Address: 125 Mercado St., Suite 201
City: Durango
State: CO
Postal Code: 81301

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):504,124.5
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:486210
Second Primary NAICS Code:

Parent Company Details:

Subpart W: Petroleum and Natural Gas Systems

SubpartWSummaryDetails:

Industry Segment Number	9
Industry Segment Name	Onshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)	378875.1
Total CO2e Emissions (mt CO2e)	504124.3
Total Reported CH4 Emissions (mt CH4)	5001.94
Total Reported N2O Emissions (mt N2O)	0.674

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)	342.0
Total Reported CH4 Emissions (mt CH4)	1955.55
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	37.4
Total Reported CH4 Emissions (mt CH4)	143.70
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	794.7
Total Reported CH4 Emissions (mt CH4)	2548.91
Total Reported N2O Emissions (mt N2O)	0.000
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)	4.1
Total Reported CH4 Emissions (mt CH4)	22.17
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	11.9
Total Reported CH4 Emissions (mt CH4)	0.54
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2.4
Total Reported CH4 Emissions (mt CH4)	16.10
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)	80.1
Total Reported CH4 Emissions (mt CH4)	308.23
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)	377602.6
Total Reported CH4 Emissions (mt CH4)	6.74
Total Reported N2O Emissions (mt N2O)	0.674

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	580 - San Juan Basin
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	119137421
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)]	105279955
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	0
Quantity of all hydrocarbon liquids transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iv)]	0

PneumaticDeviceVentingDetails:

mt CO2	342.0
mt CH4	1955.55
Did the Facility have any continuous high-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	No
Did the Facility have any intermittent bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	Yes
Did the Facility have any continuous low-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

PneumaticDeviceTypesRowDetails:

Type of Pneumatic Device	High-bleed Pneumatic Devices
Type of Pneumatic Device	Intermittent Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	700
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	261.3
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	1494.05
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8760
Type of Pneumatic Device	Low-Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	2100
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	80.7
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	461.5
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8760

NaturalGasDrivenPneumaticPumpsDetails:

mt CO2	37.4
mt CH4	143.70
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)]	70
Average estimated number of hours in the calendar year that the natural gas driven pneumatic pumps were operated, T (hours) [98.236(c)(2)]	8760
Total CO2 Emissions (mt CO2) [98.236(c)(3)]	37.4
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	143.7

AcidGasRemovalUnitsDetails:

mt CO2	0.0
Did the Facility have any acid gas removal units that vent directly to the atmosphere, to a flare or engine, or to a sulfur recovery plant subject to reporting under 98.232 [98.236(d)]?	No

DehydratorsDetails:

mt CO2	794.7
mt CH4	2548.91
mt N2O	0.000
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs greater than or equal to 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	Yes
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs less than 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	No
Did the facility have any desiccant dehydrators subject to reporting under 98.232 [98.236(e)]?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

SmallGlycolDehydrators:

Emissions vented to flare or regenerator firebox/fire tubes

Emissions that were not vented to a flare or regenerator firebox/fire tubes

DessicantDehydrators:

Emissions vented to flare or regenerator firebox/fire tubes

Emissions that were not vented to a flare or regenerator firebox/fire tubes

GlycolDehydratorsMoreThanSpecifiedValueRowDetails:

Unit ID or Name [98.236(e)(1)(i)]	ANI_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	83.3
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.8
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	330
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.048062
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.946823
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)]	33.01
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	37.09
Unit ID or Name [98.236(e)(1)(i)]	ANI_X-302
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.7
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	83.3
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.8
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	330
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.048062
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.946823
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)]	33.01
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	37.09
Unit ID or Name [98.236(e)(1)(i)]	ARR_X-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	90.23
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	4.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	370
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	98
Unit ID or Name [98.236(e)(1)(i)]	BON_D-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.25
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	91.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	79.3
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	353.4
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05842
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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)]	14.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	9.05
Unit ID or Name [98.236(e)(1)(i)]	BON_D-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	91.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	79.3
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	353.4
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05842
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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)]	14.9318182
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9636364
Unit ID or Name [98.236(e)(1)(i)]	CAP_S-1700
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	19.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	53.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	60
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	300
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.11
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.86
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)]	31.6
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	67.4545455
Unit ID or Name [98.236(e)(1)(i)]	CAP_S-1800
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	19.6
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	53.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	60
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	300
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.11
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.86
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)]	31.6
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	67.4545455
Unit ID or Name [98.236(e)(1)(i)]	COX_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	15
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	137.5
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	100
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	350
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.17
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.82
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)]	32.3
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	77.6
Unit ID or Name [98.236(e)(1)(i)]	DIA_X-600
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	66.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	76
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	340
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.12
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.87
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)]	38.6
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	73.8
Unit ID or Name [98.236(e)(1)(i)]	EAS_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	6.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	87
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85.4
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	351.6
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	11.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	22
Unit ID or Name [98.236(e)(1)(i)]	ELK_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	17.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	827
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94
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)]	17.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	99.3
Unit ID or Name [98.236(e)(1)(i)]	ELK_X-302
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	17.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	827
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94
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)]	17.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	99.3
Unit ID or Name [98.236(e)(1)(i)]	ELK_X-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	17.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	827
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94
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)]	17.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	99.3
Unit ID or Name [98.236(e)(1)(i)]	HOM_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	13
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	78.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.4
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	99.5
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	323.8
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.08
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9
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)]	8.7
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	20.1
Unit ID or Name [98.236(e)(1)(i)]	JAQ_D1
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	18
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	208
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	1.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	125
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	344
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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)]	6.6
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.6
Unit ID or Name [98.236(e)(1)(i)]	JAQ_D2
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	208
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0
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)]	0
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	125
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	344
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0
Unit ID or Name [98.236(e)(1)(i)]	MID_D1
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	60
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	90
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.5
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	107
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	880
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.95
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	4.2
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	10.9
Unit ID or Name [98.236(e)(1)(i)]	NOR_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.5
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	62.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.2
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	71.3
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	305.6
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.81
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	4.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	4.8
Unit ID or Name [98.236(e)(1)(i)]	OUT_X-708
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	23
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	58.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.4
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	71
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	322
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.98
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	13.9
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	226.9
Unit ID or Name [98.236(e)(1)(i)]	PON_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	22.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	89.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	6.6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	400
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	26.7
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	257.4
Unit ID or Name [98.236(e)(1)(i)]	PUM_X-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	10.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	93.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.2
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	330
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.08
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	17.4
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	0.6
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	No
Unit ID or Name [98.236(e)(1)(i)]	SAM_S-3300
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	29
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	4.4
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	795
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94
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)]	54.2
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	126.5
Unit ID or Name [98.236(e)(1)(i)]	SAM_S-3400
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	29
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	4.4
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	795
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94
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)]	54.2
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	126.5
Unit ID or Name [98.236(e)(1)(i)]	SAW_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	208.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	115
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	350
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	4.4
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	134.4
Unit ID or Name [98.236(e)(1)(i)]	SAW_X-302
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	208.7
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	6
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	115
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	350
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.02
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	4.4
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	134.4
Unit ID or Name [98.236(e)(1)(i)]	SIX_R-4001
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.3
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	139.9
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.5
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)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	97
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	306.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.09
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9
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)]	38.2
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	96.5
Unit ID or Name [98.236(e)(1)(i)]	SOU_D1
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	42
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	89.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	17
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	400
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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)]	35.3
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	8
Unit ID or Name [98.236(e)(1)(i)]	SOU_D2
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	42
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	89.6
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	17
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	400
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.93
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)]	35.3
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	8
Unit ID or Name [98.236(e)(1)(i)]	SPR_X-301
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	20
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	34.9
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	7
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78.6
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	838.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96
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)]	123.4
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	374.8
Unit ID or Name [98.236(e)(1)(i)]	SPR_X-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	12
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	34.9
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.7
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78.6
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	838.7
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.96
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	12.3
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	34.5
Unit ID or Name [98.236(e)(1)(i)]	TRA_X-303
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	9.2
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	54.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.2
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	330
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9
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)]	42.6
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	119.7
Unit ID or Name [98.236(e)(1)(i)]	WOR_D1
County and State [98.236(e)(1)(xviii)]	LA PLATA, CO
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	40
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	94
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.3
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	90
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	350
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.95
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	4.42
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	73.91

BlowdownVentStacksDetails:

mt CO2	4.1
mt CH4	22.17
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)]	338
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	4.1
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	22.17

AtmosphericTanksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?	No

FlareStacksDetails:

mt CO2	11.9
mt CH4	0.54
mt N2O	0.000
Did the facility have flare stacks subject to reporting under 98.232 [98.236(n)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

UniqueFlareStacksRowDetails:

Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	PUM_X-303
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)]	10740729
Flare combustion efficiency (decimal value) [98.236(n)(6)]	0.47
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.00307
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.021
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0
CO2 emissions (mt CO2) [98.236(n)(9)]	11.9
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0.54
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0

CentrifugalCompressorsDetails:

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

ReciprocatingCompressorsDetails:

mt CO2	2.4
mt CH4	16.10
Did the facility have any reciprocating compressors subject to reporting under 98.232 [98.236(p)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Total annual Reciprocating Compressor emissions CO2 Emissions (mt CO2) [98.236(p)(5)(ii)]	2.4
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	16.1
Count of Reciprocating Compressors [98.236(p)(5)(i)]	88

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	80.1
mt CH4	308.23
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?	No
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
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

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)]	9317
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	47.27
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	169.89
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)]	25204
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	17.97
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	64.57
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)]	650
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.84
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	3.04
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)]	541
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	4.38
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	15.74
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)]	740
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	9.6
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	54.99
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)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - 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)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Cast iron gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Western U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8760
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0

MajorGasEquipmentTypeRowDetails:

Major Equipment Type [98.236(r)(3)(ii)]	Wellhead
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Separators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	50
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)]	25
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)]	91
Major Equipment Type [98.236(r)(3)(ii)]	In-line heaters
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Dehydrators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Western US [98.236(r)(3)(ii)(B)]	26

CombustionEmissionsDetails:

mt CO2	377602.6
mt CH4	6.74
mt N2O	0.674
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	110
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)]	Field gas, process gas, and/or natural gas that is not of pipeline quality
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	6564997
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	377602.6088473
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	6.7356869
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.6735687