Address: 811 Louisiana Suite 2100
City: Houston
State: TX
Postal Code: 77002

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):380,811.02
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:

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)	254567.694662679
Total CO2e Emissions (mt CO2e)	380811.019130743
Total Reported CH4 Emissions (mt CH4)	5044.90551913557
Total Reported N2O Emissions (mt N2O)	0.404988220385312

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)	12.9467273121792
Total Reported CH4 Emissions (mt CH4)	993.222136332288
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	3.467160256896
Total Reported CH4 Emissions (mt CH4)	265.98693510144
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	423.783001936944
Total Reported CH4 Emissions (mt CH4)	7.9844165858304
Total Reported N2O Emissions (mt N2O)	0.000153044385312
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0
Total Reported CH4 Emissions (mt CH4)	0
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
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
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
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.429928784563636
Total Reported CH4 Emissions (mt CH4)	32.9949908274997
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	8.504608122156
Total Reported CH4 Emissions (mt CH4)	35.672003223936
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	6.92274912
Total Reported CH4 Emissions (mt CH4)	0.036169728
Total Reported N2O Emissions (mt N2O)	0.00001
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	27.878
Total Reported CH4 Emissions (mt CH4)	230.4
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	3.16010280000001
Total Reported CH4 Emissions (mt CH4)	20.7498240000001
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)	40.8066105163424
Total Reported CH4 Emissions (mt CH4)	3131.02017722458
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
Total Reported CH4 Emissions (mt CH4)	0
Total Reported N2O Emissions (mt N2O)	0
Source Reporting Form	Enhanced Oil Recovery Injection Pumps [98.236(w)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	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
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)	254039.79577383
Total Reported CH4 Emissions (mt CH4)	326.838866112
Total Reported N2O Emissions (mt N2O)	0.4048242

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	360 - Anadarko Basin
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	96262000
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)]	90685000
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	163265
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)]	163265

PneumaticDeviceVentingDetails:

mt CO2	12.9467273121792
mt CH4	993.222136332288
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)]?	Yes
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	Low-Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	104
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	0.2672706696192
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	20.503957413888
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8784
Type of Pneumatic Device	Intermittent Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	508
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	12.67945664256
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	972.7181789184
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8784

NaturalGasDrivenPneumaticPumpsDetails:

mt CO2	3.467160256896
mt CH4	265.98693510144
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)]	141
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)]	3.467160256896
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	265.98693510144

AcidGasRemovalUnitsDetails:

mt CO2	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	423.783001936944
mt CH4	7.9844165858304
mt N2O	0.000153044385312
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. Aline DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.90080316
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.01
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)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.007943279696
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.051850616832
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. Amorita DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	15.60611988
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	17.987242699296
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.049309019136
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. Ashley DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.641019986
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.887256539424
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.051567280128
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. Byron DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12.76571801
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.5045713864704
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0401312710656
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. Cherokee DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.478043041
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2664
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	3.050900642736
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.15553327104
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. Driftwood DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.8325483
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	9.908616784896
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.50584034304
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. Mckee DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.039182952
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2688
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	3.161583645696
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.1607897088
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. Salt Fork DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.544381728
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.70257517056
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.05100060672
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. South Cherokee DEHY
County and State [98.236(e)(1)(xviii)]	ALFALFA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	13.86176148
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	11.594853648
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.3990325248
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. Bond DEHY
County and State [98.236(e)(1)(xviii)]	DEWEY, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	11.56997645
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2736
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	3.066149765664
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.15667167744
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. Dart DEHY
County and State [98.236(e)(1)(xviii)]	DEWEY, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.478808125
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.1820721535424
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0203472857088
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. Robinson Dehy
County and State [98.236(e)(1)(xviii)]	DEWEY, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	13.02493745
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	9.795657636864
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.50164088832
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. Carrier DEHY
County and State [98.236(e)(1)(xviii)]	GARFIELD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.259869148
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.095658959744
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.05197879296
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. Hillsdale DEHY
County and State [98.236(e)(1)(xviii)]	GARFIELD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.949711138
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.71837688384
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.05100060672
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. Kremlin DEHY
County and State [98.236(e)(1)(xviii)]	GARFIELD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.221551778
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.095658959744
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.05197879296
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. Waukomis DEHY
County and State [98.236(e)(1)(xviii)]	GARFIELD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.815870922
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.219661035776
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.52133953536
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. Cox DEHY
County and State [98.236(e)(1)(xviii)]	GRADY, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.074735925
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	93
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)]	0.91
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)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	320
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	3.0840411725856
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.127357318656
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. Clyde DEHY
County and State [98.236(e)(1)(xviii)]	GRANT, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.50815147
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.1119414032
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51567280128
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. County Line DEHY
County and State [98.236(e)(1)(xviii)]	GRANT, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.476063852
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2496
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	5.455821384
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0148502016
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. Smith DEHY
County and State [98.236(e)(1)(xviii)]	GRANT, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.761321739
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.17595682352
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51850616832
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. Bouse Junction DEHY
County and State [98.236(e)(1)(xviii)]	MAJOR, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.203128016
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	3024
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	3.4811601552
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.17752670208
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. Canton Dehy
County and State [98.236(e)(1)(xviii)]	MAJOR, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.091297123
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	9.960974976384
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.50868214272
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. Chaney Dell DEHY
County and State [98.236(e)(1)(xviii)]	MAJOR, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.102275938
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	5856
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	13.3223708699136
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.014087006208
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. Fisher H-2SV DEHY
County and State [98.236(e)(1)(xviii)]	MAJOR, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	13.29109536
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	9.795657636864
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.50164088832
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. Orienta DEHY
County and State [98.236(e)(1)(xviii)]	MAJOR, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.225174807
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.1119414032
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51567280128
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. Anderson Creek DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.385931419
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2496
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	5.47371287424
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.01493047296
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. Liberty DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.275440348
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.04801839056
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51283943424
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. Megan DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.136026853
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.0563812856
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51283943424
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. North Alva DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.072107131
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.1119414032
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.51567280128
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. Winchester DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.394709822
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	2496
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)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	5.47371287424
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.01493047296
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. Wolgamott DEHY
County and State [98.236(e)(1)(xviii)]	WOODS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.130160764
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.783480404592
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.051283943424
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. Bent Creek DEHY
County and State [98.236(e)(1)(xviii)]	WOODWARD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.872164131
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.295915643072
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.05254377984
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. Freedom DEHY
County and State [98.236(e)(1)(xviii)]	WOODWARD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.808317733
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	19.794103927488
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.02090451456
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. Quinlan DEHY
County and State [98.236(e)(1)(xviii)]	WOODWARD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.935000712
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	18.991032674256
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.051850616832
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. Walker DEHY
County and State [98.236(e)(1)(xviii)]	WOODWARD, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.256490102
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	106.04
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)]	3.5
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)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	950
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841
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)]	10.27605744288
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.522612864
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

BlowdownVentStacksDetails:

mt CO2	0.429928784563636
mt CH4	32.9949908274997
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)]	985
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.305385771816306
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	23.4369065336134
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)]	428
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.0500645950897462
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	3.84221972354158
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)]	2
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.0289192653061224
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	2.21941616326531
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)]	14
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.0455591523514615
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	3.49644840707946

AtmosphericTanksDetails:

mt CO2	8.504608122156
mt CH4	35.672003223936
mt N2O	0
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)]	ALFALFA, OK
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)]	18.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	55.5
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)]	0.5587
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.5587
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
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	13.349475177984
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)]	54582
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
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)]	12
County and State [98.236(j)(1)(i)]	DEWEY, OK
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)]	18.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	53.5
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.1415
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.1415
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0063
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0063
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0861770259
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	0.706517424
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)]	17337
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
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)]	4
County and State [98.236(j)(1)(i)]	GARFIELD, OK
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)]	18.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	67.3
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	9
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.2072
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.2072
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0461
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0461
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	2.802967449856
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	4.598565371904
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)]	38024
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
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)]	9
County and State [98.236(j)(1)(i)]	GRANT, OK
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)]	18.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	59.1
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	5
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.5307
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.5307
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
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	3.531447963648
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)]	18051
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
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)]	5
County and State [98.236(j)(1)(i)]	MAJOR, OK
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)]	18.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	58.3
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)]	0.6947
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6947
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0074
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0074
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0188236464
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	0.6450372864
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)]	4030
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
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)]	2

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
Count of atmospheric tanks in basin [98.236(j)(2)(i)(D)]	38
Total annual oil/condensate throughput that is sent to all atmospheric tanks (barrels per year) [98.236(j)(2)(i)(A)]	31241

AtmosphericTanksCalcMethodThreeNoFlaringRowDetails:

County and State [98.236(j)(2)(ii)(A)]	ALFALFA, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	7
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	1.03096
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	2.36544
County and State [98.236(j)(2)(ii)(A)]	DEWEY, OK
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)]	0.29456
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)]	GRANT, OK
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)]	0.29456
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)]	MAJOR, OK
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)]	0.88368
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	2.02752
County and State [98.236(j)(2)(ii)(A)]	WOODS, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	13
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	1.91464
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	4.39296
County and State [98.236(j)(2)(ii)(A)]	WOODWARD, OK
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)]	1.17824
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	2.70336

FlareStacksDetails:

mt CO2	6.92274912
mt CH4	0.036169728
mt N2O	0.00001
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)]	n. Chaney Dell 10 Flare
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)]	112000
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.841
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.004
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	6.92274912
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.036169728
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.00001
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	e. Aline 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)]	160747.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0431
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. Amorita 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)]	151963.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.338
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0425
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. Ashley 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)]	159868.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Byron 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)]	154598.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.96
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.338
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0426
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. Cherokee 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)]	48218.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0429
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. Driftwood 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)]	156355.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.337
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0428
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. Mckee 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)]	49996.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Salt Fork 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)]	158112
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0429
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. South Cherokee 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)]	153720
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.6
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.338
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0426
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. Bond 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)]	48427.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.337
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0427
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. Dart 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)]	157233.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.337
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0428
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. Robinson 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)]	154598.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.338
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0426
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. Carrier 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)]	161625.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0431
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. Hillsdale 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)]	158112
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0429
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. Kremlin 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)]	161625.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0431
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. Waukomis 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)]	161625.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0431
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. Cox 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)]	45588.96
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.291
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0381
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. Clyde 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)]	159868.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. County Line 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)]	46176
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Smith 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)]	160747.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Bouse Junction 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)]	55036.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Canton 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)]	157233.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.337
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0429
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. Chaney Dell 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)]	109507.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Fisher H-2SV 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)]	154598.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.338
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0426
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. Orienta 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)]	159868.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Anderson Creek 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)]	46425.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Liberty 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)]	158990.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Megan 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)]	158990.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. North Alva 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)]	159868.8
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Winchester 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)]	46425.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Wolgamott 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)]	158990.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Bent Creek 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)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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. Freedom 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)]	162504
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0431
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. Quinlan 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)]	160747.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.95
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.336
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.043
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. Walker 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)]	162504
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.5
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.335
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0432
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 CO2	27.878
mt CH4	230.4
Did the facility have any centrifugal compressors subject to reporting under 98.232 [98.236(o)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Total annual Centrifugal Compressor emissions CO2 Emissions (mt CO2) [98.236(o)(5)(ii)]	27.878
Total annual Centrifugal Compressor emissions CH4 Emissions (mt CH4) [98.236(o)(5)(iii)]	230.4
Number of Centrifugal Compressors with wet seal oil degassing vents, Count [98.236(o)(5)(i)]	1

ReciprocatingCompressorsDetails:

mt CO2	3.16010280000001
mt CH4	20.7498240000001
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)]	3.16010280000001
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	20.7498240000001
Count of Reciprocating Compressors [98.236(p)(5)(i)]	114

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	40.8066105163424
mt CH4	3131.02017722458
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)]	28
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)]	20
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1045.25
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0215522188
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	1.6540303584
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)]	2061
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.00177790104
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.13644545472
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)]	93
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1028.39784946237
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.02615972632
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	2.00763466176
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)]	9
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	386.333333333333
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.00204837024
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.15720268032
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)]	16
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1384.875
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.01724955984
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	1.32382173312
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)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1872
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0017724096
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.1360240128
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)]	65348
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)]	14.6191065987226
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	1121.52051535012
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)]	230797
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)]	7.25407836547968
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	556.504438346035
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)]	4609
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)]	0.26416274214528
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	20.2655294088192
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)]	4563
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)]	1.62821195791488
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	124.910034810163
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)]	3581
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)]	3.10207304928
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	238.06936283904
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)]	61
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)]	1.86520281696
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	143.14545116928
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)]	2605
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)]	12.0032148
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	921.1896864
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)]	25
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)]	4091
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)]	84
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)]	30
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)]	28

CombustionEmissionsDetails:

mt CO2	254039.79577383
mt CH4	326.838866112
mt N2O	0.4048242
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	38
Are there external fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr? [98.236(z)(2)(i)]	No
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)]	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)]	4048242
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	254039.79577383
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	326.838866112
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.4048242