GHG Summary Report

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):1,112,896.1
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:486210
Second Primary NAICS Code:

Parent Company Details:

Parent Company Name:ENABLE MIDSTREAM PARTNERS LP
Address:PO Box 24300 MC LS700, Oklahoma City, OK 73124
Percent Ownership Interest:100

Subpart W: Petroleum and Natural Gas Systems

Gas Information Details

Gas Name	Carbon Dioxide
Gas Quantity	918,105.2 (Metric Tons)
Own Result?

Gas Name	Methane
Gas Quantity	7,771.05 (Metric Tons)
Own Result?

Gas Name	Nitrous Oxide
Gas Quantity	1.727 (Metric Tons)
Own Result?

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)	918105.2
Total CO2e Emissions (mt CO2e)	1112896.0
Total Reported CH4 Emissions (mt CH4)	7771.05
Total Reported N2O Emissions (mt N2O)	1.727

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)	132.0
Total Reported CH4 Emissions (mt CH4)	4601.77
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1663.4
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	40606.7
Total Reported CH4 Emissions (mt CH4)	1057.74
Total Reported N2O Emissions (mt N2O)	0.077
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Completions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Completions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	23.3
Total Reported CH4 Emissions (mt CH4)	822.00
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2150.9
Total Reported CH4 Emissions (mt CH4)	94.17
Total Reported N2O Emissions (mt N2O)	0.004
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	9.0
Total Reported CH4 Emissions (mt CH4)	59.32
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)	33.0
Total Reported CH4 Emissions (mt CH4)	1119.58
Source Reporting Form	Offshore Petroleum and Natural Gas Production [98.236(s)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Enhanced Oil Recovery Injection Pumps [98.236(w)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Enhanced Oil Recovery Hydrocarbon Liquids [98.236(x)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Combustion Equipment at Onshore Petroleum and Natural Gas Production Facilities, Onshore Petroleum and Natural Gas Gathering and Boosting Facilities, and Natural gas Distribution Facilities [98.236(z)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	873486.9
Total Reported CH4 Emissions (mt CH4)	16.46
Total Reported N2O Emissions (mt N2O)	1.646

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)]	428089377.0978335
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)]	428089377.0978335
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	569595.26
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)]	0

PneumaticDeviceVentingDetails:

mt CO2	132.0
mt CH4	4601.77
Did the Facility have any continuous high-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	Yes
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
Total Number, Countt [98.236(b)(1)(i)]	87
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	13.52355
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	481.41825
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)]	1926
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	110.490571
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	3848.11741
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	Low-Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	1323
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	7.93809
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	272.234035
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	0.0
mt CH4	0.00
Did the Facility have any natural gas driven pneumatic pumps subject to reporting under 98.232 [98.236(c)]?	No

PneumaticPumpTypesRowDetails:

Type of Pneumatic Pump

Natural Gas Driven Pneumatic Pumps

AcidGasRemovalUnitsDetails:

mt CO2	1663.4
Did the Facility have any acid gas removal units that vent directly to the atmosphere, to a flare or engine, or to a sulfur recovery plant subject to reporting under 98.232 [98.236(d)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

AcidGasInfoRowDetails:

Unit ID or Name [98.236(d)(1)(i)]	12549-AGR 1
County and State [98.236(d)(1)(vi)]	DEWEY, OK
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	755.55
Calculation Method Used (Select from list) [98.236(d)(1)(iii)]	Calculation Methodology 4 [98.233(d)(4)]
Are any CO2 emissions from the acid gas removal unit recovered and transferred outside the facility? (Yes / No) [98.236(d)(1)(iv)]	No
Total CO2 Emissions (mt CO2) [98.236(d)(1)(v)]	1663.353793

AcidGasCalcMethod4EmissionsRowDetails:

Unit ID or Name [98.236(d)(1)(i)]	12549-AGR 1
Name of simulation software package used [98.236(d)(2)(iii)(A)]	Amincalc 4.0
Natural gas feed temperature (°F) [98.236(d)(2)(iii)(B)]	78
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	828
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	1437.499908
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	4.3339
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	0.155
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	8760
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	80.233
Solvent pressure (psi) [98.236(d)(2)(iii)(I)]	850
Solvent temperature (°F) [98.236(d)(2)(iii)(J)]	90
Solvent circulation rate (gallons per minute) [98.236(d)(2)(iii)(K)]	30
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.67

DehydratorsDetails:

mt CO2	40606.7
mt CH4	1057.74
mt N2O	0.077
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)]	12682-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	86.83
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8304
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	102
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	640
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009714
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.904825
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)]	137.098667
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.113155
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000286
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)]	14695-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.87
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	54.1
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8688
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	910
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009265
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.931479
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)]	6.744358
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.108766
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000014
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	9.733802
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	156.844258
Unit ID or Name [98.236(e)(1)(i)]	14834-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	44.41
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01786
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.923695
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)]	3.525417
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.055929
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000007
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	7.748265
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	63.575507
Unit ID or Name [98.236(e)(1)(i)]	14714-Dehy 1 - Unit
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)]	31.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	102.94
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)]	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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	122
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1055
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007001
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.664616
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)]	1786.48234
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	14.819081
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.002725
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)]	14608-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	19.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	34.56
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	84
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1070
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007562
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.959772
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)]	558.167472
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.931731
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001265
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)]	14647-Dehy 1 - Unit
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)]	7.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	53.39
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006481
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.716822
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)]	681.600459
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.412783
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001093
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)]	14670-Dehy 1 - Unit
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)]	15.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.53
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)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	101
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	840
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007484
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.861729
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)]	759.143609
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.477415
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001486
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)]	14646-Dehy 1 - Unit
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)]	30.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	50.29
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006615
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.746901
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)]	643.045053
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.590797
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001078
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)]	14507-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	16.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	37.05
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	6240
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	84
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	970
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009911
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9525
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)]	375.036331
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.517798
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000836
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)]	14506-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.88
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)]	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)]	7248
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	970
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009369
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.941099
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)]	799.187416
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	13.501816
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001754
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)]	14587-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	14.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	39.62
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	6336
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)]	930
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006301
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.87904
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)]	450.835798
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.29801
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000876
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)]	14586-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	33.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.61
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	84
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	995
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005783
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.907946
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)]	637.138311
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.648168
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001298
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)]	14607-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	22
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	30.45
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1080
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007364
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.948243
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)]	591.040025
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.160907
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00131
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)]	14606-Dehy 1 - Unit
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)]	3.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	26.55
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	927
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008921
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.814731
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)]	741.756458
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.874141
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001331
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)]	14146-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	19.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	44.56
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	790
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004551
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.760251
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)]	666.979721
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.984795
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001123
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)]	14106-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	58.58
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	851
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004263
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.779153
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)]	301.029383
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.192966
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000501
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)]	14047-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	19.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	47.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	810
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006943
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.938189
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)]	448.494643
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.496881
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000977
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)]	14046-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	58.75
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	851
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004303
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.812526
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)]	265.240963
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.104922
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000467
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)]	13967-Dehy 1 - Unit
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)]	9.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	67.38
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)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	830
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.014901
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.893108
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)]	744.677658
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.889734
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00149
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)]	13987-Dehy 1 - Unit
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)]	5.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	79.44
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)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	103
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	745
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00411
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.902142
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)]	641.364514
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.490142
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001285
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)]	14266-Dehy 1 - Unit
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)]	27.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	56.49
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009743
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.845267
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)]	618.828553
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.120585
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001174
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)]	13968-Dehy 1 - Unit
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)]	18.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	72.34
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	102
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	815
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006881
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.848184
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)]	549.127141
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.242732
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001044
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)]	13905-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	25.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	46.53
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	91
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	954
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005999
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.904148
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)]	588.992466
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.820845
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001193
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)]	13904-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	41.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	59.27
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)]	3.88
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)]	7464
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	800
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0100887
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.958289
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)]	498.987154
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.707485
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001111
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)]	14366-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	23.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	90.73
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)]	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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	116
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1010
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006581
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.883997
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)]	1110.63365
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	15.736416
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.002176
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)]	14226-Dehy 1 - Unit
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)]	11.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	56.22
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	873
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008471
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85522
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)]	622.475739
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.254322
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001179
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)]	14166-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	33.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	49.17
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	7248
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	92
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	917
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.010088
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.935188
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)]	423.846245
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.062168
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000923
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)]	13946-Dehy 1 - Unit
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)]	40.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.59
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	840
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00728
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.813016
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)]	640.756612
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.715709
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00116
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)]	13874-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	37.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.46
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	86
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007883
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.957822
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)]	476.6830844
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.4093131
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0010483
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)]	13873-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	31.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	63.06
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)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009703
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.932341
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)]	718.355457
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	11.696626
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001533
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)]	13803-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	61
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8712
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	101
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	990
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00673
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.807021
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)]	698.278714
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.299902
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001257
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)]	13787-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.57
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	60.52
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	820
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008103
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.801415
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)]	593.372652
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.997703
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001067
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)]	13782-Dehy 1 - Unit
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)]	42.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	83.21
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	107
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	810
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007432
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.662685
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)]	777.095743
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.424456
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001185
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)]	13778-Dehy 1 - Unit
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)]	13.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	38.14
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	79
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005322
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.844008
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)]	569.670232
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.34406
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001063
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)]	13776-Dehy 1 - Unit
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)]	39.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	64.93
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)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	870
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007013
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.775127
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)]	691.781843
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.559512
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001192
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)]	12976-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	44.37
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8695
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	76
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	550
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011366
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.877668
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)]	143.958169
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.037892
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000283
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)]	12974-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.24
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	920
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012537
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.928642
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)]	202.356946
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.31904
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000437
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.564233
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.373903
Unit ID or Name [98.236(e)(1)(i)]	12948-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ELLIS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	52.19
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	93
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	890
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006542
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.747287
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)]	1040.901847
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.624378
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001738
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)]	12928-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.73
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	38.95
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)]	0.45
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)]	8567
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	75
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	620
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00769
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9493
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)]	28.410588
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.134593
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000062
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.191965
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.235487
Unit ID or Name [98.236(e)(1)(i)]	12927-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.84
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)]	0.45
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8602
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	91
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	570
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012649
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.911021
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.552917
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	15.33408
Unit ID or Name [98.236(e)(1)(i)]	12918-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	WASHITA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	15.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.56
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	875
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008321
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.824738
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	644.872029
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.021847
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001189
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)]	12913-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	27.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	109.54
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012813
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.946072
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)]	128.208071
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.183945
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000282
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)]	12910-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	53.03
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	97
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1015
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.015324
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.926365
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)]	119.017208
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	36.312411
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000254
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)]	12906-Dehy 1 - Unit
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)]	5.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	66.49
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.88
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)]	1464
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	695
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01759
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.907549
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)]	97.738304
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.48979
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000201
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)]	12898-Dehy 1 - Unit
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)]	30.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	56.16
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8712
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	870
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007247
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.765288
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)]	692.229283
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.444422
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001189
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)]	12894-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	69.93
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)]	1.53
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	102
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	850
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011863
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.854146
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)]	304.390567
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	4.107254
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000588
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)]	12890-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	100.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	112
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005389
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.898222
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)]	183.428962
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.683296
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000365
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)]	12886-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CANADIAN, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	99.49
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	920
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012537
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.928642
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)]	413.427144
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.780993
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000893
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)]	12874-Dehy 1 - Unit
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)]	8.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	49.16
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	94
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1000
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011165
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92991
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)]	793.4063
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	12.86496
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001691
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)]	12873-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	102
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	880
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008033
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.810498
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)]	637.988283
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.601161
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001146
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)]	12868-Dehy 1 - Unit
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)]	5.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	78.98
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	108
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	910
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012307
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.868234
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)]	586.332817
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.937459
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001118
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)]	12831-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	62.46
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.7
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	3947
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	98
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	850
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007509
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.794868
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)]	284.512402
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.287735
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000505
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)]	12804-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	65.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	1704
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	98
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	790
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004613
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.796419
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)]	124.899831
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.385412
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000213
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)]	12777-Dehy 1 - Unit
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)]	29.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	86.64
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	1114
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1005
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006277
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.793127
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)]	731.730106
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.448736
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001302
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)]	12776-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	103.58
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	111
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	710
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009181
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.827919
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)]	188.101936
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.369049
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000349
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)]	12774-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	52.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	962
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005206
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.820264
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)]	595.899372
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.112621
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.00106
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)]	12753-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.64
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	143.83
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)]	0.45
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8730
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	125
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	750
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011146
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96105
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.453269
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	20.393286
Unit ID or Name [98.236(e)(1)(i)]	12750-Dehy 1 - Unit
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)]	29.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	73.41
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	110
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1090
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007851
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.811558
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)]	751.529904
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.232693
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001391
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)]	12714-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	71.02
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8064
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	529
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00954
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.87977
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)]	124.157651
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.76315
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000244
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)]	12713-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	50.72
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)]	6.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1040
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.013268
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.907666
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)]	1305.888786
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	20.433061
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.002751
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)]	12710-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	18.56
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)]	0.45
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)]	8712
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	58
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	780
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009393
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.955253
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	0.994242
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.082769
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000002
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.533258
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	23.473079
Unit ID or Name [98.236(e)(1)(i)]	12707-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	14.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	47.12
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	4.5
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007168
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.886371
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)]	925.68147
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	13.268162
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001829
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)]	12706-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CANADIAN, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	14.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	103.07
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	115
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	822
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005636
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.831216
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)]	554.114933
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.890931
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001014
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)]	12692-Dehy 1 - Unit
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)]	15.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	48.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	94
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1010
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.000598
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.925306
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)]	657.819897
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.2614
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001355
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)]	12669-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	76.63
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.53
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	109
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	980
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01035
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.882477
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)]	3.988823
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.273994
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000008
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.76153
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	88.211015
Unit ID or Name [98.236(e)(1)(i)]	12668-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	BLAINE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	48.63
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	92
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	940
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012423
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.887633
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)]	609.064535
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.700034
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001198
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)]	12666-Dehy 1 - Unit
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)]	3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	82.5
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	3960
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	92
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	475
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008042
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.868723
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)]	53.995979
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.756545
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000107
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)]	12665-Dehy 2 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	65.39
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.53
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	710
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006568
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.795152
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)]	292.126889
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.352147
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000515
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)]	12653-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	74.22
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	98
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	675
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011426
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.871697
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)]	71.617551
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.004295
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000141
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)]	12646-Dehy 1 - Unit
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)]	8.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	116.71
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	110
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	590
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008704
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.880545
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)]	361.480279
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	5.207216
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000723
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)]	12645-Dehy 1 - Unit
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)]	0.74
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	37.44
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)]	0.45
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)]	8186
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	580
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00484
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.857686
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.861497
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.024871
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000004
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.594097
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	18.119963
Unit ID or Name [98.236(e)(1)(i)]	12623-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.97
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	756
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.013708
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.895209
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)]	664.17456
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.950217
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001358
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)]	12622-Dehy 1 - Unit
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)]	11.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.87
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1030
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007662
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.858501
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)]	729.079813
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	9.919074
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001412
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)]	12619-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.57
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	42.29
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)]	0.45
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)]	8189
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	630
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.010282
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.960916
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.409269
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	16.826911
Unit ID or Name [98.236(e)(1)(i)]	12614-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CADDO, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	80.05
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)]	0.45
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)]	8654
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	93
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	510
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012443
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.929265
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)]	48.6260473
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0500268
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0001048
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)]	12603-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	WASHITA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	42.55
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	87
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	920
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006072
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.849638
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.916526
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	61.870888
Unit ID or Name [98.236(e)(1)(i)]	12600-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	WASHITA, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	16
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	55.42
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	955
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	955
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.005073
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.903624
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)]	567.764422
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	8.616636
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001165
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)]	12593-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ROGER MILLS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	78.4
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)]	0.45
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)]	4015
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	112
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1060
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01455
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.919925
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	115.600982
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	13.716532
Unit ID or Name [98.236(e)(1)(i)]	12590-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ELLIS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	11.4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	58.77
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)]	3.88
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	96
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	853
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.008249
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.769868
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)]	936.095114
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	10.132896
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001608
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)]	12589-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	ELLIS, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	11.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.27
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	84
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	846
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009197
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.776362
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)]	671.647903
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.446201
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001172
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)]	12581-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	CUSTER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	71.49
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.78
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	94
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	610
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009495
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.841866
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)]	263.471647
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	3.422354
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000497
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)]	12552-Dehy 1 - Unit
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)]	30.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	40.14
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.77
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	805
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007881
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.785325
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)]	670.825854
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.528864
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001172
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)]	12549-Dehy 1 - Unit
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)]	2.07
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	19.5
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.67
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	60
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	800
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.966214
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)]	416.528503
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	7.386866
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000934
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)]	12545-Dehy 1 - Unit
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)]	1.52
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	51.07
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8456
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	540
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0092
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.921825
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)]	115.293256
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.860611
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000247
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)]	12727-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	WHEELER, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.34
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	56.23
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	91
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	740
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004409
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.824656
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)]	487.335764
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	6.059131
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000898
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)]	12588-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	WHEELER, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	59.81
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Electric
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.97
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	800
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007265
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.809477
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)]	413.162781
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	4.932624
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000745
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	23.3
mt CH4	822.00
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)]	All other equipment with a physical volume greater than or equal 50 cubic feet
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	1
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.000029
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0.001016
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)]	3773
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	10.209773
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	363.743112
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)]	7480
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	2.851551
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	99.837821
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)]	33
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	9.508007
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	332.891943
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Scrubbers/strainers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	6
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.582736
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	20.402583
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Facility piping
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	5605
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.146407
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	5.125897

AtmosphericTanksDetails:

mt CO2	2150.9
mt CH4	94.17
mt N2O	0.004
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?	Yes
Was Calculation Method 1 used to calculate emissions [(98.233(j)(1)]?	Yes
Was Calculation Method 2 used to calculate emissions [(98.233(j)(2)]?	No
Was Calculation Method 3 used to calculate emissions [(98.233(j)(3)]?	Yes
If Calculation Method 1 or 2 were used, were any atmospheric tanks observed to have malfunctioning dump valves during the calendar year?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

AtmosphericTanksCalculationMethodOneOrTwoSubBasinRowDetails:

County and State [98.236(j)(1)(i)]	BLAINE, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	64.9675
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	25
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	8
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8214611
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8214611
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0055968
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0055968
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.018555
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	12.08204
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	251.973579
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	1.230069
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000474
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)]	153344.38
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	33
County and State [98.236(j)(1)(i)]	BLAINE, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	WINSIM
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	66
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.879
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.879
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 flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	39.673391
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.214974
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000079
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)]	10741.74
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)]	No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	4
County and State [98.236(j)(1)(i)]	CADDO, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	51
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	3
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7741944
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7741944
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0063371
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0063371
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.198728
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	1.937597
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)]	5476.5
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)]	3
County and State [98.236(j)(1)(i)]	CANADIAN, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	68.73
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)]	0.7741944
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7741944
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0063371
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0063371
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.620391
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	6.048812
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)]	17096.6
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)]	CUSTER, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	57.6675
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	8
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	7
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8629236
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8629236
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0084843
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0084843
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.267862
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	6.564671
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	41.264919
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.262236
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000091
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)]	27859.47
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	15
County and State [98.236(j)(1)(i)]	DEWEY, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	61.992
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	8
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)]	0.6707778
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6707778
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0067348
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0067348
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.187154
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	13.806732
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	47.081386
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.273794
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000097
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)]	55911.9
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	20
County and State [98.236(j)(1)(i)]	ELLIS, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	71.8066667
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	7
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	3
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7663981
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7663981
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0066457
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0066457
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.112578
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	3.902713
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	483.036173
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	1.964037
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000831
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)]	36070.73
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	10
County and State [98.236(j)(1)(i)]	GRADY, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	63.748
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	28
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	10
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6870689
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6870689
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0060874
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0060874
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.273499
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	4.489401
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	394.775973
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	1.596289
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000681
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)]	116806.6
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	38
County and State [98.236(j)(1)(i)]	GRADY, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	63.748
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6646
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.6646
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.007
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.007
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	222.543423
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.715839
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000346
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)]	19882.92
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)]	No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	4
County and State [98.236(j)(1)(i)]	GRADY, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	WINSIM
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	63.748
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7469
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7469
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0066
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0066
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	51.824946
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.206004
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000089
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)]	8989.52
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)]	No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	4
County and State [98.236(j)(1)(i)]	ROGER MILLS, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	63.9666667
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	12
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8036
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.8036
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0072
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0072
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	108.888737
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.497884
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000199
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)]	16738.8
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)]	No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	12
County and State [98.236(j)(1)(i)]	ROGER MILLS, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	WINSIM
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	62.62
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7366
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7366
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0066
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0066
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	53.481796
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	0.198149
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000087
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)]	10206.38
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)]	No
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	4
County and State [98.236(j)(1)(i)]	WASHITA, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	66.19
Count of tanks with flaring emission control measures [98.236(j)(1)(xiv)(A)]	4
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	8
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7858296
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7858296
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0061581
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0061581
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.259386
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	2.279312
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(1)(xiv)(B)]	325.56972
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(1)(xiv)(C)]	1.511301
Annual N2O emissions from flaring (mt N2O) [98.236(j)(1)(xiv)(D)]	0.000601
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)]	29429.05
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)]	Yes
Count of atmospheric tanks [98.236(j)(1)(x)]	12
County and State [98.236(j)(1)(i)]	WOODWARD, OK
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	HYSYS
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	59.96
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	119.87
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	60.07
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)]	0.7741944
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.7741944
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.0063371
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.0063371
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0410069
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	0.7252473
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)]	3831.52
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

AtmosphericTanksCalculationMethodThreeRowDetails:

Estimate of fraction of oil/condensate throughput sent to tanks in basin with flaring [98.236(j)(2)(i)(B)]	0.222
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)]	126
Total annual oil/condensate throughput that is sent to all atmospheric tanks (barrels per year) [98.236(j)(2)(i)(A)]	57209.15

AtmosphericTanksCalcMethodThreeNoFlaringRowDetails:

County and State [98.236(j)(2)(ii)(A)]	CADDO, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	10
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	1.4728
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	3.3792
County and State [98.236(j)(2)(ii)(A)]	GRADY, 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)]	CANADIAN, 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
County and State [98.236(j)(2)(ii)(A)]	ROGER MILLS, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	12
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	1.76736
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	4.05504
County and State [98.236(j)(2)(ii)(A)]	WHEELER, TX
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)]	LIPSCOMB, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	4
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.58912
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	1.35168
County and State [98.236(j)(2)(ii)(A)]	BLAINE, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	26
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	3.82928
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	8.78592
County and State [98.236(j)(2)(ii)(A)]	CUSTER, OK
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	16
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	2.35648
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	5.40672
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)]	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

AtmosphericTanksCalcMethodThreeWithFlaringRowDetails:

County and State [98.236(j)(2)(iii)(A)]	GRADY, OK
Count of tanks with flaring emission control measures [98.236(j)(2)(iii)(B)]	15
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(2)(iii)(C)]	69.624705
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(2)(iii)(D)]	0.311607
Annual N2O emissions from flaring (mt N2O) [98.236(j)(2)(iii)(E)]	0.000125
County and State [98.236(j)(2)(iii)(A)]	ROGER MILLS, OK
Count of tanks with flaring emission control measures [98.236(j)(2)(iii)(B)]	8
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(2)(iii)(C)]	23.407168
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(2)(iii)(D)]	0.116058
Annual N2O emissions from flaring (mt N2O) [98.236(j)(2)(iii)(E)]	0.000045
County and State [98.236(j)(2)(iii)(A)]	WASHITA, OK
Count of tanks with flaring emission control measures [98.236(j)(2)(iii)(B)]	5
Annual CO2 emissions from flaring (mt CO2) [98.236(j)(2)(iii)(C)]	21.362781
Annual CH4 emissions from flaring (mt CH4) [98.236(j)(2)(iii)(D)]	0.120321
Annual N2O emissions from flaring (mt N2O) [98.236(j)(2)(iii)(E)]	0.000044

FlareStacksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
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)]	12750-Condensate Flare
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)]	425768.0818584
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12590-Condensate Flare
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)]	2386173.3874791
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12898-Condensate Flare
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)]	436527.7304001
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13776-Condensate Flare
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)]	570246.9634431
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13787-Condensate Flare
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)]	254017.1452213
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13877-Condensate Flare
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)]	354532.9473888
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13873-Condensate Flare
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)]	328442.9649061
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12777-Condensate Flare
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)]	750245.3848505
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14670-Condensate Flare
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)]	195770.7137282
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12665-Condensate Flare
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)]	700533.7415774
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12692-Condensate Flare
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)]	463034.0009114
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14106-Condensate Flare
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)]	726490.4695069
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12918-Condensate Flare
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)]	4864269.8419176
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12948-Condensate Flare
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)]	4340570.7953883
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13905-Condensate Flare
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)]	403550.4801945
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13782-Condensate Flare
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)]	1635690.4160856
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12831-Condensate Flare
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)]	178355.6167318
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14366-Condensate Flare
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)]	846423.882836
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13946-Condensate Flare
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)]	254858.123538
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14586-Condensate Flare
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)]	573398.5723679
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14647-Condensate Flare
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)]	357044.6932072
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14046-Condensate Flare
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)]	676445.4415519
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13967-Condensate Flare
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)]	326259.1098881
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14146-Condensate Flare
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)]	616984.7417847
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14714-Condensate Flare
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)]	2804943.6060441
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14646-Condensate Flare
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)]	718259.5906284
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12552-Condensate Flare
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)]	367868.3903502
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14266-Condensate Flare
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)]	212530.1463538
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12581-Condensate Flare
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)]	609576.3816678
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12623-Condensate Flare
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)]	183101.8224695
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12774-Condensate Flare
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)]	387112.5396225
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	12873-Condensate Flare
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)]	1016397.4377057
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13778-Condensate Flare
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)]	1327680.3721079
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	13803-Condensate Flare
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)]	337470.5902715
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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)]	14587-Condensate Flare
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)]	636893.2411064
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.88201
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00919
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	0.0
mt CH4	0.00
Did the facility have any centrifugal compressors subject to reporting under 98.232 [98.236(o)]?	No

ReciprocatingCompressorsDetails:

mt CO2	9.0
mt CH4	59.32
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)]	9.0337556
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	59.3173229
Count of Reciprocating Compressors [98.236(p)(5)(i)]	325

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	33.0
mt CH4	1119.58
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?	Yes
Did this facility use population counts to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(r)]?	Yes
Did the facility elect to comply with 98.236(q) according to 98.233(q)(1)(iv) for any components at the facility [per 98.236(q)(1)(iv)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Number of complete equipment leak surveys performed during the calendar year [98.236(q)(1)(i)]	4
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)]	103
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	85.28
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0208
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.7289
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)]	10
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	878.4
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0174
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.6099
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)]	133
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	66.05
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0055
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.1934
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)]	8
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	1098
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0119
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.4165
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)]	29
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	302.9
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0191
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.6694
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)]	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 - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	35
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	250.97
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0191
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.6694
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)]	21764
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	11.938
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	394.137
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)]	62549
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	4.826
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	159.089
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)]	1940
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.27
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	8.985
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)]	1299
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	1.137
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	37.521
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)]	6353.092
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	12.69
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	444.292
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Unprotected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Plastic/composite gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	194.285
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	2.064
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	72.271
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)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0

MajorGasEquipmentTypeRowDetails:

Major Equipment Type [98.236(r)(3)(ii)]	Wellhead
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Separators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	198
Major Equipment Type [98.236(r)(3)(ii)]	Meters/piping
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	170
Major Equipment Type [98.236(r)(3)(ii)]	Compressors
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	154
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 Western US [98.236(r)(3)(ii)(B)]	3
Major Equipment Type [98.236(r)(3)(ii)]	Dehydrators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	57

CombustionEmissionsDetails:

mt CO2	873486.9
mt CH4	16.46
mt N2O	1.646
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	97
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)]	No
Are there Internal fuel combustion units of any heat capacity that are compressor-drivers? [98.236(z)(2)(i)]	Yes

LargeCombustionUnitEmissionsRowDetails:

Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	15457496.86239
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	873486.93686
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	16.46225
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	1.64622