Address: 499 W. Sheridan, Suite 1500
City: Oklahoma City
State: OK
Postal Code: 73100

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):383,982.8
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:

Subpart W: Petroleum and Natural Gas Systems

SubpartWSummaryDetails:

Industry Segment Number	9
Industry Segment Name	Onshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)	151236.7
Total CO2e Emissions (mt CO2e)	383983.0
Total Reported CH4 Emissions (mt CH4)	9306.77
Total Reported N2O Emissions (mt N2O)	0.258

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)	171.3
Total Reported CH4 Emissions (mt CH4)	3470.34
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)	13214.2
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1398.5
Total Reported CH4 Emissions (mt CH4)	5191.77
Total Reported N2O Emissions (mt N2O)	0.001
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Completions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Completions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2.2
Total Reported CH4 Emissions (mt CH4)	43.84
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
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	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)	2.1
Total Reported CH4 Emissions (mt CH4)	13.87
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)	28.1
Total Reported CH4 Emissions (mt CH4)	584.38
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)	136420.2
Total Reported CH4 Emissions (mt CH4)	2.57
Total Reported N2O Emissions (mt N2O)	0.257

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	345 - Arkoma Basin
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	102132195.256018
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)]	102132195.256018
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	0
Quantity of all hydrocarbon liquids transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iv)]	0

PneumaticDeviceVentingDetails:

mt CO2	171.3
mt CH4	3470.34
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)]	54
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	16.07193
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	323.033468
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)]	1387
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	147.078765
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	2984.204952
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)]	732
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	8.120494
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	163.098465
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	13214.2
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)]	11471-AGR 1
County and State [98.236(d)(1)(vi)]	LE FLORE, OK
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	0
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)]	0
Unit ID or Name [98.236(d)(1)(i)]	11263-AGR 1
County and State [98.236(d)(1)(vi)]	WHITE, AR
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	13939.97
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)]	9055.852245
Unit ID or Name [98.236(d)(1)(i)]	11384-AGR 1
County and State [98.236(d)(1)(vi)]	PITTSBURG, OK
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	1565.6
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)]	1064.832844
Unit ID or Name [98.236(d)(1)(i)]	11282-AGR 1
County and State [98.236(d)(1)(vi)]	PITTSBURG, OK
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	5171
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)]	3093.522491

AcidGasCalcMethod4EmissionsRowDetails:

Unit ID or Name [98.236(d)(1)(i)]	11471-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)]	70
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	340
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	0
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	0
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	0
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	0
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	0
Solvent pressure (psi) [98.236(d)(2)(iii)(I)]	800
Solvent temperature (°F) [98.236(d)(2)(iii)(J)]	100
Solvent circulation rate (gallons per minute) [98.236(d)(2)(iii)(K)]	200
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.67
Unit ID or Name [98.236(d)(1)(i)]	11263-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)]	80
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	900
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	26965.276052
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	2.5708
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	1.352
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	8616
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	81.859
Solvent pressure (psi) [98.236(d)(2)(iii)(I)]	900
Solvent temperature (°F) [98.236(d)(2)(iii)(J)]	80
Solvent circulation rate (gallons per minute) [98.236(d)(2)(iii)(K)]	150
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.67
Unit ID or Name [98.236(d)(1)(i)]	11384-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)]	110
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	390
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	10555.55488
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	3.7328
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	2.457
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	2472
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	129.163
Solvent pressure (psi) [98.236(d)(2)(iii)(I)]	390
Solvent temperature (°F) [98.236(d)(2)(iii)(J)]	110
Solvent circulation rate (gallons per minute) [98.236(d)(2)(iii)(K)]	25
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.67
Unit ID or Name [98.236(d)(1)(i)]	11282-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)]	80
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	800
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	11736.11036
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	2.689
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	1.571
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	7344
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	90.346
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)]	200
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.67

DehydratorsDetails:

mt CO2	1398.5
mt CH4	5191.77
mt N2O	0.001
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs greater than or equal to 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	Yes
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs less than 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	Yes
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:

Total Number of Small Glycol Dehydrators [98.236(e)(2)(i)]	20
Vapor Recovery	No
Dehydrator vents to flares or regenerator firebox/fire tubes	No
Control devices other than vapor recovery, flare or regenerator firebox/fire tubes	Yes
Emissions vented to flare or regenerator firebox/fire tubes
Emissions that were not vented to a flare or regenerator firebox/fire tubes
Total CO2 Emissions (mt CO2) [98.236(e)(2)(iv)(B)] [98.236(e)(2)(v)(A)]	3.38614
Total CH4 Emissions (mt CH4) [98.236(e)(2)(iv)(C)] [98.236(e)(2)(v)(B)]	28.26276

OtherVentControlsTypeAndCountRowDetails:

Specify Type of Other Control Device(s) [98.236(e)(2)(iii)]	No Control Device
Number of Small Glycol Dehydrators By Other Vent Control Type [98.236(e)(2)(iii)]	20

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)]	11395-Dehy 1 -Unit 562
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.47
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	51.69
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)]	0.67
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)]	No
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)]	670
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007128
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.973801
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)]	1.54568
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	28.052692
Unit ID or Name [98.236(e)(1)(i)]	11313-Dehy 1 - Unit 425
County and State [98.236(e)(1)(xviii)]	JOHNSON, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.43
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	84.22
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)]	1.5
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)]	No
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)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	276
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011283
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.968791
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)]	2.590702
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	25.74808
Unit ID or Name [98.236(e)(1)(i)]	11256-Dehy 2 - Unit 304
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.95
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.13
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	74
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	650
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006535
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.974641
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)]	7.788
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	146.223665
Unit ID or Name [98.236(e)(1)(i)]	12060-Dehy 1 - Unit 527
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.72
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	39.82
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	77
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	652
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006074
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.969975
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)]	7.11251
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	144.236931
Unit ID or Name [98.236(e)(1)(i)]	11263-Dehy 1 - Unit 720
County and State [98.236(e)(1)(xviii)]	WHITE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	29.12
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.88
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)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	923
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0257083
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.957256
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)]	86.621628
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	445.028546
Unit ID or Name [98.236(e)(1)(i)]	11263-Dehy 2 - Unit 719
County and State [98.236(e)(1)(xviii)]	WHITE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.71
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.88
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)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	2928
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)]	923
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0257083
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.957256
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)]	28.952982
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	148.749267
Unit ID or Name [98.236(e)(1)(i)]	11999-Dehy 1 - Unit 393
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.03
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	32.47
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.67
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)]	No
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)]	73
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	720
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.013183
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.967143
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)]	3.305926
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	30.953325
Unit ID or Name [98.236(e)(1)(i)]	11227-Dehy 1 - Unit 422
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
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)]	43.1
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)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	665
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004888
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.974204
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)]	5.721796
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	147.018359
Unit ID or Name [98.236(e)(1)(i)]	11721-Dehy 1 - Unit 52
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.09
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.67
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)]	No
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)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	688
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00471
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97582
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)]	1.196014
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	30.277835
Unit ID or Name [98.236(e)(1)(i)]	11410-Dehy 2 - Unit 479
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.85
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.77
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)]	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)]	No
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)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	688
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00771
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.973545
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)]	14.542897
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	224.898355
Unit ID or Name [98.236(e)(1)(i)]	11408-Dehy 1 - Unit 599
County and State [98.236(e)(1)(xviii)]	WHITE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.71
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.99
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	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)]	811
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.004954
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.945502
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)]	611.443743
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	192.810864
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.001359
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)]	11390-Dehy 1 - Unit 31
County and State [98.236(e)(1)(xviii)]	FRANKLIN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	14.09
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	79.92
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)]	6.67
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)]	69
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	208
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007179
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.969441
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)]	6.039673
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	89.005709
Unit ID or Name [98.236(e)(1)(i)]	11364-Dehy 1 - Unit 127
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.72
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	68.36
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)]	0.67
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)]	No
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)]	475
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011714
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.972678
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)]	1.863557
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	19.589203
Unit ID or Name [98.236(e)(1)(i)]	11361-Dehy 1 - Unit 588
County and State [98.236(e)(1)(xviii)]	FRANKLIN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.64
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	52.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	83
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)]	0.012213
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.969568
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)]	12.357489
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	125.958972
Unit ID or Name [98.236(e)(1)(i)]	11358-Dehy 1 - Unit 5
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
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)]	56.58
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)]	0.67
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)]	No
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)]	700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.020814
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96337
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)]	4.56949
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	28.807651
Unit ID or Name [98.236(e)(1)(i)]	11328-Dehy 1 - Unit 2008
County and State [98.236(e)(1)(xviii)]	YELL, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.64
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.88
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)]	0.67
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	36
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)]	970
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007066
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.968459
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.009275
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.174724
Unit ID or Name [98.236(e)(1)(i)]	11304-Dehy 1 - Unit 552
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	67.14
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)]	0.67
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)]	No
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)]	450
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007122
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.976721
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)]	1.092704
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	18.71504
Unit ID or Name [98.236(e)(1)(i)]	11293-Dehy 1 - Unit 328
County and State [98.236(e)(1)(xviii)]	JOHNSON, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	97.97
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)]	3.5
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)]	No
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)]	83
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	279
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011682
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.968189
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)]	6.079408
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	59.999384
Unit ID or Name [98.236(e)(1)(i)]	11292-Dehy 1 - Unit 594
County and State [98.236(e)(1)(xviii)]	WHITE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.72
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	47.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	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)]	802
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009702
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97561
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)]	26.900386
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	377.082223
Unit ID or Name [98.236(e)(1)(i)]	11290-Dehy 2 - Unit 598
County and State [98.236(e)(1)(xviii)]	WHITE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	7.82
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	42.04
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	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)]	814
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.023098
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.958093
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)]	134.303258
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	763.700772
Unit ID or Name [98.236(e)(1)(i)]	11284-Dehy 1 - Unit 295
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.91
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	51.65
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)]	0.67
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)]	No
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)]	670
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.003828
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.976629
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.830455
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	28.052692
Unit ID or Name [98.236(e)(1)(i)]	11275-Dehy 2 - Unit 23
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.79
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.67
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)]	No
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)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	688
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.009737
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.968813
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)]	2.471498
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	30.357304
Unit ID or Name [98.236(e)(1)(i)]	11265-Dehy 1 - Unit 317
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.09
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	52.8
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.67
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)]	No
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)]	680
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012396
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9647
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)]	2.705932
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	28.251366
Unit ID or Name [98.236(e)(1)(i)]	11261-Dehy 1 - Unit 361
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.46
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	51.56
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)]	1.5
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)]	No
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)]	700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.011855
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.968761
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)]	5.8807344
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	65.1648942
Unit ID or Name [98.236(e)(1)(i)]	11252-Dehy 1 - Unit 383
County and State [98.236(e)(1)(xviii)]	POPE, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.89
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	98.64
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)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.67
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)]	No
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)]	239
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.015122
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96413
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)]	3.369502
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	24.754713
Unit ID or Name [98.236(e)(1)(i)]	11223-Dehy 1 - Unit 372
County and State [98.236(e)(1)(xviii)]	LOGAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.82
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	37.24
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)]	1.5
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)]	75
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	654
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00711
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.971677
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)]	3.61983
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	62.383466
Unit ID or Name [98.236(e)(1)(i)]	11222-Dehy 1 - Unit 16
County and State [98.236(e)(1)(xviii)]	SEBASTIAN, AR
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.93
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.21
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)]	1.5
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)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	712
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.020037
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.959237
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)]	11.721734
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	69.138363
Unit ID or Name [98.236(e)(1)(i)]	11255-Dehy 1 - Unit
County and State [98.236(e)(1)(xviii)]	LE FLORE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.38
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)]	0.6
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)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.006075
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.988279
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)]	1.273497
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	26.946479
Unit ID or Name [98.236(e)(1)(i)]	11744-Dehy 1 - Unit 722
County and State [98.236(e)(1)(xviii)]	LATIMER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.14
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)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	575
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.028704
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.954359
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)]	24.917625
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	100.771151
Unit ID or Name [98.236(e)(1)(i)]	11702-Dehy 1 - Unit 213
County and State [98.236(e)(1)(xviii)]	SEQUOYAH, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	30.41
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)]	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)]	8583
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	690
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.014592
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.967901
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)]	2.367055
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	19.660576
Unit ID or Name [98.236(e)(1)(i)]	11471-Dehy 1 - Unit 708
County and State [98.236(e)(1)(xviii)]	LE FLORE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	50.9
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)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	300
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.024504
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.950363
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)]	4.887367
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	20.864686
Unit ID or Name [98.236(e)(1)(i)]	11403-Dehy 1 - Unit 149
County and State [98.236(e)(1)(xviii)]	PITTSBURG, 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)]	23.64
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)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.5
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)]	No
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)]	620
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.025356
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.955422
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)]	13.668734
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	60.396731
Unit ID or Name [98.236(e)(1)(i)]	11387-Dehy 1 - Unit 533
County and State [98.236(e)(1)(xviii)]	PITTSBURG, 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)]	44.26
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)]	0.67
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)]	8132
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)]	700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007343
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93271
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)]	1.588317
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	26.842037
Unit ID or Name [98.236(e)(1)(i)]	11384-Dehy 1 - Unit 82
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.5
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)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	700
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.007623
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.956708
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)]	9.337653
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	153.37591
Unit ID or Name [98.236(e)(1)(i)]	11382-Dehy 1 - Unit 481
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	51.33
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	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)]	800
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.038212
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.945495
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)]	48.833936
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	170.449906
Unit ID or Name [98.236(e)(1)(i)]	11376-Dehy 1 - Unit 713
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	32.68
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	630
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.019371
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.951966
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)]	23.085856
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	139.889955
Unit ID or Name [98.236(e)(1)(i)]	11368-Dehy 1 - Unit 477
County and State [98.236(e)(1)(xviii)]	LE FLORE, 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)]	41.26
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)]	No
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)]	313
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.014806
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.960321
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)]	3.182749
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	22.251427
Unit ID or Name [98.236(e)(1)(i)]	11365-Dehy 1 - Unit 146
County and State [98.236(e)(1)(xviii)]	LE FLORE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.17
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	708
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.017609
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96735
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)]	1.164226
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	7.946938
Unit ID or Name [98.236(e)(1)(i)]	11363-Dehy 1 - Unit 441
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	33.94
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)]	1.5
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)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	600
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.012456
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.940311
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)]	4.946969
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	25.434176
Unit ID or Name [98.236(e)(1)(i)]	11332-Dehy 1 - Unit 568
County and State [98.236(e)(1)(xviii)]	LE FLORE, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	24.48
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)]	0.9
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)]	65
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)]	0.018278
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.958073
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)]	6.64364
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	43.433991
Unit ID or Name [98.236(e)(1)(i)]	11314-Dehy 1 - Unit 198
County and State [98.236(e)(1)(xviii)]	LATIMER, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	40
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)]	No
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)]	570
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.023086
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.953002
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)]	7.311183
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	39.019467
Unit ID or Name [98.236(e)(1)(i)]	11312-Dehy 1 - Unit 565
County and State [98.236(e)(1)(xviii)]	HASKELL, 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)]	62.64
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)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	570
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.042476
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.933918
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)]	105.69428
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	334.96345
Unit ID or Name [98.236(e)(1)(i)]	11303-Dehy 1 - Unit 716
County and State [98.236(e)(1)(xviii)]	PITTSBURG, 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)]	27.45
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)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
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)]	70
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)]	0.035605
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.936175
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)]	52.052446
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	178.011418
Unit ID or Name [98.236(e)(1)(i)]	11283-Dehy 1 - Unit 480
County and State [98.236(e)(1)(xviii)]	PITTSBURG, 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)]	22.99
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)]	0.525
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)]	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)]	650
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0163915
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9416128
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)]	11.046244
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	21.695142
Unit ID or Name [98.236(e)(1)(i)]	11282-Dehy 1 - Unit 721
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	14.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	120.16
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)]	7.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8702
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)]	800
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02926
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.942405
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)]	68.404297
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	341.982012
Unit ID or Name [98.236(e)(1)(i)]	11278-Dehy 1 - Unit 438
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	40
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)]	1.5
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)]	8753
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)]	100
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.017651
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.952497
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)]	8.226449
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	62.956952
Unit ID or Name [98.236(e)(1)(i)]	11229-Dehy 1 - Unit 472
County and State [98.236(e)(1)(xviii)]	PITTSBURG, OK
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.82
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)]	0.2
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)]	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)]	830
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.028282
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.923436
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)]	1.84369
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	11.483326

BlowdownVentStacksDetails:

mt CO2	2.2
mt CH4	43.84
Did the facility have any blowdown vent stacks subject to reporting under 98.232 [98.236(i)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
How were emissions determined? [98.236(i)]	Calculated by equipment or event type

BlowdownEquipmentOrEventEmissionsRowDetails:

Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Compressors
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	366
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	1.524696
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	29.488106
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)]	134
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.078352
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	1.627001
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)]	6
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.074908
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	1.555478
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)]	5
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.530726
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	11.020658
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)]	2805
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.007152
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0.148469

AtmosphericTanksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?	No
Was Calculation Method 1 used to calculate emissions [(98.233(j)(1)]?	No
Was Calculation Method 2 used to calculate emissions [(98.233(j)(2)]?	No
Was Calculation Method 3 used to calculate emissions [(98.233(j)(3)]?	No
If Calculation Method 1 or 2 were used, were any atmospheric tanks observed to have malfunctioning dump valves during the calendar year?	No

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)]?	No

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	2.1
mt CH4	13.87
Did the facility have any reciprocating compressors subject to reporting under 98.232 [98.236(p)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Total annual Reciprocating Compressor emissions CO2 Emissions (mt CO2) [98.236(p)(5)(ii)]	2.112509
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	13.8711278
Count of Reciprocating Compressors [98.236(p)(5)(i)]	76

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	28.1
mt CH4	584.38
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)]	15
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	585.6
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0377
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.7834
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	8784
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.01
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.2078
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Pressure Relief Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	8784
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0347
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.7194
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)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Pump
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Agitator Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Light Crude Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Pump
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Agitator Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Heavy Crude Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0

LeaksCalculatedWithCountsFactorsRowDetails:

Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gas Service - Valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	13367
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)]	12.515
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	259.68
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)]	41078
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)]	5.38
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	112.047
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)]	1201
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)]	0.283
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	5.968
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)]	845
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)]	1.264
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	26.174
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)]	2379.767
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)]	8.611
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	178.803
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)]	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 - 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)]	103
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)]	196
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)]	71
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)]	15
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)]	72

CombustionEmissionsDetails:

mt CO2	136420.2
mt CH4	2.57
mt N2O	0.257
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)]	Yes
Total number of combustion units meeting 98.236(z)(1) descriptions	91
Are there external fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr? [98.236(z)(2)(i)]	Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr? [98.236(z)(2)(i)]	No
Are there Internal fuel combustion units of any heat capacity that are compressor-drivers? [98.236(z)(2)(i)]	Yes

LargeCombustionUnitEmissionsRowDetails:

Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	2292118.1116
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	129525.19066
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	2.44111
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.24411
Type of combustion unit [98.236(z)(2)(i)]	External fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	122016.41302
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	6895.01954
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	0.12995
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.01299