Address: 1111 Travis St.
City: Houston
State: TX
Postal Code: 77002

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):158,484.3
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:211120
Second Primary NAICS Code:211130

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)	36249.9
Total CO2e Emissions (mt CO2e)	158484.2
Total Reported CH4 Emissions (mt CH4)	4888.60
Total Reported N2O Emissions (mt N2O)	0.065

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)	292.1
Total Reported CH4 Emissions (mt CH4)	2289.17
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	40.0
Total Reported CH4 Emissions (mt CH4)	326.09
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1288.6
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1767.0
Total Reported CH4 Emissions (mt CH4)	962.12
Total Reported N2O Emissions (mt N2O)	0.003
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Completions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Completions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.5
Total Reported CH4 Emissions (mt CH4)	8.62
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	9.4
Total Reported CH4 Emissions (mt CH4)	173.23
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)	257.1
Total Reported CH4 Emissions (mt CH4)	1.56
Total Reported N2O Emissions (mt N2O)	0.001
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)	0.4
Total Reported CH4 Emissions (mt CH4)	2.55
Source Reporting Form	Equipment Leaks Surveys and Population Counts [98.236(q,r)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	144.2
Total Reported CH4 Emissions (mt CH4)	1124.64
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)	32450.6
Total Reported CH4 Emissions (mt CH4)	0.61
Total Reported N2O Emissions (mt N2O)	0.061

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	220 - Gulf Coast Basin (LA, TX)
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	65954533.28
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)]	65358449.1708382
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	1729290.53
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)]	1729290.53

PneumaticDeviceVentingDetails:

mt CO2	292.1
mt CH4	2289.17
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)]	3
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	0.9544857
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	15.8266995
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8016
Type of Pneumatic Device	Intermittent Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	1281
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	291.074687
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	2271.3030527
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8744.4496487
Type of Pneumatic Device	Low-Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	17
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	0.045429
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	2.0397975
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	4906

NaturalGasDrivenPneumaticPumpsDetails:

mt CO2	40.0
mt CH4	326.09
Did the Facility have any natural gas driven pneumatic pumps subject to reporting under 98.232 [98.236(c)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

PneumaticPumpTypesRowDetails:

Type of Pneumatic Pump	Natural Gas Driven Pneumatic Pumps
Total count of natural gas driven pneumatic pumps, Count [98.236(c)(1)]	188
Average estimated number of hours in the calendar year that the natural gas driven pneumatic pumps were operated, T (hours) [98.236(c)(2)]	8591.52
Total CO2 Emissions (mt CO2) [98.236(c)(3)]	39.9907885
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	326.0933072

AcidGasRemovalUnitsDetails:

mt CO2	1288.6
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)]	AMINE1
County and State [98.236(d)(1)(vi)]	VERMILION, LA
Total feed rate entering the acid gas removal unit for the year (million cubic feet) [98.236(d)(1)(ii)]	835.646
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)]	1288.6346164

AcidGasCalcMethod4EmissionsRowDetails:

Unit ID or Name [98.236(d)(1)(i)]	AMINE1
Name of simulation software package used [98.236(d)(2)(iii)(A)]	AmineCalc
Natural gas feed temperature (°F) [98.236(d)(2)(iii)(B)]	76.67
Natural gas feed pressure (psi) [98.236(d)(2)(iii)(C)]	825.83
Natural gas feed flow rate (standard cubic feet per minute) [98.236(d)(2)(iii)(D)]	1620.16933
Acid gas content of feed natural gas (mole percent) [98.236(d)(2)(iii)(E)]	5
Acid gas content of outlet natural gas (mole percent) [98.236(d)(2)(iii)(F)]	2.2714
Unit operating hours (excluding downtime for maintenance or standby) [98.236(d)(2)(iii)(G)]	8472
Exit temperature of the natural gas (°F) [98.236(d)(2)(iii)(H)]	76.7
Solvent pressure (psi) [98.236(d)(2)(iii)(I)]	825
Solvent temperature (°F) [98.236(d)(2)(iii)(J)]	76.7
Solvent circulation rate (gallons per minute) [98.236(d)(2)(iii)(K)]	200
Solvent weight (pounds per gallon) [98.236(d)(2)(iii)(L)]	8.6

DehydratorsDetails:

mt CO2	1767.0
mt CH4	962.12
mt N2O	0.003
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)]	7
Vapor Recovery	No
Dehydrator vents to flares or regenerator firebox/fire tubes	Yes
Number of Small Glycol Dehydrators By Vent Control Type, Count [98.236(e)(2)(ii)] [98.236(e)(2)(iv)(A)]	3
Control devices other than vapor recovery, flare or regenerator firebox/fire tubes	No
Emissions vented to flare or regenerator firebox/fire tubes
Total CO2 Emissions (mt CO2) [98.236(e)(2)(iv)(B)] [98.236(e)(2)(v)(A)]	11.8574076
Total CH4 Emissions (mt CH4) [98.236(e)(2)(iv)(C)] [98.236(e)(2)(v)(B)]	0.0845568
Total N2O Emissions (mt N2O) [98.236(e)(2)(iv)(D)]	0
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)]	0.506538
Total CH4 Emissions (mt CH4) [98.236(e)(2)(iv)(C)] [98.236(e)(2)(v)(B)]	4.22784

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)]	TX DEHY1
County and State [98.236(e)(1)(xviii)]	GALVESTON, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.45
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	33.26
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.18
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)]	0.1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	500
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01277
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.90472
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)]	0.4824882
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	4.0361566
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY2
County and State [98.236(e)(1)(xviii)]	ORANGE, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	24.05
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.75
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	61
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	636
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00272
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.87379
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)]	210.4237551
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.8998841
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0003591
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)]	0.1265981
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.3673815
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY3
County and State [98.236(e)(1)(xviii)]	FORT BEND, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	47.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.54
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)]	1.86
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	720
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00799
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.84296
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)]	0.9201218
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0581951
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY4
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
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)]	54.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.66
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.1
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)]	8784
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)]	740
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	0.8501876
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	6.1002055
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY5
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
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)]	27.26
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.86
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	1012
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	0.8205201
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.5617184
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY6
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
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)]	99.76
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	3.87
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	120
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1020
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	235.1292831
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	1.327419
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0005131
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)]	TX DEHY7
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
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)]	39.09
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.27
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	2.5851597
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0066821
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000043
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)]	TX DEHY8
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.978
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.35
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.18
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	770
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	7.928371
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	54.3542204
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY9
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.978
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.35
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.18
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	770
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	7.928371
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	54.3542204
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY10
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.99
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	45.66
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.54
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)]	8784
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)]	860
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	8.2353909
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	59.6873947
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY11
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
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)]	25.99
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.81
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	820
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	0.7738034
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.4583578
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY12
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.13
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.84
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.34
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)]	0.5
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	780
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	3.5292341
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	24.37404
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY13
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	29.99
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.04
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)]	0.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	770
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	0.1719892
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.1193758
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY14
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	39.88
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.32
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	740
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	7.6093104
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	51.933594
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY15
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	56.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.98
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)]	8784
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)]	600
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	3.4458271
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0077128
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000056
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)]	TX DEHY16
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	38.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.28
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)]	8784
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)]	600
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	175.1305109
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.8468529
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0003439
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)]	TX DEHY17
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	39.72
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.32
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	605
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	0
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.8561479
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.5606458
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY18
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.84
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.14
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.02
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	835
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	10.4227731
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	71.8991982
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY19
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.84
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.14
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.02
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	835
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	10.4227731
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	71.8991982
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY20
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.85
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	46.61
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.01
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	605
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	0.2656628
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.1890767
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY21
County and State [98.236(e)(1)(xviii)]	HIDALGO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.12
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.37
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	1089
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00131
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92197
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)]	0.0854771
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.7656837
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY22
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	45.82
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.71
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)]	8784
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)]	670
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.001849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	6.9236454
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	46.992809
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY23
County and State [98.236(e)(1)(xviii)]	HIDALGO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.8
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	43.27
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.41
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	1010
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00131
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92197
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)]	0.0853847
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.7152835
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY24
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	44.79
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.72
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)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	780
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	7.7612748
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	54.748443
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY25
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.854
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	28.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.95
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)]	1.8
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	830
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	14.0928735
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	96.1883586
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY26
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.854
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	28.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.95
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)]	1.8
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	830
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	14.0928735
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	96.1883586
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY27
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.8
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.2720304
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0059004
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000025
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)]	TX DEHY28
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.722
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.8
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.2720304
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0059004
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000025
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)]	TX DEHY29
County and State [98.236(e)(1)(xviii)]	WEBB, TX
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)]	25.36
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.82
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)]	2.8
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	710
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0209
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.91683
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	Yes
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	19.2062769
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0324684
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000285
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)]	TX DEHY30
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	5.69
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.92
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.2614748
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0058573
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000025
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)]	TX DEHY31
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	43.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.17
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	665
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	8.3766268
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	56.9421774
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY32
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	43.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.17
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	665
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	8.3914767
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	57.0159461
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY33
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	43.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.17
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	665
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	8.3766268
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	56.9421774
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY34
County and State [98.236(e)(1)(xviii)]	ZAPATA, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	43.28
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.17
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)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	665
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.01849
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94534
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)]	8.3766268
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	56.9421774
Unit ID or Name [98.236(e)(1)(i)]	TX DEHY35
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.336
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.4
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.2213429
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0056866
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000024
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)]	TX DEHY36
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.007
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.49
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.216465
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0056686
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000024
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)]	TX DEHY37
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.203
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.52
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)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	1.216463
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0056686
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000024
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)]	TX DEHY38
County and State [98.236(e)(1)(xviii)]	REFUGIO, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	11.144
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.86
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.77
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)]	2.8
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
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)]	1050
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00425
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.97287
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	3.213244
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.0149036
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000064
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)]	TX DEHY39
County and State [98.236(e)(1)(xviii)]	WEBB, TX
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	24
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	32.67
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.63
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)]	1.63
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	71
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	660
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0209
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.91683
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)]	419.2182556
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.4106961
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.000883
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)]	5.1751997
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.2341605
Unit ID or Name [98.236(e)(1)(i)]	LA DEHY1
County and State [98.236(e)(1)(xviii)]	ST MARY, LA
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	8.3664688
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.73
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.6
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)]	8720
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)]	760
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02023
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.091897
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)]	492.1529362
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	2.7236811
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0010173
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)]	LA DEHY2
County and State [98.236(e)(1)(xviii)]	VERMILION, LA
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.2894411
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	34.66
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.79
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)]	0.27
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)]	6528
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)]	900
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02175
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93775
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)]	42.4620589
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.2479064
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0000904
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)]	LA DEHY3
County and State [98.236(e)(1)(xviii)]	CAMERON, LA
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.974484
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	45.94
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.9
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)]	0.33
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)]	7583
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)]	1152
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.00744
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.915
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)]	1.091572
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	21.6257133

BlowdownVentStacksDetails:

mt CO2	0.5
mt CH4	8.62
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)]	12
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.5199225
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	8.6210376

AtmosphericTanksDetails:

mt CO2	9.4
mt CH4	173.23
mt N2O	0.000
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?	Yes
Was Calculation Method 1 used to calculate emissions [(98.233(j)(1)]?	Yes
Was Calculation Method 2 used to calculate emissions [(98.233(j)(2)]?	No
Was Calculation Method 3 used to calculate emissions [(98.233(j)(3)]?	Yes
If Calculation Method 1 or 2 were used, were any atmospheric tanks observed to have malfunctioning dump valves during the calendar year?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

AtmosphericTanksCalculationMethodOneOrTwoSubBasinRowDetails:

County and State [98.236(j)(1)(i)]	CAMERON, LA
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	150
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	75
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	43.425
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	10
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.243846
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.529731
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.007355
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.1388501
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	6.6117091
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	66313.67
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	10
County and State [98.236(j)(1)(i)]	WEBB, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	52.390321
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	16
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.4719936
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	14.6958173
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	151683.39
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	16
County and State [98.236(j)(1)(i)]	WHARTON, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	57.608
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	4
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0563731
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	1.7552109
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	18116.47
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	4
County and State [98.236(j)(1)(i)]	FORT BEND, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	52.6028571
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	46
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.1827128
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	5.6888778
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	58717.95
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	46
County and State [98.236(j)(1)(i)]	DUVAL, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	28.92
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	14
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.202404
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	6.3019765
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	65046.07
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	14
County and State [98.236(j)(1)(i)]	JEFFERSON, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	42.7222222
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	26
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.089494
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	2.7864519
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	28760.46
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	26
County and State [98.236(j)(1)(i)]	GALVESTON, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	40.1885
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	12
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.2212876
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	6.8899288
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	71114.64
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	12
County and State [98.236(j)(1)(i)]	HIDALGO, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	52.487
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	29
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.1508258
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	4.6960554
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	48470.5
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	32
County and State [98.236(j)(1)(i)]	SAN JACINTO, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	50.1272727
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	9
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0360351
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	1.1219765
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	11580.52
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	9
County and State [98.236(j)(1)(i)]	BRAZORIA, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	53.3097561
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	18
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.2456352
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	7.6480079
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	78939.18
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	18
County and State [98.236(j)(1)(i)]	STARR, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	45.1380952
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	11
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.1420418
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	4.4225612
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	45647.62
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	11
County and State [98.236(j)(1)(i)]	KENEDY, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	45.6136364
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	2
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0725778
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	2.2597569
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	23324.16
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	2
County and State [98.236(j)(1)(i)]	ARANSAS, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	57.8125
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	10
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0781475
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	2.4331711
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	25114.06
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	10
County and State [98.236(j)(1)(i)]	REFUGIO, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	39.2161616
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	61
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	3.0322186
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	94.4100363
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	974456.48
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	61
County and State [98.236(j)(1)(i)]	ORANGE, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	47.175
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	7
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.32959
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0.329594
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0.00386
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0.003864
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0.0550189
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	1.7130485
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	17681.29
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	7
County and State [98.236(j)(1)(i)]	MATAGORDA, TX
Select Calculation Method Used (Select from list) [98.236(j)(1)(ii)]	Calculation Methodology 1
Name of software package used for Calculation Method 1 [98.236(j)(1)(ii)]	E&P Tanks 2.0
Average gas-liquid separator or non-separator equipment temperature (°F) [98.236(j)(1)(iv)]	77
Average gas-liquid separator or non-separator equipment pressure (psig) [98.236(j)(1)(v)]	32.5
Average sales oil or stabilized oil API gravity (degrees) [98.236(j)(1)(vi)]	0
Count of tanks that vented directly to the atmosphere [98.236(j)(1)(xiii)(A)]	3
Minimum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0
Maximum concentration of CH4 in flash gas (mole fraction) [98.236(j)(1)(viii)]	0
Minimum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]]	0
Maximum concentration of CO2 in flash gas (mole fraction) [98.236(j)(1)(vii)]	0
Annual CO2 emissions from venting (mt CO2) [98.236(j)(1)(xiii)(B)]	0
Annual CH4 emissions from venting (mt CH4) [98.236(j)(1)(xiii)(C)]	0
Total volume of oil sent to tanks from all gas-liquid separators and direct from wells or non-separator equipment (bbl per yr) [98.236(j)(1)(iii)]	0
Were any emissions from atmospheric tanks controlled with vapor recovery systems? [98.236(j)(1)(xii)]	No
Were any emissions from atmospheric tanks vented directly to the atmosphere? [98.236(j)(1)(xiii)(A)]	Yes
Were any emissions from atmospheric tanks vented to flare(s)? [98.236(j)(1)(xiv)]	No
Count of atmospheric tanks [98.236(j)(1)(x)]	3

AtmosphericTanksCalculationMethodThreeRowDetails:

Estimate of fraction of oil/condensate throughput sent to tanks in basin with flaring [98.236(j)(2)(i)(B)]	0
Estimate of fraction of oil/condensate throughput sent to tanks with vapor recovery system control measures [98.236(j)(2)(i)(C)]	0
Count of atmospheric tanks in basin [98.236(j)(2)(i)(D)]	77
Total annual oil/condensate throughput that is sent to all atmospheric tanks (barrels per year) [98.236(j)(2)(i)(A)]	44324.07

AtmosphericTanksCalcMethodThreeNoFlaringRowDetails:

County and State [98.236(j)(2)(ii)(A)]	JEFFERSON, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	14
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0
County and State [98.236(j)(2)(ii)(A)]	JIM HOGG, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	3
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0
County and State [98.236(j)(2)(ii)(A)]	ZAPATA, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	22
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	1.91464
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	4.39296
County and State [98.236(j)(2)(ii)(A)]	WEBB, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	5
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.58912
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	1.35168
County and State [98.236(j)(2)(ii)(A)]	SAN JACINTO, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	2
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.14728
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0.33792
County and State [98.236(j)(2)(ii)(A)]	DUVAL, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	2
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0
County and State [98.236(j)(2)(ii)(A)]	BROOKS, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	11
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.7364
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	1.6896
County and State [98.236(j)(2)(ii)(A)]	MATAGORDA, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	16
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.7364
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	1.6896
County and State [98.236(j)(2)(ii)(A)]	ORANGE, TX
Count of tanks that did not control emissions with flares [98.236(j)(2)(ii)(B)]	2
Annual CO2 emissions from tanks without flares (mt CO2) [98.236(j)(2)(ii)(C)]	0.14728
Annual CH4 emissions from tanks without flares (mt CH4) [98.236(j)(2)(ii)(D)]	0.33792

FlareStacksDetails:

mt CO2	257.1
mt CH4	1.56
mt N2O	0.001
Did the facility have flare stacks subject to reporting under 98.232 [98.236(n)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

UniqueFlareStacksRowDetails:

Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	LAFLARE1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	168336
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.91897
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.02023
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	9.4679186
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.0594032
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000208
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	LAFLARE2
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	177912
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.90898
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.05462
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	9.708105
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.0620999
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.000022
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE1
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE2
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE3
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE4
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE5
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE6
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	3091968
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.8129187
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.006322
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE7
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE8
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE9
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE10
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE11
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE12
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE13
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE14
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE15
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE16
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE17
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	184464
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.92197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.00131
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE18
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	4339296
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.8358246
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0352913
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE19
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	229701.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.8278382
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0593465
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE20
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	2968992
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.8000751
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0422855
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE21
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	415483.2
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.6128366
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.1712814
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	TXFLARE22
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	7334640
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.98
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.8791058
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0415616
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	10.8131296
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.065307
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0.0000228

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	0.4
mt CH4	2.55
Did the facility have any reciprocating compressors subject to reporting under 98.232 [98.236(p)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Total annual Reciprocating Compressor emissions CO2 Emissions (mt CO2) [98.236(p)(5)(ii)]	0.3880828
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	2.548224
Count of Reciprocating Compressors [98.236(p)(5)(i)]	14

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	144.2
mt CH4	1124.64
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?	Yes
Did this facility use population counts to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(r)]?	Yes
Did the facility elect to comply with 98.236(q) according to 98.233(q)(1)(iv) for any components at the facility [per 98.236(q)(1)(iv)]?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Number of complete equipment leak surveys performed during the calendar year [98.236(q)(1)(i)]	20
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)]	4
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2328
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0472464
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.7801942
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)]	2
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2160
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0177945
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.2924673
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)]	2280
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0029778
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.0489427
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)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2256
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0067217
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.111455
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)]	4
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2196
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0403734
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.6652921
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)]	14
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2173.7142857
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.1394694
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	2.2972101
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)]	41950
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8735.2609297
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	85.468136
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	665.53743
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)]	134066
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8741.3603747
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	38.4230191
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	299.0165647
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)]	6536
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8766.0373317
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	3.4298189
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	26.646334
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)]	2568
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8734.7352025
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	8.3463354
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	64.9840475
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)]	1038.337
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)]	8.2912441
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	64.2634425
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Unprotected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Plastic/composite gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Cast iron gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0

MajorGasEquipmentTypeRowDetails:

Major Equipment Type [98.236(r)(3)(ii)]	Wellhead
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Separators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	994
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)]	416
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)]	14
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)]	6
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)]	51

CombustionEmissionsDetails:

mt CO2	32450.6
mt CH4	0.61
mt N2O	0.061
Did the Facility have combustion units subject to reporting under 98.232?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Are there external fuel combustion units with a rated heat capacity less than or equal to 5 mmBtu/hr? [98.236(z)(1)(i)]	Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity less than or equal to 1 mmBtu/hr? [98.236(z)(1)(i)]	No
Total number of combustion units meeting 98.236(z)(1) descriptions	58
Are there external fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr? [98.236(z)(2)(i)]	No
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr? [98.236(z)(2)(i)]	No
Are there Internal fuel combustion units of any heat capacity that are compressor-drivers? [98.236(z)(2)(i)]	Yes

LargeCombustionUnitEmissionsRowDetails:

Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas (pipeline quality)
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	596084.1091618
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	32450.5566258
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	0.6115823
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.0611582