Address: 811 Main St., Suite 3400
City: Houston
State: TX
Postal Code: 77002

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):307,116.1
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:2022-01-01
GHG Report End Date:2022-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:486210
Second Primary NAICS Code:

Parent Company Details:

Subpart W: Petroleum and Natural Gas Systems

SubpartWSummaryDetails:

Industry Segment Number	9
Industry Segment Name	Onshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)	284638.9
Total CO2e Emissions (mt CO2e)	307116.1
Total Reported CH4 Emissions (mt CH4)	892.71
Total Reported N2O Emissions (mt N2O)	0.535

SubpartWSourceReportingFormRowDetails:

Source Reporting Form	Onshore Production [98.236(aa)(1)]
Required for Selected Industry Segment	No
Source Reporting Form	Facility Overview [98.236(aa)(2-11)]
Required for Selected Industry Segment	Yes
Source Reporting Form	Natural Gas Pneumatic Devices [98.236(b)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	3.0
Total Reported CH4 Emissions (mt CH4)	418.16
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.6
Total Reported CH4 Emissions (mt CH4)	88.48
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	908.3
Total Reported CH4 Emissions (mt CH4)	7.82
Total Reported N2O Emissions (mt N2O)	0.001
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Completions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Completions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.2
Total Reported CH4 Emissions (mt CH4)	54.64
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	230.1
Total Reported CH4 Emissions (mt CH4)	5.73
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2844.5
Total Reported CH4 Emissions (mt CH4)	28.94
Total Reported N2O Emissions (mt N2O)	0.005
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1.5
Total Reported CH4 Emissions (mt CH4)	9.55
Source Reporting Form	Equipment Leaks Surveys and Population Counts [98.236(q,r)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1.6
Total Reported CH4 Emissions (mt CH4)	270.78
Source Reporting Form	Offshore Petroleum and Natural Gas Production [98.236(s)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Enhanced Oil Recovery Injection Pumps [98.236(w)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Enhanced Oil Recovery Hydrocarbon Liquids [98.236(x)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Combustion 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 Segment	Yes
Total Reported CO2 Emissions (mt CO2)	280649.0
Total Reported CH4 Emissions (mt CH4)	8.60
Total Reported N2O Emissions (mt N2O)	0.529

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	430 - Permian Basin
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	215112258.8692557
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)]	210552058.0855705
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	0
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)]	225877.71

PneumaticDeviceVentingDetails:

mt CO2	3.0
mt CH4	418.16
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)]?	Yes
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 Device	High-bleed Pneumatic Devices
Type of Pneumatic Device	Intermittent Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	235
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	2.97391
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	418.15588
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8760
Type of Pneumatic Device	Low-Bleed Pneumatic Devices

NaturalGasDrivenPneumaticPumpsDetails:

mt CO2	0.6
mt CH4	88.48
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 Pump	Natural Gas Driven Pneumatic Pumps
Total count of natural gas driven pneumatic pumps, Count [98.236(c)(1)]	50
Average estimated number of hours in the calendar year that the natural gas driven pneumatic pumps were operated, T (hours) [98.236(c)(2)]	8760
Total CO2 Emissions (mt CO2) [98.236(c)(3)]	0.59111
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	88.4827

AcidGasRemovalUnitsDetails:

mt CO2	0.0
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)]?	No

DehydratorsDetails:

mt CO2	908.3
mt CH4	7.82
mt N2O	0.001
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)]	Plant 1 Dehy-F176
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.01
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	59.97
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	5.89
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)]	0.77
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)]	8760
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)]	989.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00184
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.778
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
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)]	8.12771
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0052
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0
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)]	Orla Express Dehy-F176
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	55.34
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	59.97
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)]	2.79
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)]	8760
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)]	989.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00184
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.778
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
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)]	27.9027
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.01825
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0
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)]	Dehy-F176
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.96
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	57.44
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	3.66
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
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)]	1224
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	99.01
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1009.4
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00215
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.781
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
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)]	18.10653
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.00609
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00003
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)]	TEG Dehy. Unit #1-F399
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.12
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	60.78
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	4.55
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)]	0.0448
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)]	2880
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	94
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	764.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00129
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.746
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)]	3.57031
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.03232
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0
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)]	D1-F404
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	22.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	102.02
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)]	1.96
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)]	Yes
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)]	8760
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)]	1014.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00136
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.754
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)]	601.13322
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.14818
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00107
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)]	DEHY1-F552
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	33.12
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.01
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	3.2
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)]	14.3
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)]	6720
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	106
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1051.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00243
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.788
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
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)]	118.66561
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.09653
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00018
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)]	DEHY2-F552
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	33.25
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.01
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	3.03
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)]	16.8
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)]	6720
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	106
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1051.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00243
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.788
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
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)]	130.10462
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.10585
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00018
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)]	6-DHY-1-F553
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	22.57
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	74.97
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)]	2.21
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	108.47
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1009.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.000709
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.791
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)]	0.05169
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.82645
Unit ID or Name [98.236(e)(1)(i)]	6-DHY-1-F554
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	25.66
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	63.68
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	6.01
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)]	2.23
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	101.29
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	955.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00102
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.766
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)]	0.07593
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.81855
Unit ID or Name [98.236(e)(1)(i)]	6-DHY-1-F555
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	28.86
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	119.25
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)]	2.06
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	125.78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1007.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.000968
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.782
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)]	0.05642
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.69536
Unit ID or Name [98.236(e)(1)(i)]	7-DEHY-1-F556
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	39.03
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	97.12
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)]	2.32
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	116.62
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	957.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00118
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.762
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)]	0.07947
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.77483
Unit ID or Name [98.236(e)(1)(i)]	4-DHY-1-F558
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	24.93
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	76.41
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)]	2.06
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	109.01
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1004.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00482
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.771
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)]	0.31827
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.73909
Unit ID or Name [98.236(e)(1)(i)]	5-DHY-1-F559
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	18.87
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	74.22
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	6.57
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)]	2.12
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	108.25
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1014.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00106
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.773
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)]	0.07467
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.78277
Unit ID or Name [98.236(e)(1)(i)]	6-DHY-1-F560
County and State [98.236(e)(1)(xviii)]	EDDY, NM
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	24.87
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	88.16
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)]	2.21
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	113.98
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	991.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.000898
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.752
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)]	0.06157
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.77086

BlowdownVentStacksDetails:

mt CO2	0.2
mt CH4	54.64
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)]	Facility piping
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
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)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Emergency shutdowns
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
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)]	372
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.23642
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	38.10131
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)]	421
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.01014
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	16.53778

AtmosphericTanksDetails:

mt CO2	230.1
mt CH4	5.73
mt N2O	0.000
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)]?	Yes
Was Calculation Method 2 used to calculate emissions [(98.233(j)(2)]?	No
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)]	EDDY, NM
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	Promax
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	0
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	0
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	0
Count of tanks that control emissions with vapor recovery systems [98.236(j)(1)(xii)(A)]	6
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	7
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	12
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.0425962
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.1648888
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0023323
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.05724
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	2.79972
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	229.09512
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.07764
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.00024
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)]	139199.8
Total CO2 mass that was recovered (mt CO2) [98.236(j)(1)(xii)(B)]	0.7812
Total CH4 mass that was recovered (mt CH4) [98.236(j)(1)(xii)(C)]	18.83589
Annual CO2 emissions from tanks with vapor recovery systems (mt CO2) [98.236(j)(1)(xii)(D)]	0.05724
Annual CH4 emissions from tanks with vapor recovery systems (mt CH4) [98.236(j)(1)(xii)(E)]	2.79972
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	19

AtmosphericTanksCalculationMethodThreeRowDetails:

Estimate of fraction of oil/condensate throughput sent to tanks in basin with flaring [98.236(j)(2)(i)(B)]	0.048
Estimate of fraction of oil/condensate throughput sent to tanks with vapor recovery system control measures [98.236(j)(2)(i)(C)]	0
Count of atmospheric tanks in basin [98.236(j)(2)(i)(D)]	5
Total annual oil/condensate throughput that is sent to all atmospheric tanks (barrels per year) [98.236(j)(2)(i)(A)]	2299.5

AtmosphericTanksCalcMethodThreeNoFlaringRowDetails:

County and State [98.236(j)(2)(ii)(A)]	EDDY, NM
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)]	0.02424
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0.05568

AtmosphericTanksCalcMethodThreeWithFlaringRowDetails:

County and State [98.236(j)(2)(iii)(A)]	EDDY, NM
Count of tanks with flaring emission control measures [98.236(j)(2)(iii)(B)]	3
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(2)(iii)(C)]	0.89424
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(2)(iii)(D)]	0.00108
Annual N2O emissions from flaring (mt N2O) [98.236(j)(2)(iii)(E)]	0

FlareStacksDetails:

mt CO2	2844.5
mt CH4	28.94
mt N2O	0.005
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)]	WL2 Flare-F176
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)]	569400
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.95492
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00014
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	29.01564
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.52195
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)]	WL1/WLCS Flare-F176
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	Yes
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)]	7091700
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.95492
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00014
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	372.79116
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	2.60044
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.00068
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	ECD-1-F404
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)]	12336964.42016
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.95336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00014
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.00008
CO2 emissions (mt CO2) [98.236(n)(9)]	647.41247
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	4.51608
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.00126
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	FL-5100-F552
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)]	21056440
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.63491
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00126
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.0738
CO2 emissions (mt CO2) [98.236(n)(9)]	1681.26495
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	20.83752
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.00323
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	13-ECD-1-F553
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)]	440375.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.42356
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00106
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	14.87465
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.06189
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)]	14-ECD-1-F554
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)]	481369.89996
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.46669
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00059
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	17.81556
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.07637
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)]	14-ECD-F555
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)]	518299.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.40966
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00049
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	15.11583
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.06383
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)]	14-ECD-F556
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)]	608936.79996
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.33913
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00045
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	15.57684
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.06305
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)]	13-ECD-1-F558
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)]	427956.89996
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.50111
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00072
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	17.95935
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.07174
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)]	12-ECD-F559
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)]	426086.59996
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.43865
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00055
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	16.04189
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.06342
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)]	12-ECD-F560
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)]	537442.00004
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.34619
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00041
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	16.63992
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.06638
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0

CentrifugalCompressorsDetails:

mt CO2	0.0
mt CH4	0.00
Did the facility have any centrifugal compressors subject to reporting under 98.232 [98.236(o)]?	No

ReciprocatingCompressorsDetails:

mt CO2	1.5
mt CH4	9.55
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)]	1.45343
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	9.55084
Count of Reciprocating Compressors [98.236(p)(5)(i)]	57

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	1.6
mt CH4	270.78
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)]?	Yes
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)]	46
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)]	70
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	8358
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.23367
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	44.90286
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)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2352
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.00061
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.14552
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)]	166
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	8443
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.13812
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	28.84808
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)]	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 - Pressure Relief Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	58
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	7660
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.12056
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	31.34519
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)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	8760
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.00164
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.53957
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)]	47
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1595
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.02249
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	4.99636

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)]	5043
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)]	0.58857
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	79.59084
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)]	18182
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)]	0.28531
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	40.21649
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)]	380
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)]	0.01342
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	1.5548
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)]	357
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)]	0.06401
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	8.96756
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)]	456.81
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)]	0.09772
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	28.15532
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)]	0
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)]	4.74
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)]	0.00842
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	1.52106
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)]	0
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 Western US [98.236(r)(3)(ii)(B)]	6
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 Western US [98.236(r)(3)(ii)(B)]	337
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 Western US [98.236(r)(3)(ii)(B)]	1
Major Equipment Type [98.236(r)(3)(ii)]	In-line heaters
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
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 Western US [98.236(r)(3)(ii)(B)]	2

CombustionEmissionsDetails:

mt CO2	280649.0
mt CH4	8.60
mt N2O	0.529
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) descriptions	17
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)]	Yes
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)]	External fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	0
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	0
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	0
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0
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 and/or process gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	46488.49
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	3397.51645
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	3.37441
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.00615
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
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	4101159.03
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	272416.50683
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	5.13424
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.51332
Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	71613.35
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	4835.02389
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	0.09113
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.0091