Address: 10691 East Carter Rd, Suite 201
City: Traverse City
State: MI
Postal Code: 49684

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):298,808.8
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:211130
Second Primary NAICS Code:

Parent Company Details:

Subpart W: Petroleum and Natural Gas Systems

SubpartWSummaryDetails:

Industry Segment Number	9
Industry Segment Name	Onshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)	190020.5
Total CO2e Emissions (mt CO2e)	298808.8
Total Reported CH4 Emissions (mt CH4)	4346.30
Total Reported N2O Emissions (mt N2O)	0.439

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)	1346.7
Total Reported CH4 Emissions (mt CH4)	3481.84
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	87.5
Total Reported CH4 Emissions (mt CH4)	226.27
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)	544.7
Total Reported CH4 Emissions (mt CH4)	79.96
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)	83.7
Total Reported CH4 Emissions (mt CH4)	216.52
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2.1
Total Reported CH4 Emissions (mt CH4)	14.02
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)	14.6
Total Reported CH4 Emissions (mt CH4)	37.75
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)	187941.1
Total Reported CH4 Emissions (mt CH4)	289.95
Total Reported N2O Emissions (mt N2O)	0.439

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	305 - Michigan Basin
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	24445398
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)]	19091426
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	1346.7
mt CH4	3481.84
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)]	1795
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	1339.8905304
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	3464.355744
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)]	88
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	6.7634544
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	17.4872586
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	87.5
mt CH4	226.27
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)]	119
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)]	87.512421
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	226.2678566

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	544.7
mt CH4	79.96
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)]?	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)]	5
Vapor Recovery	No
Dehydrator vents to flares or regenerator firebox/fire tubes	No
Control devices other than vapor recovery, flare or regenerator firebox/fire tubes	No
Emissions vented to flare or regenerator firebox/fire tubes
Emissions that were not vented to a flare or regenerator firebox/fire tubes
Total CO2 Emissions (mt CO2) [98.236(e)(2)(iv)(B)] [98.236(e)(2)(v)(A)]	0.84423
Total CH4 Emissions (mt CH4) [98.236(e)(2)(iv)(C)] [98.236(e)(2)(v)(B)]	7.0464

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)]	Comstock Hills
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.75663
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	24.61
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)]	0.3
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1087
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13793
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.86009
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)]	14.344212
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.1210869
Unit ID or Name [98.236(e)(1)(i)]	Doctors Club
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.9964
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	12.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.44
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)]	0.3
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	51
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1076
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.12263
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.82562
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)]	14.7415586
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.987368
Unit ID or Name [98.236(e)(1)(i)]	Hubbard Lake
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.0259
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	23.2
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)]	0.1334
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	71
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1054
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06472
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.89894
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)]	3.035728
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9650623
Unit ID or Name [98.236(e)(1)(i)]	Lost Lake Woods
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.38047
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.68
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.16
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)]	0.1334
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1077
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.1171
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.88013
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)]	4.8476284
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9205196
Unit ID or Name [98.236(e)(1)(i)]	Mt Maria
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.01928
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	7.49
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.22
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	38
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1108
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07067
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.90642
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.4039137
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.2217047
Unit ID or Name [98.236(e)(1)(i)]	North Bay
County and State [98.236(e)(1)(xviii)]	ALCONA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.2205323
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	9.26
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.28
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)]	0.338
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	43
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1106
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.14005
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85112
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)]	20.5825535
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.3664802
Unit ID or Name [98.236(e)(1)(i)]	Blue Herron
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.220832
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	13.93
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.48
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	54
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1086
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.16483
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.83489
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)]	10.6886233
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1185579
Unit ID or Name [98.236(e)(1)(i)]	Brady Bunch
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.985667
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	12.38
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.4
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	51
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1064
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.12197
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.87747
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)]	8.1456051
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1639171
Unit ID or Name [98.236(e)(1)(i)]	Broad
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.3684
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	23.54
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.85
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)]	0.3
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)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1075
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.17082
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.82752
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)]	17.7613927
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.0212967
Unit ID or Name [98.236(e)(1)(i)]	Carbon Black
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.22363
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	14.85
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.52
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	56
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1066
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.15333
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.84647
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	9.8144608
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1293534
Unit ID or Name [98.236(e)(1)(i)]	Dubie Brothers
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.504
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	9.52
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.28
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	44
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1077
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.09562
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.90151
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)]	6.8343614
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1991158
Unit ID or Name [98.236(e)(1)(i)]	Flint Nappers
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.15674
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	37.44
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.83
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	87
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1123
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07853
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.91798
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)]	4.1721392
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.257357
Unit ID or Name [98.236(e)(1)(i)]	Head Start
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.164874
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	13.02
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.43
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	52
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1053
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.14701
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85277
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	9.6555222
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1248174
Unit ID or Name [98.236(e)(1)(i)]	Highway 65
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
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)]	20.38
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.68
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)]	0.338
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)]	4176
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	66
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1082
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13965
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85934
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)]	17.0064341
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.3685667
Unit ID or Name [98.236(e)(1)(i)]	Minke Coat
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.67856
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	13.29
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.42
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	54
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1084
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06893
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92485
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)]	4.6092205
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.2345867
Unit ID or Name [98.236(e)(1)(i)]	Mother Hubbard
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.53422
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	21.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.71
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	68
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1106
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.10924
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.89007
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)]	6.5959534
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.22742
Unit ID or Name [98.236(e)(1)(i)]	Schmitt Creek
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.5214
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)]	0.94
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)]	0.375
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	74
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1078
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.09985
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.89657
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)]	12.7548256
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.7107565
Unit ID or Name [98.236(e)(1)(i)]	Scott Creek
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.9458
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	15.16
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.47
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)]	0.375
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	57
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1074
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13218
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.86692
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)]	19.0726364
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.6282935
Unit ID or Name [98.236(e)(1)(i)]	Thunder Bay North
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.1
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	19.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.71
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)]	0.1667
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)]	6048
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)]	1062
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06591
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9303
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)]	3.9734659
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.2173502
Unit ID or Name [98.236(e)(1)(i)]	Thunder Bay South
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.9617
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.39
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.45
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)]	0.15
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	86
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1126
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.08409
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.90401
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)]	4.0132006
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0903444
Unit ID or Name [98.236(e)(1)(i)]	Timber Wolf
County and State [98.236(e)(1)(xviii)]	ALPENA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.66339
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	19.27
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.65
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1101
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.10686
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.89275
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)]	6.5959534
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.2223397
Unit ID or Name [98.236(e)(1)(i)]	Chess Play
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.9767
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	15.5
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.52
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	56
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	942
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06929
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92516
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)]	4.1324046
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0932474
Unit ID or Name [98.236(e)(1)(i)]	Custer 33 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.61893
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.44
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)]	0.375
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1042
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13424
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.78788
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)]	16.8077608
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	2.3370874
Unit ID or Name [98.236(e)(1)(i)]	Forest Home 10 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.27227
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	26.92
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.51
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	73
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	942
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04127
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.95672
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.1456716
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0977834
Unit ID or Name [98.236(e)(1)(i)]	Jordan 12 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.1797
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	16.85
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.6
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	59
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	956
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04291
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9507
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.5390447
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1313492
Unit ID or Name [98.236(e)(1)(i)]	Lakes of the North
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.35644
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	20.99
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.2
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)]	0.125
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	977
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13718
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.84735
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.7615256
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.7641211
Unit ID or Name [98.236(e)(1)(i)]	Mancelona 8 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.112
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	20.54
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.5
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)]	0.109
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	64
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	970
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.1529
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.8183
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.5628523
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.6319444
Unit ID or Name [98.236(e)(1)(i)]	Warner 10 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.64977
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.02
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.03
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	944
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.06923
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.92383
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)]	3.3536052
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0691163
Unit ID or Name [98.236(e)(1)(i)]	Warner 27 CPF
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.19009
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	19.26
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.72
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	62
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	931
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.09209
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.90682
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.2052404
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0623125
Unit ID or Name [98.236(e)(1)(i)]	Warner 36
County and State [98.236(e)(1)(xviii)]	ANTRIM, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.80266
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	42.64
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.9
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	86
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	902
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.1265
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.8721
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.7615256
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9969952
Unit ID or Name [98.236(e)(1)(i)]	Fred 10
County and State [98.236(e)(1)(xviii)]	CRAWFORD, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.3175
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	20.15
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.96
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	64
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1003
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.1386
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.7846
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)]	7.9469318
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.986109
Unit ID or Name [98.236(e)(1)(i)]	Clearwater Central CPF
County and State [98.236(e)(1)(xviii)]	KALKASKA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.0025
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	28.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.52
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	76
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1028
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05294
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.88942
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.8489751
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1113004
Unit ID or Name [98.236(e)(1)(i)]	Bear Lake 29 CPF
County and State [98.236(e)(1)(xviii)]	MANISTEE, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.65538
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	63.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	3.03
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	86
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	530
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.07977
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85978
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.388053
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.6033681
Unit ID or Name [98.236(e)(1)(i)]	Chief Creek CPF
County and State [98.236(e)(1)(xviii)]	MANISTEE, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.93177
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	72.54
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	4.54
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	95
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	626
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05873
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.85506
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)]	1.867529
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.6880083
Unit ID or Name [98.236(e)(1)(i)]	Arthur Miller CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.02544
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	19.91
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.73
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1041
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.10243
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.89529
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)]	6.0794029
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1606512
Unit ID or Name [98.236(e)(1)(i)]	Briley 34
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.28314
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.95
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)]	0.25
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	83
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1103
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.2633
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.712
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)]	20.5030841
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.459024
Unit ID or Name [98.236(e)(1)(i)]	Connie Stevens East CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.381
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.46
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.02
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1216
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.28607
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.69982
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)]	16.0528023
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0507005
Unit ID or Name [98.236(e)(1)(i)]	Fosters Lager CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.58254
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	14.2
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.44
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	49
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)]	0.05481
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9409
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.9443382
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9015595
Unit ID or Name [98.236(e)(1)(i)]	Gilchrist
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.233533
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	17.4
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.74
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)]	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)]	1085
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.19652
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.69166
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)]	7.231708
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.574066
Unit ID or Name [98.236(e)(1)(i)]	King Edwards CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.534567
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	21.38
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.71
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	67
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1073
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.1691
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.8309
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)]	10.0131341
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1297162
Unit ID or Name [98.236(e)(1)(i)]	Loud 15 CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.5178
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.38
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)]	0.334
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	74
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1120
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.2737
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.6625
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)]	30.6751569
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.8944723
Unit ID or Name [98.236(e)(1)(i)]	Miller Creek CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.99135
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	29.87
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.24
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	77
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1051
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.18673
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.81293
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)]	10.0528688
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0778253
Unit ID or Name [98.236(e)(1)(i)]	North Hardwood CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.64169
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	8.89
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.25
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	33
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1061
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.26767
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.72491
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)]	21.1785734
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.0040823
Unit ID or Name [98.236(e)(1)(i)]	Rust Road CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.554805
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	25.61
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.89
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1074
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.22715
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.77263
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)]	12.8342949
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0646711
Unit ID or Name [98.236(e)(1)(i)]	Scenic CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.829832
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	39.66
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.75
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1037
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.2797
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.71045
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)]	13.9071307
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9501845
Unit ID or Name [98.236(e)(1)(i)]	Webber Creek CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.45186
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	9.8
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.29
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	43
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1062
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.22162
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.77777
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	9.2581756
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.6322165
Unit ID or Name [98.236(e)(1)(i)]	West Albert 11
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.5614
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	20.83
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1
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)]	0.117
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1001
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.11491
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.72894
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)]	4.5694858
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.6534446
Unit ID or Name [98.236(e)(1)(i)]	West Albert 31
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.1867
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	33.3
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.1
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	84
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1052
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0432
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.8214
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)]	0.2034415
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9904635
Unit ID or Name [98.236(e)(1)(i)]	X-Rea CPF
County and State [98.236(e)(1)(xviii)]	MONTMORENCY, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.63977
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	18.64
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.62
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	62
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1040
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.18899
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.81101
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)]	11.3243779
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0751945
Unit ID or Name [98.236(e)(1)(i)]	Elmers Glewoll CPF
County and State [98.236(e)(1)(xviii)]	OSCODA, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.96194
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	32.17
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)]	0.1667
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1070
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.11663
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.73058
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)]	6.2383415
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0027105
Unit ID or Name [98.236(e)(1)(i)]	Bagley 30 CPF
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.5101
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	26.98
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.24
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	72
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	992
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.24119
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.75108
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)]	12.8342949
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.952271
Unit ID or Name [98.236(e)(1)(i)]	Chester 1
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.78497
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	8.97
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.27
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)]	0.134
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	40
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	921
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.08285
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.91117
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)]	4.4900165
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.8486706
Unit ID or Name [98.236(e)(1)(i)]	Chester 7
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.769067
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	70.84
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	4.04
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	104
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	963
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.27309
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.71828
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)]	11.4038472
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.8959349
Unit ID or Name [98.236(e)(1)(i)]	Chester 12 Fox
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.16036
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	41.84
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.16
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	88
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	995
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.08521
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.91301
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)]	4.0926699
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.1215516
Unit ID or Name [98.236(e)(1)(i)]	Chester 22
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.01747
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	21.44
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.79
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	65
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	971
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.17899
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.7786
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)]	10.0131341
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9723198
Unit ID or Name [98.236(e)(1)(i)]	Dover 36
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.63758
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	7.04
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.2
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)]	0.134
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	33
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	995
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.21751
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.78003
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)]	12.7548256
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.8110225
Unit ID or Name [98.236(e)(1)(i)]	Elmira 23 CPF
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.116172
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	33.18
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.15
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1003
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13614
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.86169
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)]	6.9933
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.360776
Unit ID or Name [98.236(e)(1)(i)]	Elmira 34
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	0.558391
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	42.05
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.67
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	889
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.14946
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.84862
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)]	6.7946267
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9711405
Unit ID or Name [98.236(e)(1)(i)]	Hayes 29
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.9
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	9.39
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	0.35
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)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	41
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	957
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.13533
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.78645
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	5.4436483
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.5805978
Unit ID or Name [98.236(e)(1)(i)]	Hayes 34
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.266
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	24.93
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.84
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)]	0.1405
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1010
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.2285
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.7664
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)]	10.4104807
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.8010435
Unit ID or Name [98.236(e)(1)(i)]	Mossback
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	1.18911
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	40.18
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	2.05
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	85
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	913
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.05294
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9443
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.4635489
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0698421
Unit ID or Name [98.236(e)(1)(i)]	Old Vandy North CPF
County and State [98.236(e)(1)(xviii)]	OTSEGO, MI
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	3.29797
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.67
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	1.97
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)]	0.167
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	No
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8760
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	73
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	908
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.04246
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.94894
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	No
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	2.1377247
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0390886

BlowdownVentStacksDetails:

mt CO2	83.7
mt CH4	216.52
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)]	Facility piping
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Pipeline venting
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	1
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	83.7431862
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	216.5223064
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)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Scrubbers/strainers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Pig launchers and receivers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Emergency shutdowns
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	All other equipment with a physical volume greater than or equal 50 cubic feet
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0

AtmosphericTanksDetails:

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

FlareStacksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
Did the facility have flare stacks subject to reporting under 98.232 [98.236(n)]?	No

CentrifugalCompressorsDetails:

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

ReciprocatingCompressorsDetails:

mt CO2	2.1
mt CH4	14.02
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)]	2.1344554
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	14.015232
Count of Reciprocating Compressors [98.236(p)(5)(i)]	77

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	14.6
mt CH4	37.75
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?	Yes
Did this facility use population counts to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(r)]?	Yes
Did the facility elect to comply with 98.236(q) according to 98.233(q)(1)(iv) for any components at the facility [per 98.236(q)(1)(iv)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Number of complete equipment leak surveys performed during the calendar year [98.236(q)(1)(i)]	13
Optical gas imaging instrument as specified in §60.18 [98.234(a)(1)]	Yes
Method 21 [98.234(a)(2)]	Yes
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)]	Yes
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)]	2
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	828
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0512181
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.132427
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)]	3
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	520
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0403716
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.1043827
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)]	3
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	224
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0055142
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.0142572
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)]	5
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	427.2
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0377508
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.0976067
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Pressure Relief Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Pump Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0

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)]	Eastern 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)]	6182
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)]	9.2291958
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	23.8625596
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)]	Eastern 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)]	24462
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)]	4.0577409
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	10.4914974
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)]	Eastern 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)]	134
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)]	0.451966
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	1.1685812
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)]	Eastern 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)]	134
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)]	0.2963711
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0.7662828
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)]	Eastern 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 - Unprotected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern 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)]	Eastern 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)]	3.1
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)]	0.4285217
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	1.1079648
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)]	Eastern 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 Eastern US [98.236(r)(3)(ii)(B)]	158
Major Equipment Type [98.236(r)(3)(ii)]	Meters/piping
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	291
Major Equipment Type [98.236(r)(3)(ii)]	Compressors
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	77
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 Eastern US [98.236(r)(3)(ii)(B)]	67

CombustionEmissionsDetails:

mt CO2	187941.1
mt CH4	289.95
mt N2O	0.439
Did the Facility have combustion units subject to reporting under 98.232?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Are there external fuel combustion units with a rated heat capacity less than or equal to 5 mmBtu/hr? [98.236(z)(1)(i)]	Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity less than or equal to 1 mmBtu/hr? [98.236(z)(1)(i)]	Yes
Total number of combustion units meeting 98.236(z)(1) descriptions	67
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 and/or process gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	3553304
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	187941.1064367
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	289.9496064
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.438833