Facility Name:Targa Resources Corp. 420 Fort Worth Syncline GB
Facility Identifier:
Facility Reporting Year:2020
Facility Location:
Address: 811 Louisiana Suite 2100
City: Houston
State: TX
Postal Code: 77002

Facility Site Details:
CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):228,112.51
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:211130
Second Primary NAICS Code:

Parent Company Details:
Parent Company Name:TARGA RESOURCES CORP
Address:811 Louisiana Street, Suite 2100, Houston,  TX 77002
Percent Ownership Interest:100

Subpart W: Petroleum and Natural Gas Systems

Gas Information Details

Gas NameCarbon Dioxide
Gas Quantity175,333.663842 (Metric Tons)
Own Result?

Gas NameMethane
Gas Quantity2,107.556115 (Metric Tons)
Own Result?

Gas NameNitrous Oxide
Gas Quantity0.301835 (Metric Tons)
Own Result?


SubpartWSummaryDetails:
Industry Segment Number9
Industry Segment NameOnshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)175333.663842323
Total CO2e Emissions (mt CO2e)228112.513624717
Total Reported CH4 Emissions (mt CH4)2107.55611451441
Total Reported N2O Emissions (mt N2O)0.30183530044918


SubpartWSourceReportingFormRowDetails:
Source Reporting FormOnshore Production [98.236(aa)(1)]
Required for Selected Industry SegmentNo
Source Reporting FormFacility Overview [98.236(aa)(2-11)]
Required for Selected Industry SegmentYes
Source Reporting FormNatural Gas Pneumatic Devices [98.236(b)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Source Reporting FormNatural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Source Reporting FormAcid Gas Removal Units [98.236(d)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)5802.293376
Source Reporting FormDehydrators [98.236(e)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)68.7323775852224
Total Reported CH4 Emissions (mt CH4)2.578438237208
Total Reported N2O Emissions (mt N2O)0.00007
Source Reporting FormWell Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Source Reporting FormCompletions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormCompletions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormBlowdown Vent Stacks [98.236(i)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)87.1413210847518
Total Reported CH4 Emissions (mt CH4)721.950633860812
Source Reporting FormAtmospheric Storage Tanks [98.236(j)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)1.07636819136
Total Reported CH4 Emissions (mt CH4)3.9589373952
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormTransmission Storage Tanks [98.236(k)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormWell Testing [98.236(l)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormAssociated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormFlare Stacks [98.236(n)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormCentrifugal Compressors [98.236(o)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Source Reporting FormReciprocating Compressors [98.236(p)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)2.1621756
Total Reported CH4 Emissions (mt CH4)14.197248
Source Reporting FormEquipment Leaks Surveys and Population Counts [98.236(q,r)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)159.407894622398
Total Reported CH4 Emissions (mt CH4)1320.27753463603
Source Reporting FormOffshore Petroleum and Natural Gas Production [98.236(s)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Total Reported CH4 Emissions (mt CH4)0
Total Reported N2O Emissions (mt N2O)0
Source Reporting FormEnhanced Oil Recovery Injection Pumps [98.236(w)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Source Reporting FormEnhanced Oil Recovery Hydrocarbon Liquids [98.236(x)]
Required for Selected Industry SegmentNo
Total Reported CO2 Emissions (mt CO2)0
Source Reporting FormCombustion Equipment at Onshore Petroleum and Natural Gas Production Facilities, Onshore Petroleum and Natural Gas Gathering and Boosting Facilities, and Natural gas Distribution Facilities [98.236(z)]
Required for Selected Industry SegmentYes
Total Reported CO2 Emissions (mt CO2)169212.850329239
Total Reported CH4 Emissions (mt CH4)44.5933223851632
Total Reported N2O Emissions (mt N2O)0.30176825923


FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:
Select the basin associated with this facility [98.236(a)(9)]420 - Fort Worth Syncline
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]76810247.01
Quantity of gas transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(ii)]72311000
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]73684
Quantity of all hydrocarbon liquids transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iv)]73684


PneumaticDeviceVentingDetails:
mt CO20
mt CH40
Did the Facility have any continuous high-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?No
Did the Facility have any intermittent bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?No
Did the Facility have any continuous low-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


PneumaticDeviceTypesRowDetails:
Type of Pneumatic DeviceHigh-bleed Pneumatic Devices
Type of Pneumatic DeviceLow-Bleed Pneumatic Devices
Type of Pneumatic DeviceIntermittent Bleed Pneumatic Devices


NaturalGasDrivenPneumaticPumpsDetails:
mt CO20
mt CH40
Did the Facility have any natural gas driven pneumatic pumps subject to reporting under 98.232 [98.236(c)]?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


PneumaticPumpTypesRowDetails:
Type of Pneumatic PumpNatural Gas Driven Pneumatic Pumps
Total count of natural gas driven pneumatic pumps, Count [98.236(c)(1)]0
Average estimated number of hours in the calendar year that the natural gas driven pneumatic pumps were operated, T (hours) [98.236(c)(2)]8784
Total CO2 Emissions (mt CO2) [98.236(c)(3)]0
Total CH4 Emissions (mt CH4) [98.236(c)(4)]0


AcidGasRemovalUnitsDetails:
mt CO25802.293376
Did the Facility have any acid gas removal units that vent directly to the atmosphere, to a flare or engine, or to a sulfur recovery plant subject to reporting under 98.232 [98.236(d)]?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


AcidGasInfoRowDetails:
Unit ID or Name [98.236(d)(1)(i)]d. V-2 Amine Treater
County and State [98.236(d)(1)(vi)]MONTAGUE, TX
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]2466.432
Calculation Method Used (Select from list) [98.236(d)(1)(iii)]Calculation Methodology 2 [98.233(d)(2)]
Are any CO2 emissions from the acid gas removal unit recovered and transferred outside the facility? (Yes / No) [98.236(d)(1)(iv)]No
Total CO2 Emissions (mt CO2) [98.236(d)(1)(v)]5802.293376


AcidGasCalcMethod2EmissionsRowDetails:
Unit ID or Name [98.236(d)(1)(i)]d. V-2 Amine Treater
Annual average fraction of CO2 content in the vent from the acid gas removal unit, VolCO2 (volumetric fraction) [98.236(d)(2)(i)(A)]0.99
Annual volume of gas vented from the acid gas removal unit, Vs (actual or standard cubic feet) [98.236(d)(2)(i)(B)]111424000
Annual volume of gas vented reported on an Actual or Standard basis? [98.236]Standard
Temperature used to calculate volume of gas vented (°F) [98.236]60
Pressure used to calculate volume of gas vented (psi) [98.236]14.7


DehydratorsDetails:
mt CO268.7323775852224
mt CH42.578438237208
mt N2O0.00007
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs greater than or equal to 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?Yes
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs less than 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?No
Did the facility have any desiccant dehydrators subject to reporting under 98.232 [98.236(e)]?No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


SmallGlycolDehydrators:
Emissions vented to flare or regenerator firebox/fire tubes
Emissions that were not vented to a flare or regenerator firebox/fire tubes


DessicantDehydrators:
Emissions vented to flare or regenerator firebox/fire tubes
Emissions that were not vented to a flare or regenerator firebox/fire tubes


GlycolDehydratorsMoreThanSpecifiedValueRowDetails:
Unit ID or Name [98.236(e)(1)(i)]e. Bellevue DEHY EPN V-1
County and State [98.236(e)(1)(xviii)]CLAY, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]7.243674863
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]36.79
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.38
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]775
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]0.982533898368
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.034395052032
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Munson DEHY
County and State [98.236(e)(1)(xviii)]DENTON, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]34.53054372
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]59.81
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]2.83
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]102
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]1083
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.207
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.058
Unit ID or Name [98.236(e)(1)(i)]e. Cherryhomes DEHY
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]3.107043716
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]84.23
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.76
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]110
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]910
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]3.67504188264
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.0901870848
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Gibtown EPN V-1
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]2.424517986
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]39.54
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]4.78
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]3336
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]66
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]425
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]4.76842489056
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.18187978752
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00001
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Jaw EPN V-1
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]1.327460317
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]65.08
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.836
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]3024
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]881
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]0.999451491192
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.023158130688
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Perrin DEHY
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]5.333038251
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]77.18
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]3.49
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]10.11718553904
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.33094738944
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00001
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Tiger DEHY
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]5.186489071
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]43.47
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]7.5
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]446
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.317
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.088
Unit ID or Name [98.236(e)(1)(i)]e. Wizard Wells DEHY
County and State [98.236(e)(1)(xviii)]JACK, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]1.277748634
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]50.8
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.57
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]400
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.578123352
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.105258321
Unit ID or Name [98.236(e)(1)(i)]e. Mansfield EPN V-1
County and State [98.236(e)(1)(xviii)]MONTAGUE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]2.473554645
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]36.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.527
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]550
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.41465399
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.155495246
Unit ID or Name [98.236(e)(1)(i)]e. New Harp DEHY
County and State [98.236(e)(1)(xviii)]MONTAGUE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]30.0407377
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]46.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]4.528
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]91
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]988
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.15
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.052
Unit ID or Name [98.236(e)(1)(i)]e. Sandy Oak DEHY
County and State [98.236(e)(1)(xviii)]MONTAGUE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]10.4450929
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]46
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]4.528
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]91
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]997
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.124
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.054
Unit ID or Name [98.236(e)(1)(i)]e. Sunset DEHY
County and State [98.236(e)(1)(xviii)]MONTAGUE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]10.16681148
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]20.32
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]2.553
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]64
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]960
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]9.57232675584
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.28060452864
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00001
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Brannon DEHY EPN V-1
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]3.185836066
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]116.63
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]1.665
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]845
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]4.111000525152
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.168834945024
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Bridgeport EPN V-1
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]0.643819672
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]57.66
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]0.46
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]470
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]3.3129705729024
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.061031232
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Cottonwood DEHY
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]4.951731481
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]166.51
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Electric/Pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]5
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]2592
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]133
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]825
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.241
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.027
Unit ID or Name [98.236(e)(1)(i)]e. Decatur EPN V-1
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]0.974879121
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]41.87
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]1.026
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]2184
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]87
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]960
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]1.212469713
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.0390446784
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00000
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. East Chico DEHY
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]9.688221311
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]92.18
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Electric/Pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]1.698
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]113
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]14.774934584448
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.123471558144
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00001
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Greenwood EPN V-1
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]9.463598361
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]47.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]2.886
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]92
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]1000
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]10.96126039008
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]0.44413028352
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]0.00001
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]No
Unit ID or Name [98.236(e)(1)(i)]e. Sitz DEHY
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]20.15925137
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]110.01
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Electric/Pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]18
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]123
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]1020
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]1.386
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.181
Unit ID or Name [98.236(e)(1)(i)]e. Waggoner DEHY
County and State [98.236(e)(1)(xviii)]WISE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]56.41429508
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]79.08
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]Electric/Pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]11.1
Report type of absorbent used [98.236(e)(1)(vii)]Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]108
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]920
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]0.033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]0.749
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]0.827
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]0.08


BlowdownVentStacksDetails:
mt CO287.1413210847518
mt CH4721.950633860812
Did the facility have any blowdown vent stacks subject to reporting under 98.232 [98.236(i)]?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No
How were emissions determined? [98.236(i)]Calculated by equipment or event type


BlowdownEquipmentOrEventEmissionsRowDetails:
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]Compressors
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]472
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]8.80610075263072
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]72.9570075489295
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]Pig launchers and receivers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]162
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]8.6027564932565
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]71.2723358556418
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]Pipeline venting
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]16
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]69.7324638388645
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]577.72129045624


AtmosphericTanksDetails:
mt CO21.07636819136
mt CH43.9589373952
mt N2O0
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?Yes
Was Calculation Method 1 used to calculate emissions [(98.233(j)(1)]?No
Was Calculation Method 2 used to calculate emissions [(98.233(j)(2)]?Yes
Was Calculation Method 3 used to calculate emissions [(98.233(j)(3)]?Yes
If Calculation Method 1 or 2 were used, were any atmospheric tanks observed to have malfunctioning dump valves during the calendar year?No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


AtmosphericTanksCalculationMethodOneOrTwoSubBasinRowDetails:
County and State [98.236(j)(1)(i)]JACK, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]Calculation Methodology 2
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]65
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]10
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]65.3
Count of tanks that control emissions with vapor recovery systems [98.236(j)(1)(xii)(A)]6
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.3027
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.3027
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]0.0036
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]0.0036
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]13964
Total CO2 mass that was recovered (mt CO2) [98.236(j)(1)(xii)(B)]0.40192190208
Total CH4 mass that was recovered (mt CH4) [98.236(j)(1)(xii)(C)]12.33579313152
Annual CO2 emissions from tanks with vapor recovery systems (mt CO2) [98.236(j)(1)(xii)(D)]0
Annual CH4 emissions from tanks with vapor recovery systems (mt CH4) [98.236(j)(1)(xii)(E)]0
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]Yes
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]No
Count of atmospheric tanks [98.236(j)(1)(x)]6
County and State [98.236(j)(1)(i)]MONTAGUE, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]Calculation Methodology 2
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]65
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]19
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]53.4
Count of tanks that control emissions with vapor recovery systems [98.236(j)(1)(xii)(A)]2
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.1169
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.1169
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]0.0056
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]0.0056
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]5779
Total CO2 mass that was recovered (mt CO2) [98.236(j)(1)(xii)(B)]0.032513208784
Total CH4 mass that was recovered (mt CH4) [98.236(j)(1)(xii)(C)]0.247743233472
Annual CO2 emissions from tanks with vapor recovery systems (mt CO2) [98.236(j)(1)(xii)(D)]0
Annual CH4 emissions from tanks with vapor recovery systems (mt CH4) [98.236(j)(1)(xii)(E)]0
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]Yes
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]No
Count of atmospheric tanks [98.236(j)(1)(x)]2
County and State [98.236(j)(1)(i)]WISE, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]Calculation Methodology 2
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]65
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]18
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]67
Count of tanks that control emissions with vapor recovery systems [98.236(j)(1)(xii)(A)]4
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]2
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.346
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]0.346
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]0.0126
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]0.0126
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]0.19268819136
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]1.9314173952
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]28498
Total CO2 mass that was recovered (mt CO2) [98.236(j)(1)(xii)(B)]0.82722787056
Total CH4 mass that was recovered (mt CH4) [98.236(j)(1)(xii)(C)]8.2917499392
Annual CO2 emissions from tanks with vapor recovery systems (mt CO2) [98.236(j)(1)(xii)(D)]0
Annual CH4 emissions from tanks with vapor recovery systems (mt CH4) [98.236(j)(1)(xii)(E)]0
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]Yes
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]No
Count of atmospheric tanks [98.236(j)(1)(x)]6


AtmosphericTanksCalculationMethodThreeRowDetails:
Estimate of fraction of oil/condensate throughput sent to tanks in basin with flaring [98.236(j)(2)(i)(B)]0
Estimate of fraction of oil/condensate throughput sent to tanks with vapor recovery system control measures [98.236(j)(2)(i)(C)]0.727272727272727
Count of atmospheric tanks in basin [98.236(j)(2)(i)(D)]22
Total annual oil/condensate throughput that is sent to all atmospheric tanks (barrels per year) [98.236(j)(2)(i)(A)]25443


AtmosphericTanksCalcMethodThreeNoFlaringRowDetails:
County and State [98.236(j)(2)(ii)(A)]CLAY, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]2
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]0
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]0
County and State [98.236(j)(2)(ii)(A)]DENTON, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]2
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]0
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]0
County and State [98.236(j)(2)(ii)(A)]JACK, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]4
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]0.29456
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]0.67584
County and State [98.236(j)(2)(ii)(A)]MONTAGUE, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]6
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]0.29456
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]0.67584
County and State [98.236(j)(2)(ii)(A)]WISE, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]8
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]0.29456
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]0.67584


FlareStacksDetails:
mt CO20
mt CH40
mt N2O0
Did the facility have flare stacks subject to reporting under 98.232 [98.236(n)]?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No


UniqueFlareStacksRowDetails:
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Bellevue DEHY EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]17392.32
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.206
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.196
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Cherryhomes DEHY
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]60609.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.155
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.211
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Gibtown EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]82732.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.229
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.165
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Jaw EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]16299.36
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.148
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.213
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Perrin DEHY
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]163382.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.211
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.205
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Sunset DEHY
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]165139.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.177
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.221
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Brannon DEHY EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]75805.92
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.232
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.178
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Bridgeport EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]50859.36
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.125
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.201
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Decatur EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]21294
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.191
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.208
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. East Chico DEHY
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]229262.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.0561
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.319
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]e. Greenwood EPN V-1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]202910.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]0.228
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]0.193
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]0
CO2 emissions (mt CO2) [98.236(n)(9)]0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]0


CentrifugalCompressorsDetails:
mt CO20
mt CH40
Did the facility have any centrifugal compressors subject to reporting under 98.232 [98.236(o)]?No


ReciprocatingCompressorsDetails:
mt CO22.1621756
mt CH414.197248
Did the facility have any reciprocating compressors subject to reporting under 98.232 [98.236(p)]?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No
Total annual Reciprocating Compressor emissions CO2 Emissions (mt CO2) [98.236(p)(5)(ii)]2.1621756
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]14.197248
Count of Reciprocating Compressors [98.236(p)(5)(i)]78


OtherEmissionsFromEquipmentLeaksDetails:
mt CO2159.407894622398
mt CH41320.27753463603
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?Yes
Did this facility use population counts to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(r)]?Yes
Did the facility elect to comply with 98.236(q) according to 98.233(q)(1)(iv) for any components at the facility [per 98.236(q)(1)(iv)]?No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No
Number of complete equipment leak surveys performed during the calendar year [98.236(q)(1)(i)]12
Optical gas imaging instrument as specified in §60.18 [98.234(a)(1)]No
Method 21 [98.234(a)(2)]No
Infrared laser beam illuminated instrument [98.234(a)(3)]No
Acoustic leak detection device [98.234(a)(5)]No
Optical gas imaging instrument as specified in §60.5397a [98.234(a)(6)]Yes
Method 21 as specified in §60.5397a [98.234(a)(7)]No
Component count calculation method for all emission source types in Table R.1 other than gathering pipelines [98.236(r)(3)(i)]Component Count Method 1


OnshorePetroleumAndNaturalGasProductionAndGatheringAndBoostingRowDetails:
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]2
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]1765
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0.0171566472
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0.1421398272
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Pressure Relief Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Pump Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]2
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]2084
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0.02676881328
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0.22177494528
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Gas Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Pump
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Agitator Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Light Crude Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Pump
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Agitator Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0
Component Type [98.236(q)(2)(i)]Onshore Production or GB Components, Heavy Crude Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]0


LeaksCalculatedWithCountsFactorsRowDetails:
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gas Service - Valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]41334
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]76.286891033401
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]631.783353819341
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gas Service - Connectors
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]144472
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]37.4618928293914
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]310.247278025933
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gas Service - Open ended lines
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]2895
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]1.3688862861168
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]11.336673406464
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gas Service - Pressure relief valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]2864
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]8.43116198588928
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]69.8241562066944
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Flanges
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Connectors
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Open ended lines
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Pumps
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Light crude service - Other equipment leak sources (such as instruments, loading arms, stuffing boxes, compressor seals, dump lever arms, breather caps)
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Heavy crude service - Valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Heavy crude service - Flanges
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Heavy crude service - Connectors
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Heavy crude service - Open ended lines
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Heavy crude service - Other equipment leak sources (such as instruments, loading arms, stuffing boxes, compressor seals, dump lever arms, breather caps)
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gathering pipelines - Protected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]2187
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]15.62969240712
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]129.48927328512
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gathering pipelines - Unprotected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gathering pipelines - Plastic/composite gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]531
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]20.18544462
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]167.23288512
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]Gathering pipelines - Cast iron gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]0


MajorGasEquipmentTypeRowDetails:
Major Equipment Type [98.236(r)(3)(ii)]Wellhead
Equipment type present at facility? [98.236(r)(3)(ii)(A)]No
Major Equipment Type [98.236(r)(3)(ii)]Separators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]0
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]20
Major Equipment Type [98.236(r)(3)(ii)]Meters/piping
Equipment type present at facility? [98.236(r)(3)(ii)(A)]Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]0
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]2487
Major Equipment Type [98.236(r)(3)(ii)]Compressors
Equipment type present at facility? [98.236(r)(3)(ii)(A)]Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]0
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]70
Major Equipment Type [98.236(r)(3)(ii)]In-line heaters
Equipment type present at facility? [98.236(r)(3)(ii)(A)]Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]0
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]21
Major Equipment Type [98.236(r)(3)(ii)]Dehydrators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]0
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]18


CombustionEmissionsDetails:
mt CO2169212.850329239
mt CH444.5933223851632
mt N2O0.30176825923
Did the Facility have combustion units subject to reporting under 98.232?Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]No
Are there external fuel combustion units with a rated heat capacity less than or equal to 5 mmBtu/hr? [98.236(z)(1)(i)]Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity less than or equal to 1 mmBtu/hr? [98.236(z)(1)(i)]No
Total number of combustion units meeting 98.236(z)(1) descriptions21
Are there external fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr? [98.236(z)(2)(i)]Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr? [98.236(z)(2)(i)]No
Are there Internal fuel combustion units of any heat capacity that are compressor-drivers? [98.236(z)(2)(i)]Yes


LargeCombustionUnitEmissionsRowDetails:
Type of combustion unit [98.236(z)(2)(i)]Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]Natural gas (pipeline quality)
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]2421028
Unit of measure [98.236(z)(2)(iii)thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]129005.69959914
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]2.431317369
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]0.2431317369
Type of combustion unit [98.236(z)(2)(i)]Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]Field gas, process gas, and/or natural gas that is not of pipeline quality
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]586365.2233
Unit of measure [98.236(z)(2)(iii)thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]40207.1507300993
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]42.1620050161632
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]0.05863652233