carb opgee v2 launch v6 - california air resources board · pdf fileupstream modeling goals...

Download CARB OPGEE v2 Launch V6 - California Air Resources Board · PDF fileUpstream modeling goals Five goals of the upstream modeling effort 1. Build a rigorous, engineering-based model

If you can't read please download the document

Upload: ngolien

Post on 06-Feb-2018

215 views

Category:

Documents


0 download

TRANSCRIPT

  • OPGEE v2.0aOil Production Greenhouse Gas Emissions Estimator

    Kourosh Vafi,1 MohammadS.Masnadi,1 JacobEnglander,1VinayTripathi1,AdamR.Brandt,1SylviaSleep,3 DianaPacheco,2 AndreaOrellana,2 ZainabDashnadi,3 JouleBergerson,3 Heather

    MacLean2

    1 DepartmentofEnergyResourcesEngineering,StanfordUniversity2 DepartmentofCivilandEnvironmentalEngineering,UniversityofToronto3 DepartmentofChemicalandPetroleumEngineering,UniversityofCalgary

    Photos:Brandt(2006-2011)

  • Impacts from crude oil productionGoal: Improve modeling, extend capabilities

    We want to improve the modeling of unconventional oil resources Heavy oil and oil sands Tight oil via horizontal drilling and HF CO2 EOR

    Include features and capabilities that are not modeled in old version of OPGEE Crude oil mining and upgrading Drilling and fracturing modeling CO2 storage and recycling

    Source: Huffington post

    Source: National Geographic

    Introduction

  • ExampleLCAmodel- gasoline

    Exploration and field development

    Oil production

    Separation/reinjection

    Crude transport

    Crude refining

    Product transport

    Product consumption

    Upstream Refining Consumption

    Well-to-tank------------------------------------>

    Well-to-wheels---------------------------------------------------------------->

    Source:El-Houjeiri etal.2014

  • OPGEEmodelintroduction

    Source:El-HoujeiriandBrandt(2012a,2012b)

    El-Houjeiriand

    BrandtO

    PGEE

    v1.1D

    ocumentation

    64

    Scrubber

    Contactor

    350 psi Lean amine

    Qamine [gpm]

    Power BHPCP [hp]

    Power BHPF [hp]

    Power BHPBP [hp]

    Power BHPF [hp]

    Acid gases QCO2 + QH2S [MMscf]

    Sweet gas

    Charcoal filter

    Amine cooler

    Charge pump

    Booster pump

    Heat exchanger

    Reflux condenser

    Reflux pump

    Reflux accum.

    Power BHPRP [hp]

    Power HR[MMscf/d]

    Still

    Solid filter

    Flash tank Low pressure

    Flashed gas

    Qg [MMscf/d] Reboiler

    Figure 3.12: Amine simple process flow diagram [47, p. 112].

    OilProductionGreenhousegasEmissionsEstimator(OPGEE)

    Modelsemissionsgivenfieldparametersandtechnologies

    Thefirst open-sourceGHGtoolforoilandgasoperations

    Anyonecandownload,use,modify,explore

    Documentation(>200pp.)withallsourcesdefined

  • Upstream modeling goalsFive goals of the upstream modeling effort

    1. Build a rigorous, engineering-based model of GHG emissions from oil production operations

    2. Use disaggregated data for accuracy and flexibility

    3. Use public data where possible

    4. Document sources for all equations, parameters, assumptions

    5. Maintain model as free to access, use, and modify by any interested party

    OPGEEmodelinggoals

  • 1. Oilsandsminingandupgrading2. Drillingandhydraulicfracturing3. CO2 enhancedoilrecovery

    Improvementsandaddedfeatures

  • Upstream modeling goalsGoal: to integrate oil sands production and upgrading more directly into the OPGEE model

    Oil sands mining is included in production and extraction worksheet Oil sands upgrading is included in "surface processing worksheet

    Use data from a variety of sources Alberta Energy Regulator (AER) reported energy use COSIA (Canadas Oil Sands Innovation Alliance) default

    templates for mining and in situ operations AEMERA (Alberta Environmental Monitoring, Evaluation, and

    Reporting Agency) data on fugitive emissions

    Addedfeature:Oilsandsminingandupgr.

  • Upstream modeling goalsStand alone mining operations

    Stand alone mines do not upgrade on site but sell diluted bitumen

    Use more modern paraffinic froth treatment (PFT) technology

    Somewhat less energy intensive, but lack benefits of integrating upgrading on site

    Oilsandsmining:StandaloneEl-Houjeiri and Brandt OPGEE v2.0a Documentation 71

    Raw ore in

    Electricityimportsand exportsMWh/d

    Natural gasimportsmscf/d

    DilutedBitumenbbl/d

    DieselimportsmBtu/d

    Mine

    Diluentimportsbbl/d

    Figure 4.13: Non-integrated bitumen mining operation

    quantity of diesel fuel consumed can then be converted into an energy consump-tion rate:

    EMNdi = QMNdi LHVdi (4.47)

    where LHVdi is the lower heating value of diesel fuel [mBtu LHV/gallon]. Thisquantity can then be gathered on the Energy Consumption gathering sheet andused to compute emissions on the GHG Emissions gathering sheet.

    Similar quantities are computed for all main inputs to non-integrated miningoperations by using intensities of electricity use (IMNel ) and natural gas (I

    MNng ). For

    the case of integrated mining and upgrading operations, the relevant intensities fordiesel, electricity, and natural gas are similarly named (IMIdi , I

    MIel , and I

    MIng respec-

    tively). Recall via convention above that consumption of coke or refinery processgas is computed as part of upgrading operations in Section 5.3.

    After these mine-type-specific calculations are performed, the overall consump-tion due to mining is then computed using binary variables from the Active Fieldsheet. For the case of diesel energy consumption:

    Edi = yMNEMNdi + yMI EMIdi (4.48)

    where yMN and yMI represent binary variables for mining-non-integrated and mining-integrated, respectively.

    Miningflowdiagram(StandAlone)

  • Upstream modeling goalsIntegrated mining and upgrading operations

    Oil sands mining integrated with upgraders to allow heat recovery for use at mine

    Benefits due to reduced natural gas requirements subtracted from mine use

    Oilsandsmining:Integratedwithupgrader

    El-Houjeiri and Brandt OPGEE v2.0a Documentation 72

    UpgraderRaw ore in SCO out

    mBtu/d

    Electricity importsand exportsMWh/d

    bbl/d

    Natural gas importsmscf/d

    Coke consumed

    Heat recovery (mBtu/d)

    Coke exportedt/d

    mscf/dProcess gas exports

    MineBitumen

    bbl/d

    (Computed in upgrader calculations)

    Internal consumption flowstreated in upgrader calcs.

    Process gas consumed

    (Computed in upgrader calculations)

    Distillate fuel (diesel)mBtu/d

    Diesel importsmBtu/d

    Figure 4.14: Upgrader-integrated bitumen mining operation

  • Upstream modeling goalsAddedfeature:Oilsandsminingandupgr.El-Houjeiri and Brandt OPGEE v2.0a Documentation 67

    78

    107

    55

    43

    144

    3

    103

    45 4953

    74

    101

    4

    120

    0

    20

    40

    60

    80

    100

    120

    140

    160

    Suncor (1967)

    Syncrude -Mildred lake

    (1978)

    Syncrude -Aurora (2001)

    CNRL -Horizon (2008)

    Shell -Muskeg

    River (2002)

    Shell -Jackpine (2010)

    Imperial -Kearl Lake

    (2013)

    Nat

    ural

    Gas

    Con

    sum

    ptio

    n (m

    3 /m3

    bit)

    Project Name (Startup Year)

    2014 IntensityIntensity over Project Life

    NFT PFT

    COSIA range: 67-118

    COSIA range: 54-76

    Figure 4.11: Natural gas use in mining operations

    Table 4.13: Non-integrated PFT mining energy intensities

    Fuel OPGEEvalue

    AER PWavg.

    COSIAavg.

    COSIArange

    Notes

    Natural gas 85 85 93 67 118Electricity cons. 125 125 114 99 130Electricity gen. 77 77 114 96 132Frac. elect. gen. onsite 0.6 0.6 1.0 1.0 1.0Diesel 12.5 - 12.5 9 16 aDiluent 25.4% 25.4% - -a COSIA Mine Template ranges presented for low (9%) and high (12%) grade ore.

    pine, and Imperial Kearl). Volumetric blending rates over all months aver-aged 25.4% diluent in dilbit. The range over 2014 was from 24.3% to 26.5%Although Kearl dilutes bitumen with SCO (creating syn-bit) the dilutionfraction was nearly identical to those of Muskeg River and Jackpine.

    Table 4.13 gives results as used in OPGEE, results for the AER production-weighted average, COSIA template average, and COSIA template range.

    Proposed modeling of integrated NFT mining operations The integrated mining opera-tion is illustrated in Figure 4.14. The net flows across the process boundary areroughly equivalent to the stand-alone mining operation, with some exceptions.First, large volumes of diluent are not used to reduce the viscosity of bitumen,as upgrading the bitumen to SCO renders it ready for pipeline transport. Also, twonew co-products can be exported from the system: process gas and coke. There-fore, emissions credits should be given for these fuels if they are exported. Lastly,new internal flows between upgrader and mine include heat recovered from up-

    El-Houjeiri and Brandt OPGEE v2.0a Documentation 68

    145

    323

    5

    52

    181

    60

    122102

    161

    47

    185

    105

    64

    152

    0

    50

    100

    150

    200

    250

    300

    350

    Suncor (1967) Syncrude -Mildred lake

    (1978)

    Syncrude -Aurora (2001)

    CNRL -Horizon (2008)

    Shell -Muskeg River

    (2002)

    Shell -Jackpine

    (2010)

    Imperial -Kearl Lake

    (2013)

    Elec

    trici

    ty C

    onsu

    mpt

    ion

    (kW

    h/m

    3bi

    t)

    Project Name (Startup Year)

    2014 IntensityIntensity over Project Life

    NFT PFT

    COSIA range: 99-130COSIA value:113

    Figure 4.12: Electricity use in mining operations

    grader operations that is used in mine ore separations, as well as upgrader productstreams (distillate fuels) that are consumed in mining trucks. New internal con-sumption at the upgrader can include coke and process gas.

    Due to sharing of waste heat at integrated mining and upgrading projects, someeff