission

reductions/

57,738 tonnes CO2e


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sequestration

Unique site identifier This aggregated project has a completed aggregated project reporting

sheet with locations of all subprojects, which is submitted with this

report.

Is the project located

in Alberta?

Yes

Project boundary All subprojects will be executed in Alberta, and are located at remote

wellsite locations. This project includes GHG reductions from

approximately 1,253 locations for the described project conditions.

Ownership Carbon offset credits generated under the 2017 Aggregated Project for

Methane Emission Reductions from Pneumatic Devices will belong to the

Project Developer, Peyto Exploration and Development Corp. Original

ownership and right of claim to offset credits are demonstrated through

land/mineral right contracts, operating permits, royalty payments

agreements, and/or other documentation.

2.1 Project Implementation

The emission offset project was implemented in accordance with the project plan and the

Quantification Protocol for Greenhouse Gas Emission Reductions from Pneumatic Devices,

Version 2.0, January 2017.

This is the first project report submitted for this emission offset project.

There are no modifications to calculation procedures.

There is one modification to data collection. It was previously assumed that the number of

pump strokes will be estimated by the amount of chemical injected. Since the project plan was

submitted, the pump controller was able to be connected to the out flow computers, and

therefore stroke counts are now automatically updated daily.

There are no modifications to record keeping procedures.

There are no modifications to emission factors

There are no modifications to any other variables during the reporting period.

There are no changes to the emission offset project as a result of regulatory changes

There are no changes to the emission reduction or sequestration

There are no modifications to record keeping procedures.

2.2 Protocol

The project uses the Quantification Protocol for Greenhouse Gas Emission Reductions from

Pneumatic Devices, Version 2.0, January 2017. This protocol is applicable to the emission offset

project because project will achieve ongoing greenhouse gas emission reductions through the

combination of vent gas capture of pneumatic vent sources, the electrification of pneumatic

chemical pumps via solar power systems, the conversion of high bleed pneumatic controllers to

low bleed devices, and instrument gas to instrument air system conversions.


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For this reporting period, subprojects vent gas capture of pneumatic vent sources and

electrification of pneumatic chemical pump project types were reported.

This emission offset project meets the quantification protocol applicability requirements due to

the following:

1. Pneumatic devices in the project condition perform the same effective process control or

operational function as the baseline condition, which implies that at a minimum:

a. Non-vent devices are effective replacements based on manufacturer specifications

b. Vent gas capture systems are installed in a manner that allows relief of vent

backpressure to maintain functionality of pneumatic devices.

2. This project reduces or eliminates emissions from methane venting.

3. Conversions are defined as to occur at brownfield sites with existing equipment being

replaced.

4. The project proponent inspects and maintains pneumatic devices as a part of regular

operations for vent gas capture projects. Records demonstrating the maintenance and

inspection activities of facilities are kept.

5. The project proponent has developed and maintained an inventory of devices.

6. This project meets the requirements for offset eligibility for the Alberta carbon offset

system.

The following protocol flexibilities were applied to the project:

1. Multiple conversions and installs were aggregated under one project report. This flexibility

allows for the offset project developer to minimize administration and verification costs with

each emission offset subproject by combining multiple similar subprojects into a single

aggregated project.

2.3 Risks

There were no unidentified risks that were not already outlined in the project plan. There are no

other emission offset projects on the legal land description of the emission offset project sites.

3.0 Project Quantification

3.1 Summary Table Non-Levied Emissions

Vintage1 Gas Type2 Baseline

Emissions

Project Emissions Total Reduction

or

Sequestration

Year 2017 CO2 51 3,430 -3,379

Year 2017 CH4 28,372 231 28,141

Year 2017 N2O 0 26 -26

Year 2017 Other (specify) n/a


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Total Year 2017 CO2e 28,423 tCO2e 3,687 tCO2e 24,736 tCO2e

Year 2018 CO2 66 3289 -3,223

Year 2018 CH4 36,470 221 36,249

Year 2018 N2O 0 25 -25

Year 2018 Other n/a

Total Year 2018 CO2e 36,536 tCO2e 3,535 tCO2e 33,001 tCO2e

Total for

Reporting Period

CO2e 64,959 tCO2e 7,222 tCO2e 57,737 tCO2e

1 - If the reporting period spans more than one year, provide summary for each year separately

2 - Indicate if gas type is not applicable for this project

3.1 Summary Table Levied Emissions and Biogenic CO2

There are no levied or biogenic emissions in this project report. Emission reductions were attained

through vent gas capture and the installation of solar-powered electric pneumatic devices. These

devices are exempt from paying the carbon levy due to being part of the oil and gas production

process.

3.2 Calculations

The project report includes the following project types eligible under the quantification protocol:

Vent gas capture

o Vent gas will be captured from pneumatic vent sources through vent gas

emission bottles at each wellsite. Each emissions bottle captures enough gas to

feed all Catadyne heaters in the wellsite separator shack.

Chemical pump electrification

o Pneumatic pumps will be converted to a non-venting solar-powered equivalent.

The following provides detail on the monitoring plan as related to the inputs to the calculation:

Gas analysis data is sampled on an annual or biennual basis (as per AER D017

requirements). The gas samples are collected and analyzed by an accredited third-party

laboratory and electronic copies of the results are provided to Peyto. This analysis

determines the fractions of the individual molecular components found in the gas

streams. The relevant information from the analysis is uploaded into CygNet by Peyto

under the appropriate facility profile.

It was previously assumed that the number of pump strokes will be estimated by the

amount of chemical injected. Since the project plan was submitted, the pump controller

was able to be connected to the out flow computers, and therefore stroke counts are

now automatically updated daily.

Operations personnel use tablets with wifi capabilities to record Catadyne activity data

for each individual well site. All data is tracked in SCADA:

o Operating hours are measured continuously and monitored by field operators.

o Cata-dyne load settings are recorded by operators.


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All monitoring specifications were in accordance with the Project Plan. Manufacturer-supplied

specifications for Texsteam 1400 pumps and injection pressures were used to determine pump

emission factors. Catadyne heater fuel consumption rate is estimated from manufacturer

specifications. All Catadyne heaters purchased are either 12x24 or 24x24 in size. To simplify

inventory, two 12x24 Catadyne heaters were selected in the place of one 24x24 heater. See

Appendix A for more detail.

Emissions reductions were calculated on a project basis for each sub-project type and then

subsequently aggregated into a total emissions reduction, using the following equations:

Emissions Reduction = Sum of Emissions Baseline – Sum of Emissions Project

Chemical Pump Electrification Projects:

Emissions Baseline = Emissions Baseline Vented Gas

Emissions Project = Emissions Project Vented Gas

Vent Gas Capture Projects:

Emissions Baseline = Emissions Uncaptured Vent Gas

Emissions Project = Emissions Vent Gas Capture

Where:

Emissions Baseline = Emissions under the baseline condition of either project type

Emissions Baseline Vented Gas = Emissions under B7 baseline vented gas

Emissions Uncaptured Vent Gas = Emissions under B8 uncaptured fuel gas

Emissions Project = Sum of emissions under the project condition

Emissions Project Vented Gas = Emissions under P7 project vented gas

Emissions Vent Gas Capture = Emissions under P17 vent gas capture

Calculation of Baseline Emissions:

B7 – Baseline Vented Gas and B8 – Baseline Uncaptured Vent Gas for all project Sub-

Types:

Emissions Baseline Vented Gas

∑ ( ⁄ ) ∑ (

⁄ )

Emissions Uncaptured fuel gas ( ) ⁄ ( ) ⁄

Where:

Vented Gas Baseline = for converting pumps to non-venting equivalents, or;

Captured Gas for fuel gas capture


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Calculation parameters for Baseline Emissions

Parameter/Variable Unit Measured

/Estimated Method Frequency Justification

Emissions Baseline Vented

Gas

Tonnes of

CO2e N/A N/A N/A

Quantity being

calculated

Emissions Uncaptured Fuel

Gas

Tonnes of

CO2e N/A N/A N/A

Quantity being

calculated

Vented Gas Baseline j m3 Calculated See Above Per Report

Intermediary

quantity being

calculated.

Captured Gas Baseline j m3 Calculated See Above Per Report

Intermediary

quantity being

calculated.

%CH4 % Measured Direct

Annual or

biennually as

per AER

D017

requirements

Gas composition

should remain

relatively stable

during steady-

state operation.

Protocol

deviation

granted by

ACCO (see

Appendix E)

%CO2 % Measured Direct

Annual or

biennually as

per AER

D017

requirements

Gas composition

should remain

relatively stable

during steady-

state operation.

Protocol

deviation

granted by

ACCO (see

Appendix E)

Density of CH4 (ρCH4) kg/m3 Estimated Reference N/A

Adjusted for

standard

temperature and

pressure.

Source: GPSA

Engineering Data

Book

Density of CO2 (ρCO2) kg/m3 Estimated Reference N/A

Adjusted for

standard

temperature and

pressure.


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Source: GPSA

Engineering Data

Book

Operating hours /

Op.Hrs Hrs Measured

Direct

measurement Annual

Operating hours

based on

measured well

production

hours.

Pump Strokes n/a Estimated Direct

Measurement Per report

Daily stroke

counts are

automatically

uploaded

Pump Emission Factor

/ EFPump Type j m3/stroke Estimated

Manufacturer

reference

data

Annual

Annual estimate

in consideration

of changes to

injection

pressure. Base

case used was a

Texsteam 1400

pump (3/8”

plunger, 1”

stroke). See

Appendix A.

GWPCH4 n/a Estimated

Provided in

Carbon Offset

Emission

Factor

Handbook

N/A

Most current

factor published

in the Carbon

Offset Emission

Factors

Handbook will be

used.

Discount Rate due to

Leaks/DR % Estimated

See Appendix

A of Protocol

See

Appendix A

of Protocol

Subprojects

have a regular

inspection and

maintenance

program. The DR

has been set to

0.025.

Fuel Device

Load/Load % Measured

Direct

measurement

of

combustion

device

Annual/Per

Report

Reading from

fuel use device


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Fuel Consumption

Rate / Fuel Con. Rate kg/hr Estimated

Reference

from

manufacturer

specifications

Once

Estimated

parameter is a

conservative

overestimation

in absence of

equipment

measurement

(see Appendix

A).

Calculation of Project Emissions:

Project vented gas – P7 for conversion project sub-types:

Emissions Project Vented Gas

∑ ( ⁄ ) ∑ (

⁄ )

Where:

Vented Gas = 0 for electrification of pumps

Calculation parameters for Project Condition: Conversion project sub-types



Vented Gas Project j m3 Calculated See Above Per Report

Intermediary

quantity being

calculated.

%CH4 % Measured Direct

Annual or

biennually as

per AER

D017

requirements

Gas composition

should remain

relatively stable

during steady-

state operation.

Protocol

deviation granted

by ACCO (see

Appendix E)

%CO2 % Measured Direct

Annual or

biennually as

per AER

D017

requirements

Gas composition

should remain

relatively stable

during steady-

state operation.

Protocol

deviation granted


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by ACCO (see

Appendix E)

Density of CH4 (ρCH4) kg/m3 Estimated Reference N/A

Adjusted for

standard

temperature and

pressure.

Source: GPSA

Engineering Data

Book

Density of CO2 (ρCO2) kg/m3 Estimated Reference N/A

Adjusted for

standard

temperature and

pressure.

Source: GPSA

Engineering Data

Book

GWPCH4 n/a Estimated

Provided in

Carbon Offset

Emission

Factor

Handbook

N/A

Most current

factor published

in the Carbon

Offset Emission

Factors

Handbook will be

used.

Vent Gas Capture Projects – P17 Vent Gas Capture

Emissions Vent Gas Capture =

⁄ ⁄ ⁄ ( )

Where:

Calculation parameters for Project Condition: Vent Gas Capture

Unit

Measure

d

/Estimat

ed

Method Frequen

cy Justification

Emissions Vent Gas

Capture

Tonnes

of CO2e N/A N/A N/A

Quantity being

calculated


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Unit

Measure

d

/Estimat

ed

Method Frequen

cy Justification

Captured Gas Project j m3 Calculated See Above Per

Report

Intermediary quantity

being calculated.

Destruction

Efficiency of

Combustion Source

/ DE

% Estimated Referenced Value Per

Report

The DE has been set

to 100% based on

manufacturer

specified value (see

Appendix A).

CO2 Emission

Factor EFFuelCO2

g CO2

per m3 Estimated

Carbon Offset

Emission Factors

Handbook, Fuel

Related Emissions

“non-marketable

product”

Per

Report

Must use most current

factors published in

the Carbon Offset

Emission Factors

Handbook.

CH4 Emission Factor

EFfuelCH4

g CH4

per m3 Estimated

Carbon Offset

Emission Factors

Handbook, Fuel

Related Emissions

“non-marketable

product”

Per

Report



the Carbon Offset

Emission Factors

Handbook.

N2O Emission

Factor EFFuelN2O

g N2O

per m3 Estimated

Carbon Offset

Emission Factors

Handbook, Fuel

Related Emissions

“non-marketable

product”

Per

Report



the Carbon Offset

Emission Factors

Handbook.

Operating hours /

Op.Hrs Hrs Measured Direct measurement Annual

Operating hours

based on measured

well production hours.

Fuel Device

Load/Load % Measured

Direct measurement of

combustion device

Annual/P

er Report

Reading from fuel use

device

Fuel Consumption

Rate / Fuel Con.

Rate

kg/hr Estimated

Reference from

manufacturer

specifications

Once

Estimated parameter

is a conservative

overestimation in

absence of equipment

measurement (see

Appendix A).

%CH4 % Measured Direct Annual

or

biennuall

Gas composition

should remain

relatively stable


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Unit

Measure

d

/Estimat

ed

Method Frequen

cy Justification

y as per

AER

D017

requirem

ents

during steady-state

operation. Protocol

deviation granted by

ACCO (see Appendix

E)

Density of CH4

(ρCH4) kg/m3 Estimated Reference N/A

Adjusted for standard

temperature and

pressure. Source:

GPSA Engineering

Data Book

GWPCH4, CO2, N2O Unitless Estimated

Provided in Carbon

Offset Emission Factor

Handbook

N/A

Most current factor

published in the

Carbon Offset

Emission Factors

Handbook will be

used.

4.0 References

Cata-dyne, Year Unknown, WX Series Explosion-Proof Gas Catalytic Heaters Catalog

Dresser Industrial Products Group (TexSteam), 2006, Series 5100 Air or Gas Driven Injectors

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Appendix A: Supporting Information

7Cata‑Dyne™

WX

Series E

xplo

sion‑P

roof G

as Catalytic H

eaters – Cata‑D

yne™ E

xplo

sion‑P

roof G

as Catalytic H

eaters

WX Series Explosion-Proof Gas Catalytic HeatersThe Cata‑Dyne™ WX Series infrared gas catalytic explosion‑proof

heaters are the industry standard for hazardous location heating needs�

They are available in over twenty, three‑inch depth cabinet sizes, with

gas, electrical and accessory connections on the back side of the

heater� These are the heaters of choice for many of our customers who

have come to trust their reliability�

Applications

WX Series heaters are used in many different applications that involve spot or space heating where hazardous materials may be present�

These include:

• Comfort heating for industrial buildings and installations

• Freeze protection for equipment or components

• Drying or curing processes

Features

• Heater box constructed of 300 series stainless steel for corrosion

protection

• Cata‑Dyne™ proprietary explosion‑proof catalyst pad�

• Standard 3/8" NPT gas connections

• Explosion‑proof electrical junction box with standard 3/4" NPT

connections

• Cata‑Dyne™ heaters are designed to operate on either natural gas

or propane

• Cata‑Dyne™ heaters do not require electrical power to operate

once they have been started

• Our explosion‑proof catalytic technology is the most efficient in

the industrial heating market

• Heater contains no moving parts and is designed to operate

indefinitely when supplied with air and clean fuel

• Internal heater components such as our proprietary catalyst

pad and preheat Caloritech™ tubular element are manufactured

in‑house

Certifications

The WX Series Cata‑Dyne™ explosion‑proof catalytic heaters are approved for the following:

• Canadian Standards Association (CSA) for use in Class I, Division

1 & 2, Group D hazardous locations

• Factory Mutual (FM) for use in Class I, Division 1, Group D

hazardous locations� Temperature code T2C at an ambient

temperature of 40°C (104°F)

See Table 1, page 11 for fuel & electrical ratings�

11Cata‑Dyne™

WX

& B

X Fuel &

Electrical R

ating Data – C

ata‑Dyne™

Exp

losio

n‑Pro

of Gas C

atalytic Heaters

Table 1 – WX Series Fuel and Electrical Rating Data (CSA and FM)

Model No.

Max. Gas Input Min. Gas Input Max. Gas FlowStart‑Up Amperage

Natural Gas / Propane Natural Gas Propane CFH m3/hr

Btu/hr kW Btu/hr kW Btu/hr kWNatural

GasPropane

Natural Gas

Propane 12V 120V 208V 240V 380V 480V 600V

W6x6 1,250 0�366 500 0�147 375 0�110 1�25 0�5 0�0354 0�0142 7�1 0�7 – 0�4 – – –

W6x12 2,500 0�733 1,000 0�293 750 0�220 2�5 1�0 0�0708 0�0283 7�1 0�7 – 0�4 – – –

W6x24 5,000 1�465 2,000 0�586 1,500 0�440 5�0 2�0 0�1416 0�0566 15�0 2�1 1�2 1�0 – – –

W6x60 12,500 3�663 5,000 1�465 3,750 1�099 12�5 5�0 0�3540 0�1416 – – – – – 1�3 ‑

W8x8 2,222 0�651 900 0�264 700 0�205 2�2 0�9 0�0629 0�0252 7�1 0�7 ‑ 0�4 – – –

W10x12 4,167 1�221 1,700 0�498 1,250 0�366 4�2 1�7 0�1180 0�0472 15�0 2�1 1�2 1�0 – – –

W12x12 5,000 1�465 2,000 0�586 1,500 0�440 5�0 2�0 0�1416 0�0566 15�0 2�1 1�2 1�0 – – –

W12X24 10,000 2�931 4,000 1�172 3,000 0�879 10�0 4�0 0�2832 0�1133 30�0 4�2 2�4 2�1 – 1�5 0�9

W12x36 15,000 4�396 6,000 1�758 4,500 1�319 15�0 6�0 0�4248 0�1699 30�0 5�0 2�9 2�5 1�6 1�3 1�0

W12x48 20,000 5�861 8,000 2�345 6,000 1�758 20�0 8�0 0�5663 0�2265 30�0 6�7 3�9 3�3 2�1 1�7 1�3

W12x60 25,000 7�327 10,000 2�931 7,500 2�198 25�0 10�0 0�7079 0�2832 45�0 10�4 6�0 5�2 3�3 2�6 2�1

W12x72 30,000 8�792 12,000 3�517 9,000 2�638 30�0 12�0 0�8495 0�3398 ‑ 12�1 7�0 6�0 3�8 3�0 2�4

W18x24 15,000 4�396 6,000 1�758 4,500 1�319 15�0 6�0 0�4248 0�1699 30�0 4�2 2�4 2�1 – 1�5 –

W18x30 18,750 5�495 7,500 2�198 5,625 1�649 18�75 7�5 0�5309 0�2124 – – – – – 1�5 –

W18x36 22,500 6�594 9,000 2�638 6,750 1�978 22�5 9�0 0�6371 0�2549 – 10�0 5�8 5�0 3�2 2�5 2�0

W18x48 30,000 8�792 12,000 3�517 9,000 2�638 30�0 12�0 0�8495 0�3398 – 13�3 7�7 6�7 4�2 3�3 2�7

W18x60 37,500 10�990 15,000 4�396 11,250 3�297 37�5 15�0 1�0619 0�4248 – 20�8 12�0 10�4 6�6 5�2 4�2

W18x72 45,000 13�188 18,000 5�275 13,500 3�956 45�0 18�0 1�2743 0�5097 – 24�2 14�0 12�1 7�6 6�0 4�8

W24x24 20,000 5�861 8,000 2�345 6,000 1�758 20�0 8�0 0�5663 0�2265 30�0 4�2 2�4 2�1 – 1�5 –

W24x30 25,000 7�327 10,000 2�931 7,500 2�198 25�0 10�0 0�7079 0�2832 30�0 4�2 2�4 2�1 – 1�5 –

W24x36 30,000 8�792 12,000 3�517 9,000 2�638 30�0 12�0 0�8495 0�3398 – 10�0 5�8 5�0 3�2 2�5 2�0

W24x48 40,000 11�723 16,000 4�689 12,000 3�517 40�0 16�0 1�1327 0�4531 – 13�3 7�7 6�7 4�2 3�3 2�7

W24x60 50,000 14�654 20,000 5�861 15,000 4�396 50�0 20�0 1�4159 0�5663 – 20�8 12�0 10�4 6�6 5�2 4�2

W24x72 60,000 17�584 24,000 (7�034) 18,000 5�275 60�0 24�0 1�6990 0�6796 – 24�2 14�0 12�1 7�6 6�0 4�8

Table 2 – BX Series Fuel and Electrical Rating Data (FM only) ‑ Available only in the USA

Model No.

Max. Gas Input Min. Gas Input Max. Gas FlowStart‑Up Amperage

Natural Gas/ Propane Natural Gas Propane CFH m3/hr

Btu/hr kW Btu/hr kW Btu/hr kW Natural Gas Propane Natural Gas Propane 12V 120V 208V 240V 380V 480V 600V

H6x6 1,500 0�44 500 0�147 375 0�11 1�5 0�6 0�0425 0�017 7�1 0�7 – 0�4 – – –

H6x12 3,000 0�879 1,000 0�293 750 0�22 3 1�2 0�085 0�034 7�1 0�7 – 0�4 – – –

H6x24 6,000 1�758 2,000 0�586 1,500 0�44 6 2�4 0�1699 0�068 15 2�1 1�2 1 – – –

H8x8 2,667 0�782 900 0�264 700 0�205 2�7 1�1 0�0755 0�0302 7�1 0�7 – 0�4 – – –

H10x12 5,000 1�465 1,700 0�498 1,250 0�366 5 2 0�1416 0�0566 15 2�1 1�2 1 – – –

H12x12 6,000 1�758 2,000 0�586 1,500 0�44 6 2�4 0�1699 0�068 15 2�1 1�2 1 – – –

H12X24 12,000 3�517 4,000 1�172 3,000 0�879 12 4�8 0�3398 0�1359 30 4�2 2�4 2�1 – 1�5 0�9

H12x36 18,000 5�275 6,000 1�758 4,500 1�319 18 7�2 0�5097 0�2039 – 5 2�9 2�5 1�6 1�3 1

H12x48 24,000 7�034 8,000 2�345 6,000 1�758 24 9�6 0�6796 0�2718 30 6�7 3�9 3�3 2�1 1�7 1�3

H12x60 30,000 8�792 10,000 2�931 7,500 2�198 30 12 0�8495 0�3398 45 10�4 6 5�2 3�3 2�6 2�1

H12x72 36,000 10�551 12,000 3�517 9,000 2�638 36 14�4 1�0194 0�4078 – 12�1 7 6 3�8 3 2�4

H18x24 18,000 5�275 6,000 1�758 4,500 1�319 18 7�2 0�5097 0�2039 30 4�2 2�4 2�1 – 1�5 –

H18x30 22,500 6�594 7,500 2�198 5,625 1�649 22�5 9 0�6371 0�2549 – – – – – 1�5 –

H18x36 27,000 7�913 9,000 2�638 6,750 1�978 27 10�8 0�7646 0�3058 – 10 5�8 5 3�2 2�5 2

H18x48 36,000 10�551 12,000 3�517 9,000 2�638 36 14�4 1�0194 0�4078 – 13�3 7�7 6�7 4�2 3�3 2�7

H18x60 45,000 13�188 15,000 4�396 11,250 3�297 45 18 1�2743 0�5097 ‑ 20�8 12 10�4 6�6 5�2 4�2

H18x72 54,000 15�826 18,000 5�275 13,500 3�956 54 21�6 1�5291 0�6116 ‑ 24�2 14 12�1 7�6 6 4�8

H24x24 24,000 7�034 8,000 2�345 6,000 1�758 24 9�6 0�6796 0�2718 30 4�2 2�4 2�1 ‑ 1�5 ‑

H24x30 30,000 8�792 10,000 2�931 7,500 2�198 30 12 0�8495 0�3398 30 4�2 2�4 2�1 ‑ 1�5 ‑

H24x36 36,000 10�551 12,000 3�517 9,000 2�638 36 14�4 1�0194 0�4078 ‑ 10 5�8 5 3�2 2�5 2

H24x48 48,000 14�067 16,000 4�689 12,000 3�517 48 19�2 1�3592 0�5437 ‑ 13�3 7�7 6�7 4�2 3�3 2�7

H24x60 60,000 17�584 20,000 5�861 15,000 4�396 60 24 1�699 0�6796 ‑ 20�8 12 10�4 6�6 5�2 4�2

H24x72 72,000 21�101 24,000 7�034 18,000 5�275 72 28�8 2�0388 0�8155 ‑ 24�2 14 12�1 7�6 6 4�8

Table 3 – MKII Series (CSA and FM)

M E M O R A N D U M TO: To whom it may concern FROM: Jarek Szynkarczuk, Ph.D. RE: Emission Statement on CCI Thermal Catalytic Heaters (Explosion-Proof Catalytic Heaters) ____________________________________________________________________________

CCI Thermal Technologies Inc.'s Cata-Dyne™ Heater The Cata-Dyne™ emitter is a flameless, gas-fired appliance that converts natural gas or propane into usable infrared energy. This energy, emitted as infrared radiant heat, is readily absorbed by most materials.

Reactants and combustion byproduct information: For every 1 SCFH (standard cubic foot per hour) of combusted natural gas, 10 SCFH of air will be consumed, and the following byproducts produced: - carbon dioxide (CO2) - 1 SCFH - water vapor (H2O) - 2 SCFH These numbers are multiplied depending on the BTU rating of your heater. For example, a heater rated at 10,000 BTU/H will consume 10 SCFH of natural gas and 100 SCFH of air, and will produce; CO2 -10 SCFH, H2O - 20 SCFH.

Please notice that improper usage of the heater may generate different emissions than those described above. If you require further information, please do not hesitate to call me at (780) 577-5578. Regards, Jarek Szynkarczuk, Ph.D. Manager, R&D

1

DESCRIPTIONThe 5100 Series Texsteam Chemical Injectors are single acting, positive displacement plunger-typepumps, powered by gas via a diaphragm with a spring return. Speed control is accomplished by regulating the exhaust gas discharge flow. Reversal isaccomplished by a direct spring- actuated switchingmechanism (rotary three-way valve). Volume is controlled by the speed of the pump and by the strokelength, either 1” or 1/3” lengths.

The 5100 Series is capable of pumping high pressureswith gas pressure as low as 8 psi and handling volumeoutput up to 30 gallons per day.

The pump is lightweight, compact and contains a minimum of working parts for easy maintenance. Eachfluid pump head is equipped with a stainless steelplunger, ball checks, ball check springs, top seat, topbushing, bottom bushing, adjustable VEE type packingand a priming valve. The packing yoke is equippedwith a drain to monitor for possible packing leaks.Because of the sealed bearings, the unit is oil-less.

APPLICATIONS• The introduction of de-emulsifiers, solvents,

corrosion inhibitors, de-salting agents and flocculants in oil country operation

• High pressure bearing lubrication

• Water treatment

• Blending processes in refining and process plants

• Injection of methanol in gas pipelines

• Hydrostatic testing

• Sampling

Series 5100 LPWt. 45 pounds

The 5100 Series performs accurately because (1) thehead is designed for high volumetric efficiency, (2) a positive trip mechanism assures fine control ofplunger stroke length, and (3) the speed is regulatedby controlling the exhaust gas discharge flow which creates a rapid fluid discharge with slow suction.

Microswitch Option Available

ACCESSORIES, OPTIONS, & VOLUME

Sour Gas Trim - Pump modelsL and LP are furnished withsour gas trim as standard.Models H and HP are availablefor sour gas service specification.

TB-40 Regulator - for inlet gaspressure greater than 35 PSIand up to 1500 PSI

Alternate Parts - Teflon, Viton,or Fluorosilicone packing,hastelloy balls.

35

30

25

20

15

10

5

0 3 6 9 12 15 18 21 24 27 30

Maximum Recommended Speed Above1500 psi Injection Pressure3/16” Plunger 28 Strokes per Minute1/4” Plunger 26 Strokes per Minute3/8” Plunger 14 Strokes per Minute1/2” Plunger 14 Strokes per Minute

Model 5105 1/2” Plunger 1” Stroke

Model 5105 1/2” Plunger 1” Stroke

Model 5104 3/16” Plunger 1/3” Stroke

Model 5105 1/2” Plunger 1/3” Stroke

Model 5101 1/4” Plunger 1/3” StrokeModel 5104 3/16” Plunger 1” StrokeModel 5103 3/8” Plunger 1/3” StrokeModel 5101 1/4” Plunger 1” Stroke

Power End to Fluid End RatioPlunger Operating Ratio

Size Fluid/Gas1/16” 1200/11/4” 750/13/8” 300/11/2” 180/1

Maximum GPD = gallons per dayPlunger Discharge For Operation Off Air or Gas Pressure to 33 PSI Constant

Size Pressure Power Unit1

5100 Series (Standard Packaging) Model Number Maximum Volume3/16” 1500 PSI 5104 4.2 GPD1/4” 1500PSI 5101 7.5 GPD3/8” 1500PSI 5103 16.8 GPD1/2” 1500PSI 5105 32.0 GPD

3/16” 6000PSI 5104 2.8 GPD1/4” 6000PSI 5101 5.0 GPD3/8” 6000PSI 5103 12.0 GPD1/2” 3500PSI 5105 22.0 GPD

(High Pressure Packing) Model Number Maximum Volume

Stroke Per Minute (1” Max. Stroke Length)

Gallo

nsPe

rDay

1. Basic pump no tank, base, regulator, gauge (Shipping Weight: 45 lbs.)2. Furnished with 5 gallon stainless steel tank mounted on heavy galvanized steel base and equipped

with level gauge and suction line but no regulator or gauge (Shipping Weight: 60 lbs.)3. Furnished with regulator and gauge but no tank or base (Shipping Weight: 48 lbs.)4. Furnished with 5 gallon stainless steel tank mounted on heavy galvanized steel base and equipped

with level gauge, suction line, regulator and gauge (Shipping Weight: 62 lbs.)*Volumes shown for low pressure heads with standard packing are at zero PSIG discharge pressure.

**Volumes For high pressure head with hard packing are shown at 1500 PSIG discharge pressure.

2

GAS CONSUMPTION CHART (Standard Cubic Feet of Gas Required to Pump One Gallon)For inlet regulator sizing,

double the requirement indicated

1/2” Plunger 1” Stroke 5105 53 54 57 62 71 76 84 951/2” Plunger 1/3” Stroke 159 162 171 186 213 228 252 2853/8” Plunger 1” Stroke 5103 120 126 148 164 177 185 243 278 314 355 3743/8” Plunger 1/3” Stroke 360 378 444 492 531 555 729 834 942 1065 11221/4” Plunger 1” Stroke 5101 244 245 248 270 288 308 340 355 369 405 4971/4” Plunger 1/3” Stroke 732 735 744 810 864 924 1020 1065 1107 1215 14913/16” Plunger 1” Stroke 5104 457 458 462 469 476 530 545 555 560 575 5893/16” Plunger 1/3” Stroke 1371 1374 1386 1407 1428 1590 1635 1665 1680 1725 1776

Injection Press in PSI 100 200 500 1000 1500 2000 3000 3500 4000 5000 6000

3

INSTALLATION

IMPORTANT:Max. Gas Diaphragm Chamber Pressure 35 P.S.I.Oil thrust rod occasionally.

1. Remove pump from carton and inspect for possible damage in transit from factory. The cardboard carton was designed especially for this pump and offers ampleprotection for normal handling. If the pump has been damaged in transit, file claim with the carrier.

2. Loosen and remove the four thumb screws that hold the cover.

3. Oil the thrust rod.4. Select the stroke length desired, either full or short

according to your requirements. See the data chart,full stroke is 1“, and short stroke is equal to 1/3”.

5. Check plunger packing gland to make sure packingis 1/4 turn past finger tight.

6. Install the priming valve TA-1497 in its position on the pump head.

7. Blow or clean line before hooking up air or gas line to inlet. On models 5100 LP and 5100 L the air or gas line (if it does not exceed 35 psi) is piped directly into the inlet TA-906. The inlet is a 1/4” female connection. Do not hook up the gas supply to the small valve. This is the gas exhaust, Gas supply should be constant pressure to assure even stroke speed.

If the gas supply pressure exceeds 35 psi or is erratic, somemeans of reducing the gas pressure to below 35 psi mustbe used. Model 5100 HP and 5100 H are equipped with apressure regulator and pressure gauge for reducing the gaspressure. The regulator supplied with the 5100 HP and 5100 Hcan be used up 400 psi. If the gas supply pressure exceeds400 psi, the customer should equip the pump with aTexsteam TB-40 regulator which has a maximum inlet pressure of 1500 psi.

8. Close gas exhaust valve. The gas exhaust is a 1/4” female pipe connection.

9. Hook up the fluid suction piping to the bottom bushing on the pump head. This is a 1/4” female pipe connection.Care should be exercised in that a suitable strainer should be installed in the suction line to trap foreign matter that might injure the plunger, plunger packing or interfere with the check valve operation.

10. On hooking up the fluid discharge line, the top connection on the pump head is the outlet and it is a 1/4” FNPT. The discharge line should be at least 5/16” tubing and a TA-676 line check should be installed at the point of injection in case the fluid discharge line ruptures or is broken. Careful observation of the flow direction during installation will eliminate the possibility of a ruptured fluid discharge line.

11. Turn the gas on and slowly open the gas exhaust valve.The pump will start automatically. Make certain the suction line is filled with fluid by opening the priming valve to check for fluid. After the pump discharges clear fluid without bubbles, close the priming valve for normal pumping operations. At this point make a visualcheck of the plunger drip and using the TA-315 gland wrench, slowly tighten the gland nut until leakage just stops. It may be necessary to readjust the packing the next day. A slight leak during break-in is beneficial. Sufficient time should be allowed to let the packing “seat in”. Packing should only be adjusted after pressure has been removed from the pump head. Neveradjust packing against pressure.

12. After the pump is in operation, replace the cover and thumb screws.

START UP AND OPERATIONAfter the pump has been installed, only a few minor adjustments are necessary for every day operation. Here are a few check points.

1. Check gas supply pressure.

2. Check speed control with the chart which will give you the volume the pump is injecting.

3. Check for excess leakage around the packing gland. If is not possible to stop excess leaking, replace the packing. If the plunger is badly scored, replace the plunger. Do not adjust packing against pressure.

4. Open the priming valve to check pump action.

5. Oil thrust rod occasionally.

4

MAINTENANCE

Should the pump run but fail to pump chemical,remove TB-736 bottom bushing and TA-1496 topbushing - inspect and clean balls and seats. Inspect fordamage and replace if necessary. Should pump stillnot pump chemical, remove TB-548 cover and checkto see if TA-290 Cotter Pin and TA-1828 StrokeAdjusting Pin are in place.

Check to see if chemical is getting to pump, unscrewTA-1497 priming valve stem. When chemical flowsfrom bleed hole, shut TA-1497 priming valve.

If the pump fails to operate after hooking up gas or airto TA-906 (inlet bushing); make sure the inlet pressuredoes not exceed 35 psi - excessive pressure couldtend to lock the pump; make sure the speed controlvalve (gas exhaust) is open; and make sure theplunger packing is not too tight. Use gland wrench TA-315 to adjust packing gland nut TA-6353, if necessary.

If pump stops and a constant flow of gas comes fromTA-1835 air vent, this means that the TC-2128diaphragm has ruptured.

TO REPLACE DIAPHRAGM

Remove TC-252 diaphragm cover. Remove lock nutand washer on end of TB-444. Do not allow TB-444thrust rod to turn when removing lock nut and washer.To prevent the rod from turning, remove TB-548 coverand hold the rod in position by inserting punch or driftpin into the “large” hole forward of the TA-6564Stirrup assembly. Replace burst diaphragm andreassemble.

TO REPLACE RETURN SPRING

Remove TC-252 diaphragm cover - remove lock nutand washer on end of TB-444 thrust rod. It is impor-tant that you do not allow TB-444 thrust rod to returnwhen moving lock nut and washer. To prevent the rodfrom turning remove TB-548 cover and hold the rod inposition by inserting punch or drift pin into the “large”hole forward of the TA-6564 stirrup assembly.

Pull TC-2128 diaphragm – TB-438 diaphragm plate - return spring TA-1821 can then be removed.Reassemble in reverse of above.

REPLACING TA-4147 VALVE DISC ASSEMBLY

If the pump has a heavy continuous leaking of gas – TA-4147 valve disc assembly probably needs

replacing. Disconnect power supply into TA-906 discretainer. Remove TA-906 Disc retainer from TA-441body - caution: care should be taken not to lose TA-77valve spring and TA-579 washer located directly underTA-906 disc retainer.

Before removing, note the position of the TA-4056valve disc, so that the disc is replaced to the sameposition as it was removed (see page 8). Lap the TA-4056 disc with a good valve grinding compoundbefore replacing.

When replacing TA-4056 valve disc be sure to alsoreplace the TA-4062 drive pin that was supplied whenyou ordered the disc assembly.

REMOVING TB-446 VALVE ASSEMBLY FROM PUMPHOUSING

Should it be necessary to remove TB-1631 flipper arm assembly from the pump housing, disconnect TB-1193 SS tubing, the power inlet from TA-906 discretainer and the gas exhaust line. Remove the fourP01-031100-3900 machine screws and four P52-031000-3900 lock washers. The TB-446 valve assembly can then be withdrawn from pump body.

The flipper arm bearing is an integral part of the TB-1631 flipper arm assembly and is press fit into the TB-441 body. A punch must be used to remove the flipper arm from the valve body. To do this the procedure under the heading, “Replacing TA-4147Valve Disc Assembly.” must be performed. When theseparts are removed the TB-1631 flipper arm assemblymay be punched from the body.

Upon reassembling the lower shaft of the TB-1627 flipper arm must fit into the TA-6563 flipper springadapter.

TO REPLACE THE FLIPPER SPRING

Follow the procedure as outlined under “Removing TB-446 Valve Assembly from Pump Housing.”

After removing the valve assembly, remove TB-548cover. At this point TA-6564 stirrup assembly may beturned upside down on the thrust rod - unscrew TA-1820 flipper spring. To reassemble follow the aboveprocedure in reverse.

5

LP & HP

1/4” FNPTGASINLET35 PSIG MAX.

NOTE- 1/4” FNPT GAS EXHAUSTThe backpressure on this exhaustport must be zero psig for maximumpump performance.

Furnishedon H&HPmodelsonly

GLANDWRENCH

1/4” FNPT

DRAIN

1/4” FNPT

PARTS LIST

1 TC-0252 1 Diaphragm Cover Cast Iron2 TD-0251 1 Housing Cast Iron

3** TC-2128 1 Molded Diaphragm Buna-N, Nylon4 P54-062000-0200 1 Washer Stl. Zinc Pl.5 TA-3320 1 Locknut Stl. Zinc Pl.

6** TA-1821 1 Return Spring C.S. Zinc Pl.7 TB-1193 1 Pilot Valve Line Assy. 303 S.S. Tubing8 P86-025075-0200 4 Wing Screws Stl. Zinc Pl.9 TB-0438 1 Diaphragm Plate Steel10 TB-0548 1 Cover Cast Iron11 TB-0444 1 Thrust Rod Steel12 TB-0446 1 Pilot Valve See Page 713 TA-1823 1 Bumper Plate Steel14 TB-0447 1 Rod Adapter Steel15 TA-0290 1 Pin Steel16 P01-037125-3900 8 Hex Hd. Cap Screw SS17 P25-037000-3900 8 Hex Nut SS18 P01-031100-3900 4 Hex Hd. Mach. Screw SS19 P52-031000-3900 4 Lockwasher SS

20* TA-1854 1 Pressure Gauge Range Brass Element0-35 psig

21* TA-1718 1 Regulator Aluminum/Brass22* TA-3324 1 Nipple Stl. Zinc Pl.

24 P52-037000-3900 1 Light Lockwasher SS25 TA-0075 1 Street El. C.S. Galv.26 P26-037000-0200 1 Hex. Nut Semifinish Stl. Zinc Pl.27 TA-1827 1 Bumper Plate Screw Steel28* TA-1828 1 Adjusting Pin Steel29* TA-1546 1 Gasket Buna-N30 TA-1835 1 Air Vent Brass31** TA-1820 1 Flipper Spring Steel32** TA-0746 3 Washer C.S. Zinc Pl.33 TA-6564 1 Stirrup Assembly Cast Iron & Steel34 1 Injector Head Head Assemblies

(See page 8 for part list)36** TA-0315 1 Gland Wrench Steel37** TA-6563 1 Spring Adapter (Bottom) Steel38** TA-0058 1 Gasket-Pilot Valve Fiber39 TA-2489 1 Gas Exhaust Valve Ni. Plated Brass40 TA-1829 1 Hex. Hd. Screw Steel41 P51-037000-0200 1 Internal Tooth Lockwasher Carbon Stl. Zinc Pl.42 TB-0471 1 Trip Stirrup Cast Iron43** TA-6563 1 Spring Adapter (Top) Steel44** TA-2355 1 Rollpin Steel45 TA-4015 1 Male Con. & Comp. Nut C.S. Cad. Pl.46 TA-4016 1 Elbow Con. & Comp. Nut C.S. Cad. Pl.

NOTES: * Furnished on H & HP models only** Recommended spare part*** Parts not mounted - packaged with unit

No.Item Part No. Reqd. Name Material

No.Item Part No. Reqd. Name Material

6

7-1/2” (5 gallon)8-3/4”(10 gallon)

16” (5 gal.)24” (10 gal.)

Bolt Hole c: 8-3/4” x 15-5/8” (5 gal.)12-1/4” x 22-1/8” (10 gal.)

1/4” FNPT GAS INLET35 PSIG MAX.

1/4” FNPTDISCHARGE

Optional Sight FeedAssembly (TB-38)

Furnished in lieu of Item 25 whenspecified mounted on tank

Diaphragm VentAssembly(TA-1835)

1 TA-0529 1 Gauge Stick 5 Gallon Stainless Steel1 TA-1742 1 Gauge Stick 10 Gallon Stainless Steel2 TA-0664 1 5 Gallon Tank 430 Stainless Steel2 TA-1539 1 10 Gallon Tank 304 Stainless Steel3 TA-3118 1 Connector Polypropylene4 TA-3116 1 Elbow Connector & Polypropylene

1 Compression Nut Assy.5* TB-0038 1 Sight Feed Assembly Optional and in lieu

1 of Item 256 TA-0950 1 Base, 5 Gal. Steel

TB-0758 1 Base, 10 Gal. Steel7 TA-3123 1 Suction Line 5/16”x22” Polypropylene9** TA-2459 1 Screen Stainless Steel10 TA-0792 1 Bushing Brass11 P53-031000-0200 4 Cut Washer C.S. Zinc Pl.12 P52-031000-3900 2 Lockwasher SS13 P25-037000-3900 2 Hex Nut SS15 P01-031100-3900 2 Hex Head Cap Screw SS16** P10-031125-0200 1 Pan Hd. Slotted Steel Zinc Pl.

Machine Screw17** TA-0098 1 Bowl Glass18 TA-0206 1 Strainer Monel19** TA-0104 1 Bowl Gasket Fiber20 TB-0039 1 Sight Feed Body Aluminum21 TA-0101 1 Shut off Assembly Brass25 TB-0871 1 Tank Gauge, 5 Gal. Assembly

TB-1285 1 Tank Gauge, 10 Gal. Assembly

* Optional. Will be supplied in lieu of Item 25, Tank Gauge** Recommended spare part*** Between pump and resevoir (same relative position as Item 13)

PARTS LISTNo.

Item Part No. Reqd. Name Material

7

PILOT VALVE ASSEMBLY

*TB-874 Repair Kit parts

1** TA-0200 Upper Valve Seat20 P25-025000-0200 Nut21 P55-025000-3900 Washer22 TA-3106 U-Bolt23 TA-3112 Handle Valve24* TA-3199 O-Ring, Viton25 TC-0393 Frame, Alum.26* TA-3100 Spring, 303 SS27* TA-3101 Flat Washer28* TA-3102 Gauge Glass29* TA-2184 O-Ring, Viton30 TA-3103 Strainer, 303 SS31 TA-3104 Retainer Nut, 303 SS32 TA-3115 Valve Body, 303 SS33 TA-3144 Stem Valve, 303 SS34 TA-3113 Spring, 316 SS35 TA-3328 Washer, 303 SS36 TA-3107 O-Ring, Viton37 TA-2163 O-Ring, Buna-N

Page No.No. Item Part No. Reqd. Name Material

5 20 TA-2847 1 Pressure Gauge S.S. Element0-60 psig

5 21 TA-2845 1 Regulator Aluminum250# max. inlet

Parts Required for Sour Gas ApplicationsFurnished Only When Ordering Pump

Models H and AP for Sour Gas Applications

** Recommended Spare Part

TB-871Tank Gauge

For 5 Gal. Tank

1 TB-0441 1 Body Cast IronValve Disc and 17-4 Ph SS

2 TA-4147 1 Drive- Pin Assy. Steel HardenedTA-4062 Pin Only

4* TA-0077 1 Valve Spring Stainless SteelElbow Connector

5 TA-4016 1 & Compression C.S. Zinc PlatedNut Assy.

6 P03-025037-0200 1 Hex Socket SteelCap Screw

7 P53-025000-0200 1 Washer C.S. 8 TA-0906 1 Disc Retainer C.S. Zinc Plated9 TB-1631 1 Flipper Arm & 17-4 SS Flipper Arm

Bearing Assy. with C.S. Bearing10* TA-0579 1 Washer Stainless Steel11 TA-0677 1 Outlet Body Brass12* TA-0391 1 Spring Stainless Steel13* TA-0054 1 Ball Stainless Steel14* TA-2093 1 O-Ring Viton

TA-0479 1 O-Ring Buna-N15 TA-0678 1 Inlet Body Brass16 TA-1296 1 Outlet Body Stainless Steel17 TA-1297 1 Inlet Body Stainless Steel18* TA-1574 1 Gasket Stainless Steel19 TA-2489 1 Valve Brass, Ni Plated

Brass Line Check(TA-676)

303 SS Line Check(TA-675)

Outside ViewBackside View

Pin Only(TA-4062)

*NOTE: To assemble,move lever arm to left asshown and align hole inpilot valve disc with holein pilot valve body.

PARTS LISTNo.

Item Part No. Reqd. Name Material

Item Part No. Name

PARTS LIST

TB-142

Section A-A

1/4”, 3/8”, 1/2”Heads

3/16”Head

1/4” FNPTDischarge

1/4” FNPTSuction

Head Assembly No. TB-1472 TB-0166 TB-0755 TB-0203 TB-0756 TB-0496 TB-07321 Body TC-2040 TC-0275 TC-0291 TC-0276 TC-0425 TC-0272 TB-03492* Plunger 17-4 PH TA-5643 TA-1312 TA-1312 TA-1745 TA-1745 TA-1876 TA-18763 Plunger Packing Gland 303-SST TA-5642 TA-1463 TA-1463 TA-0957 TA-0957 TA-1219 TA-12194* Plunger Packing Buna-N TA-3969 TA-1461 TA-1461 TA-1456 TA-1456 TA-0959 TA-0959

(see table below for maximum Buna-N Hard TA-3948 TA-2295 TA-2295 TA-1875 TA-1875 TA-1874 TA-1874 discharge pressures) Viton TA-3967 TA-4102 TA-4102 TA-4101 TA-4101 TA-4103 TA-4103

Viton Hard TA-6253 TA-6555 TA-6555 TA-6556 TA-6556 TA-6557 TA-6557Teflon TA-3966 TA-1642 TA-1642 TA-1234 TA-1234 TA-1012 TA-1012

Fluorosilicone TA-6574 TA-6257 TA-6257 TA-6258 TA-6258 TA-6259 TA-62595* O-Ring, Suction & Discharge Buna-N TA-0479 TA-0479 TA-0479 TA-0479 TA-0479 TA-0479 TA-0479

(included in items 8 & 14) Viton TA-2580 TA-2580 TA-2580 TA-2580 TA-2580 TA-2580 TA-2580Teflon TA-6159 TA-6159 TA-6159 TA-6159 TA-6159 TA-6159 TA-6159

Fluorosilicone TA-4113 TA-4113 TA-4113 TA-4113 TA-4113 TA-4113 TA-4113Kalrez TA-5037 TA-5037 TA-5037 TA-5037 TA-5037 TA-5037 TA-5037Aflas TA-5073 TA-5073 TA-5073 TA-5073 TA-5073 TA-5073 TA-5073

6 Top Bushing 302-SST TA-1496 TA-1496 TA-1496 TA-1496 TA-1496 TA-1496 TA-14967* Ball Check Spring 316-SST TA-0077 TA-0077 TA-0077 TA-0077 TA-0077 TA-0077 TA-0077

316-SST TA-0054 TA-0054 TA-0054 TA-0054 TA-0054 TA-0054 TA-00548* Large Top Ball 3/8” Hastelloy TA-0064 TA-0064 TA-0064 TA-0064 TA-0064 TA-0064 TA-00649* Top Seat-Assembly Buna-N "O” Ring 303-SST TB-0737 TB-0737 TB-0737 TB-0737 TB-0737 TB-0737 TB-0737

Top Seat-Assembly (Metal-to-Metal) 303-SST N/A TA-0806 TA-0806 TA-0806 TA-0806 TA-0806 TA-080610* Small Top Ball 1/4” 316-SST N/A TA-0126 TA-0126 TA-0126 TA-0126 TA-0126 TA-012611 Priming Valve 303-SST TA-5462 TA-1497 TA-1497 TA-1497 TA-1497 TA-1497 TA-149712 Nut, Plunger Packing Gland 303-SST TA-6353 TA-6353 TA-6353 TA-6353 TA-6353 TA-6353 TA-6353

Suction Ball 3/8” 316-SST TA-0054 TA-0054 TA-0054 TA-0054 TA-0054 TA-0054 TA-0054Hastelloy TA-0064 TA-0064 TA-0064 TA-0064 TA-0064 TA-0064 TA-0064

13 Suction Ball 1/2” (Use with TA-0771) 316-SST N/A TB-0053 TB-0053 TB-0053 TB-0053 TB-0053 TB-0053Metal-to Metal Bottom Seat onlyBottom Seat (w/Buna-N “O-Ring) 303-SST TB-1216 TB-0736 TB-0736 TB-0736 TB-0736 TB-0736 TB-0736

14* Bottom Seat Bushing Metal-to Metal 303-SST N/A TA-0771 TA-0771 TA-0771 TA-0771 TA-0771 TA-0771(Use w/TA-0053 1/2” Ball Only)

15 Gasket 304-SST TA-4394 N/A N/A N/A N/A N/A N/A18 Locknut Brass TA-0225 TA-0225 TA-0225 TA-0225 TA-0225 TA-0225 TA-0225

Plunger Size/Model # 3/16" 1/4" 3/8" 1/2"5104 5101 5103 5105

Item Material Material All Ductile All Ductile All Ductile All No. Specification Construction Stainless w/SS Stainless w/SS Stainless w/SS Stainless

Steel** Trim Steel Trim Steel Trim Steel

*Recommended Spare Parts** Ductile not Available

3/16” 1/4” 3/8” 1/2”Buna-N 3000 3000 3000 3000Buna Head 6000 6000 6000 3500Viton Hard 6000 6000 6000 3500Viton 3000 3000 3000 3000Teflon 3000 3000 3000 3000

Material Pressure psig

Plunger Packing - Max Discharge Pressure

INJECTOR HEADS

8

9

TA 7093 Microswitch Valve Kit

Item Part No. Name Material

A. P01-031050-0200 HHCS C.S. Zinc Pl.

B. P01-025050-0200 HHCS C.S. Zinc Pl.

C. P52-031000-0200 Lockwasher C.S. Zinc Pl.

D. TA 7091 Microswitch Aluminum

E. TA 7088 Microswitch AluminumMounting Plate

F. TA 7090-1 Thrust Collar Assembly

G. TA 7095 Bushing C.S. Zinc Pl.

H. TA 7096 Elbow C.S. Zinc Pl.

I. TA 7092 Tubing S.S.

J. TA 7097 Ferrule C.S. Zinc Pl.

K. TA 7098 Flareless Nut C.S. Zinc Pl.

5100 MICROSWITCH VALVE INSTALLATION

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J K

C

F

A

H

G

D E

INSTALLATION

1. If pump is installed in the field, shutoff gas flow to the pump.

2. Disconnect the gas supply pipe from the TA-0906 disc retainer gas inlet to the pump. Disconnect and remove the TB 1193 pilot valve line assembly as shown below.

3. Remove the four P01-031-3900 machine screws and four P52-031000-3900 lock washers and remove the switching valve assembly, TB 0446, from the pump housing.

B

Switching Valve Assembly RemovalTB 1193 Removal

10

9. Remove Bumper Plate Assembly, TA 1823, TA 0459, TA 3323, and TA 1827.

10. Install microswitch thrust rod collar assembly TA 7090-1. Ensure that the clamping bolt is on the opposite side of the thrust rod from where the microswitch will be installed. Place TA 7090-1 over the area where the stirrup assembly TA 6564 would normally attach to the thrust rod. Do not tighten the clamping bolt at this time.

11. Push the diaphragm TC 2128 back into position and reinstall the TC 0252 diaphragm cover.

12. Reinsert TA 1828 adjusting pin.

13. Install TA 7092 microswitch valve onto the TA 7088 mounting plate with the two P01-025050-0200 HHCS. Ensure the “TXT” tag is facing up.

14. With the microswitch installed in the mounting plate, ensure the lever arm is switched to the left position. Place the gasket, TA 0058 between the mounting plate and the housing, then attach the mounting plate to the pump housing, TD 0531 using the four HHCS, P01-031050-0200, with the four lock washers, P52-031000-0200. Ensure the microswitch valve extended shaft is between the forks on the TA 7090-1 assembly.

Port 1

Port 2

Port 3

Steps 4 through 8

Bumper Plate

Steps 10 through 12

Microswitch Assembly Installed

4. Remove the TB 0548 cover. 5. Remove adjusting pin, TA 1828.6. Remove TC 0252 diaphragm cover.7. Pull diaphragm TC 2128 and thrust rod

TB 0444 out. 8. Remove stirrup assembly TA 6564.

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16. Attach the 1/4 MNPT X 3/8 tubing 90° elbow, TA 7096, to Port 2 (center port).

17. Assemble the tubing using the ferrule, TA 7097, and flareless nut, TA 7098, then attach the tubing assembly, TA7092, to the elbow and to the pump head.

18. Tighten the clamping bolt on the thrust rod collar assembly.

19. Connect supply gas to Port 1 on the microswitch valve. Stroke the pump several times. You may need to adjust the location of the thrust rod collar to optimize operation of the pump.

20. Control the speed of the pump using the gas supply pressure and the speed control valve to achieve the desired stroke rate.

Min. gas pressure: 18 psi Max. gas pressure: 35 psi

Microswitch Valve Replacement1. Shutoff gas flow to the pump.2. Disconnect the gas supply pipe from Port 1 on the

microswitch valve.3. Disconnect and remove TA 7092 tubing assembly.4. Remove two bushings, TA 7095, from Ports 2 and

3 on the microswitch valve.5. Remove the TB 0548 cover.6. Remove the four P01-031-3900 machine screws

and four P52-031000-3900 lock washers. Remove the microswitch valve assembly from the pump housing.

7. Remove the old microswitch from the mounting plate and replace with the new microswitch.

8. Reinstall the mounting plate with microswitch valve and gasket using the four machine screws and lock washers. Ensure the microswitch valve extended shaft is between the forks of the TA 7090-1 assembly.

9. Reinstall the TB 0548 cover.10. Replace the TA 7095 bushings back into ports 2

and 3 as shown.

11. Reconnect the TA 7092 tubing assembly.12. Reconnect the gas supply line to the

microswitch valve.

Port 1

Port 2

Port 3

Speed Control Valve Installation

Steps 16 through 19

15. Attach the speed control valve, TA-2489 to the exhaust, Port 3 (left port).

Dresser, Inc.16240 Port Northwest DriveHouston, Texas 77041-2645

Phone: 832-590-2306 Fax: 713.849.2879www.dresser.com

Dresser Industrial Products Group

Series 51004.07

©2006 Dresser, Inc.Texsteam is a registered trademark of Dresser, Inc.

y = ‐2E‐15x4 + 1E‐10x3 ‐ 2E‐06x2 + 0.0171x + 107.54

0

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0 5000 10000 15000 20000 25000 30000

SCF requ

ired pe

r gallon of fluid injected

Pressure (kPa)

Texsteam 5100 Pump, 3/8" plunger, 1" stroke, Gas Consumption

3/8" full

Poly. (3/8" full)

Regulatory and Compliance Branch 12th Floor Baker Centre 10025 – 106 Street Edmonton AB T5J 1G4 Telephone 780-427-5200 www.alberta.ca

February 14, 2019 Hillary Yeung, B.A.Sc., P.Eng. North Shore Environmental Consultants Inc. 134-12143 40 Street SE Calgary, Alberta T2Z 4E6 RE: Protocol Deviation Request - Greenhouse Gas Emission Reductions from Pneumatic Devices for Peyto 2017 Aggregated Project for Methane Emission Reductions from Pneumatic Devices (Project ID# 3395-2492) Thank you for your request on February 5, 2019 to deviate from the gas composition requirements set forth in the Quantification Protocol for Greenhouse Gas Reductions from Pneumatic Devices. Your request relates to the following project under the Alberta Emissions Offset Registry (AEOR):

a) Peyto 2017 Aggregated Project for Methane Emission Reductions from Pneumatic Devices, Project ID 3395-2492

The request is to deviate from the protocol requirement to use annual gas analysis for carbon dioxide and methane composition. North Shore on behalf of Peyto has proposed to use biennial (every two years) gas analysis for well sites that are required to use biennial sampling as per Alberta Energy Regulator (AER) Directive 017. The Alberta Climate Change Office grants the request to use biennial gas composition for the wells that are required to use biennial sampling as per Directive 017. This deviation is specific to the Quantification Protocol for Greenhouse Gas Emission Reductions from Pneumatic Devices; it does not grant permission to deviate from any regulatory requirements including but not limited to AER Directive 017 or Directive 060. If you have any further questions please contact [email protected]. Sincerely, Amanda Bambrick, M.Sc., P.Ag. Acting Director, Emissions Inventory and Trading Alberta Climate Change Office

Scott MacDougall for Amanda Bambrick

Enclosure cc: Alberta Emission Offset Registry (file)