New Mexico Gas Company - Redonda Compressor Station ... · New Mexico Gas Company - Redonda...

46
New Mexico Gas Company - Redonda Compressor Station Storage Tanks Emission units: Number of Tanks Tanks 4 Used Oil Tank Volume Height (shell) Diameter Throughput 63 5 10 2 bbl ft ft bbl/day Ethylene Glycol Tank Volume 137 Height (shell) 20 Diameter 7 Throughput 4 bbl ft ft bbl/day Uncontrolled Emissions VOCs VOCs 0.075 0.33 lb/hr ton/yr Tanks 4.09d Uncontrolled Emissions VOCs VOCs Negligible Negligible lb/hr ton/yr Tanks 4.09d HAPs HAPs 0.002327626 0.010 lb/hr ton/yr Tanks 4.09d HAPs HAPs 5.8219E-05 2.55E-04 lb/hr ton/yr Tanks 4.09d Wastewater Tank Not a source of air emissions. Mercaptan Tank Pressurized storage vessel. Not a source of air emissions. Pipeline Liquids Tank Volume 47 Height (shell) 10 Diameter 6 Throughput 1 bbl ft ft bbl/day Uncontrolled Emissions VOCs VOCs 0.041 0.179725 lb/hr ton/yr Tanks 4.09d HAPs HAPs 1.8185E-03 0.01 lb/hr ton/yr Tanks 4.09d Emissions Summary HAPs (lb/hr) HAPs (tpy) VOC (lb/hr VOC (tpy) 4.2043E-03 0.02 0.12 0.51

Transcript of New Mexico Gas Company - Redonda Compressor Station ... · New Mexico Gas Company - Redonda...

)

New Mexico Gas Company - Redonda Compressor Station

Storage Tanks

Emission units Number of Tanks

Tanks 4

Used Oil Tank Volume Height (shell) Diameter Throughput

63 5

10 2

bbl ft ft bblday

Ethylene Glycol Tank Volume 137 Height (shell) 20 Diameter 7 Throughput 4

bbl ft ft bblday

Uncontrolled Emissions VOCs VOCs

0075 033

lbhr tonyr

Tanks 409d

Uncontrolled Emissions VOCs VOCs

Negligible Negligible

lbhr tonyr

Tanks 409d

HAPs HAPs 0002327626

0010 lbhr tonyr

Tanks 409d HAPs HAPs

58219E-05

255E-04 lbhr tonyr

Tanks 409d

Wastewater Tank Not a source of air emissions

Mercaptan Tank Pressurized storage vessel Not a source of air emissions

Pipeline Liquids Tank Volume 47 Height (shell) 10 Diameter 6 Throughput 1

bbl ft ft bblday

Uncontrolled Emissions VOCs VOCs

0041 0179725

lbhr tonyr

Tanks 409d

HAPs HAPs 18185E-03

001 lbhr tonyr

Tanks 409d

Emissions Summary

HAPs (lbhr) HAPs (tpy) VOC (lbhr VOC (tpy) 42043E-03 002 012 051

New Mexico Gas Company --Redonda Compressor Station Unit 3 - BaldorGM 20 Electric Generator

EMISSION CALCULATION FOR CO and NOx Rate (lbhr) = Multiply EF (gkW-hr) by Rating (kW) and divide by 4536 to convert g to lb 1 lb = 45360 gm

Uncontrolled Emission Rate

Rating (kW) Emission Factor (EF) Sea Level Emissions 500 hr (lbhr)

(tonyear)

NOX + THC (gkw-hr) CO (gkW-hr) NOx (lbhr) CO (lbhr) NOx (tonyr) CO (tonyr) 3790 722 2947 060 246 015 062

The manufacturer specifies deration rate of 3 every 1000 over 4000 ft Altitude at Redonda is ~5370 ft and a deration of 41 is applied

Derated

Derated Rating Uncontrolled Emission Factor Derated Emission Rate (lbhr)

(kW) Emissions 500hr (tonyear)

NOX + THC (gkw-hr) CO (gkW-hr) NOx (lbhr) CO (lbhr) NOx (tonyr) CO (tonyr) 3635 722 2947 058 236 014 059

Calculations Basis Manufacturers data used for CO and NOx emission factors (see page 13 of 27 in manufacturers data)

Note SO2 VOC and VOC rates from EPA AP42 - Table 32-3

Uncontrolled Emission Factors for 4-Stroke Rich-Burn Engines

Pollutant EF (lbMMBTU) Emission Rate (lbhr) Emission Rate 500hr (tpy)

SO2 0000588 000026 000006

VOC 00296 001298 000325 PM 000991 000435 000109 PM = TSP for this facility and this unit emissions of PM = PM10 = PM25

1 MMBtu = 10200 MMScf (per AP-42) emission rate (lbhr) = (EF lbMMBtu 1020 MMBtuMMScf 377 MMScf year) 8760 hryear

6Fuel consumption = 377 MMScfyr (430 cfhr8760hryr)10 =377 MMcfyr

Fuel Type Pipeline quality natural gas Stack Velocity Calculation Flow Rate 250 cfm Flow Rate 417 cfs diameter 021 ft

Area 003 ft2

Velocity 12223 fts

PM

PM

PM

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

3-Year Average Operating Hours 261 2010 2011 and 2012

3-Year Average Number of Starts 12 2010 2011 and 2013

Engine speed 1200 rpm

Sea level hp 1680 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1611 hp

Potential Emission Calculations

NOx CO VOC SO2 PM25PM10

23 14 025 ghp-hr Mfg data 2001 817 497 09 02 04 lbhr Hourly emission rate

3578 2178 39 09 16 tpy Annual emission rate (8760 hrsyr)

11 06 00 00 00 tpy SSM (assuming 52 30 minute starts per year)

Allowable Emission Calculations

NOx CO VOC SO2 PM25PM10

15 195 015 ghp-hr Catalyst controlled emissions (miratech specs)

20 30 05 ghp-hr Catalyst controlled with safety factor

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

310 470 77 09 16 tpy Annual controlled emission rate (8760 hrsyr)

321 477 77 09 16 tpy Annual emission rate with SSM

Actual Emission Calculations

NOx CO VOC SO2 PM25PM10

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

09 14 02 00 00 tpy Annual emission rate (3-year average)

02 01 00 00 00 tpy Annual emission rate of SSM (3-year ave)

12 15 02 00 00 tpy Annual emission total with SSM (3-year ave)

Sample Calculations

NOx Catalyst controlled emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1611 hp 4536 glb = 71 lbhr

71 lbhr 8760 hrsyr 2000 lbton = 310 tonsyr

CO Catalyst controlled emission factor manufaturer data =195 ghp-hr

195 ghp-hr 155 = 30 ghp-hr (safety factor)

30 ghp-hr 1611 hp 4536 glb = 107 lbhr

107 lbhr 8760 hrsyr 2000 lbton = 470 tonsyr

VOC Catalyst controlled emission factor manufaturer data =025 ghp-hr

025 ghp-hr 23 = 05 ghp-hr (safety factor)

05 ghp-hr 1611 hp 4536 glb = 18 lbhr

18 lbhr 8760 hrsyr 2000 lbton = 77 tonsyr

SO2 Fuel sulfur content 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

000714 lb SMscf 139 (Mscfhr) 64 lb SO232 lb S = 019 lbhr SO2

019 lbhr 8760 hrsyr 2000 lbton = 087 tonsyr

PM 25PM10 AP-42 EF = 0029 lbMMBtu (EF is the sum of PM25 PM10 and PM condensable)

AP-42 EF Heat input = PM lbhr

0029 lbMMBtu 125 MMBtuhr = 036 lbhr

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

Fuel Consumption

Heat Rate 7780 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 125 MMBtuhr Heat Rate hp

Fuel consumption 139 Mscfhr Heat input fuel heat value

Annual fuel usage 1220 MMcfyr 8760 hrsyr operation

Exhaust Parameters

Exhaust temp 1152 deg F Mfg Data

11140 lbhr Mfg Data

Stack diameter 117 ft Mfg Data

Stack height 30 ft Mfg Data

Stack flow 7981 acfm Mfg Data Flow(lbhr)Exhaust Temp(oR)2250

Stack velocity 1245 fts Mfg Data

PM

New Mexico Gas Company -Redonda Compressor Station

Waukesha 7042 GL Emission Unit 1

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model 7042 GL

Type Turbocharged four-cycle lean burn engine

3-Year Average Operating Hours 2458 hrs years 201020112012

Engine speed 1200 rpm

Sea level hp 1478 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1417 hp

Potential Emission Calculations

PM25

NOx CO VOC SO2 PM10

15 265 1 ghp-hr Mfg data

47 83 31 02 01 lbhr Hourly emission rate

62 91 31 02 01 Hourly Emission rate with safety factor

273 399 137 07 05 tpy

SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

PM based on AP-42 EF Heat input = PM lbhr

(EF is the sum of PM25 PM10 and PM condensable)

001 lbMMBtu 103 MMBtuhr = 01 lbhr

Allowable Emission Calculations equal PTE (no controls)

Actual Emission Calculations (three year average 2010-2012)

NOx CO VOC SO2 PM25PM10

62 91 31 02 01 lbhr

77 112 38 02 01 tpy

Sample Calculations

NOx Emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1417 hp 4536 glb = 62 lbhr

62 lbhr 8760 hrsyr 2000 lbton = 273 tonsyr

CO Emission factor manufaturer data =265 ghp-hr

265 ghp-hr 11 = 83 ghp-hr (safety factor)

83 ghp-hr 1417 hp 4536 glb = 91 lbhr

91 lbhr 8760 hrsyr 2000 lbton = 399 tonsyr

VOC Emission factor manufaturer data =10 ghp-hr

10 ghp-hr 1417 hp 4536 glb = 31 lbhr

31 lbhr 8760 hrsyr 2000 lbton = 137 tonsyr

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 133 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 7292 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

New Mexico Gas Company --Redonda Compressor Station Unit 3 - BaldorGM 20 Electric Generator

EMISSION CALCULATION FOR CO and NOx Rate (lbhr) = Multiply EF (gkW-hr) by Rating (kW) and divide by 4536 to convert g to lb 1 lb = 45360 gm

Uncontrolled Emission Rate

Rating (kW) Emission Factor (EF) Sea Level Emissions 500 hr (lbhr)

(tonyear)

NOX + THC (gkw-hr) CO (gkW-hr) NOx (lbhr) CO (lbhr) NOx (tonyr) CO (tonyr) 3790 722 2947 060 246 015 062

The manufacturer specifies deration rate of 3 every 1000 over 4000 ft Altitude at Redonda is ~5370 ft and a deration of 41 is applied

Derated

Derated Rating Uncontrolled Emission Factor Derated Emission Rate (lbhr)

(kW) Emissions 500hr (tonyear)

NOX + THC (gkw-hr) CO (gkW-hr) NOx (lbhr) CO (lbhr) NOx (tonyr) CO (tonyr) 3635 722 2947 058 236 014 059

Calculations Basis Manufacturers data used for CO and NOx emission factors (see page 13 of 27 in manufacturers data)

Note SO2 VOC and VOC rates from EPA AP42 - Table 32-3

Uncontrolled Emission Factors for 4-Stroke Rich-Burn Engines

Pollutant EF (lbMMBTU) Emission Rate (lbhr) Emission Rate 500hr (tpy)

SO2 0000588 000026 000006

VOC 00296 001298 000325 PM 000991 000435 000109 PM = TSP for this facility and this unit emissions of PM = PM10 = PM25

1 MMBtu = 10200 MMScf (per AP-42) emission rate (lbhr) = (EF lbMMBtu 1020 MMBtuMMScf 377 MMScf year) 8760 hryear

6Fuel consumption = 377 MMScfyr (430 cfhr8760hryr)10 =377 MMcfyr

Fuel Type Pipeline quality natural gas Stack Velocity Calculation Flow Rate 250 cfm Flow Rate 417 cfs diameter 021 ft

Area 003 ft2

Velocity 12223 fts

PM

PM

PM

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

3-Year Average Operating Hours 261 2010 2011 and 2012

3-Year Average Number of Starts 12 2010 2011 and 2013

Engine speed 1200 rpm

Sea level hp 1680 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1611 hp

Potential Emission Calculations

NOx CO VOC SO2 PM25PM10

23 14 025 ghp-hr Mfg data 2001 817 497 09 02 04 lbhr Hourly emission rate

3578 2178 39 09 16 tpy Annual emission rate (8760 hrsyr)

11 06 00 00 00 tpy SSM (assuming 52 30 minute starts per year)

Allowable Emission Calculations

NOx CO VOC SO2 PM25PM10

15 195 015 ghp-hr Catalyst controlled emissions (miratech specs)

20 30 05 ghp-hr Catalyst controlled with safety factor

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

310 470 77 09 16 tpy Annual controlled emission rate (8760 hrsyr)

321 477 77 09 16 tpy Annual emission rate with SSM

Actual Emission Calculations

NOx CO VOC SO2 PM25PM10

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

09 14 02 00 00 tpy Annual emission rate (3-year average)

02 01 00 00 00 tpy Annual emission rate of SSM (3-year ave)

12 15 02 00 00 tpy Annual emission total with SSM (3-year ave)

Sample Calculations

NOx Catalyst controlled emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1611 hp 4536 glb = 71 lbhr

71 lbhr 8760 hrsyr 2000 lbton = 310 tonsyr

CO Catalyst controlled emission factor manufaturer data =195 ghp-hr

195 ghp-hr 155 = 30 ghp-hr (safety factor)

30 ghp-hr 1611 hp 4536 glb = 107 lbhr

107 lbhr 8760 hrsyr 2000 lbton = 470 tonsyr

VOC Catalyst controlled emission factor manufaturer data =025 ghp-hr

025 ghp-hr 23 = 05 ghp-hr (safety factor)

05 ghp-hr 1611 hp 4536 glb = 18 lbhr

18 lbhr 8760 hrsyr 2000 lbton = 77 tonsyr

SO2 Fuel sulfur content 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

000714 lb SMscf 139 (Mscfhr) 64 lb SO232 lb S = 019 lbhr SO2

019 lbhr 8760 hrsyr 2000 lbton = 087 tonsyr

PM 25PM10 AP-42 EF = 0029 lbMMBtu (EF is the sum of PM25 PM10 and PM condensable)

AP-42 EF Heat input = PM lbhr

0029 lbMMBtu 125 MMBtuhr = 036 lbhr

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

Fuel Consumption

Heat Rate 7780 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 125 MMBtuhr Heat Rate hp

Fuel consumption 139 Mscfhr Heat input fuel heat value

Annual fuel usage 1220 MMcfyr 8760 hrsyr operation

Exhaust Parameters

Exhaust temp 1152 deg F Mfg Data

11140 lbhr Mfg Data

Stack diameter 117 ft Mfg Data

Stack height 30 ft Mfg Data

Stack flow 7981 acfm Mfg Data Flow(lbhr)Exhaust Temp(oR)2250

Stack velocity 1245 fts Mfg Data

PM

New Mexico Gas Company -Redonda Compressor Station

Waukesha 7042 GL Emission Unit 1

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model 7042 GL

Type Turbocharged four-cycle lean burn engine

3-Year Average Operating Hours 2458 hrs years 201020112012

Engine speed 1200 rpm

Sea level hp 1478 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1417 hp

Potential Emission Calculations

PM25

NOx CO VOC SO2 PM10

15 265 1 ghp-hr Mfg data

47 83 31 02 01 lbhr Hourly emission rate

62 91 31 02 01 Hourly Emission rate with safety factor

273 399 137 07 05 tpy

SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

PM based on AP-42 EF Heat input = PM lbhr

(EF is the sum of PM25 PM10 and PM condensable)

001 lbMMBtu 103 MMBtuhr = 01 lbhr

Allowable Emission Calculations equal PTE (no controls)

Actual Emission Calculations (three year average 2010-2012)

NOx CO VOC SO2 PM25PM10

62 91 31 02 01 lbhr

77 112 38 02 01 tpy

Sample Calculations

NOx Emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1417 hp 4536 glb = 62 lbhr

62 lbhr 8760 hrsyr 2000 lbton = 273 tonsyr

CO Emission factor manufaturer data =265 ghp-hr

265 ghp-hr 11 = 83 ghp-hr (safety factor)

83 ghp-hr 1417 hp 4536 glb = 91 lbhr

91 lbhr 8760 hrsyr 2000 lbton = 399 tonsyr

VOC Emission factor manufaturer data =10 ghp-hr

10 ghp-hr 1417 hp 4536 glb = 31 lbhr

31 lbhr 8760 hrsyr 2000 lbton = 137 tonsyr

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 133 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 7292 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

PM

PM

PM

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

3-Year Average Operating Hours 261 2010 2011 and 2012

3-Year Average Number of Starts 12 2010 2011 and 2013

Engine speed 1200 rpm

Sea level hp 1680 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1611 hp

Potential Emission Calculations

NOx CO VOC SO2 PM25PM10

23 14 025 ghp-hr Mfg data 2001 817 497 09 02 04 lbhr Hourly emission rate

3578 2178 39 09 16 tpy Annual emission rate (8760 hrsyr)

11 06 00 00 00 tpy SSM (assuming 52 30 minute starts per year)

Allowable Emission Calculations

NOx CO VOC SO2 PM25PM10

15 195 015 ghp-hr Catalyst controlled emissions (miratech specs)

20 30 05 ghp-hr Catalyst controlled with safety factor

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

310 470 77 09 16 tpy Annual controlled emission rate (8760 hrsyr)

321 477 77 09 16 tpy Annual emission rate with SSM

Actual Emission Calculations

NOx CO VOC SO2 PM25PM10

71 107 18 02 04 lbhr Hourly emission rate controlled wsafety factor

09 14 02 00 00 tpy Annual emission rate (3-year average)

02 01 00 00 00 tpy Annual emission rate of SSM (3-year ave)

12 15 02 00 00 tpy Annual emission total with SSM (3-year ave)

Sample Calculations

NOx Catalyst controlled emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1611 hp 4536 glb = 71 lbhr

71 lbhr 8760 hrsyr 2000 lbton = 310 tonsyr

CO Catalyst controlled emission factor manufaturer data =195 ghp-hr

195 ghp-hr 155 = 30 ghp-hr (safety factor)

30 ghp-hr 1611 hp 4536 glb = 107 lbhr

107 lbhr 8760 hrsyr 2000 lbton = 470 tonsyr

VOC Catalyst controlled emission factor manufaturer data =025 ghp-hr

025 ghp-hr 23 = 05 ghp-hr (safety factor)

05 ghp-hr 1611 hp 4536 glb = 18 lbhr

18 lbhr 8760 hrsyr 2000 lbton = 77 tonsyr

SO2 Fuel sulfur content 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

000714 lb SMscf 139 (Mscfhr) 64 lb SO232 lb S = 019 lbhr SO2

019 lbhr 8760 hrsyr 2000 lbton = 087 tonsyr

PM 25PM10 AP-42 EF = 0029 lbMMBtu (EF is the sum of PM25 PM10 and PM condensable)

AP-42 EF Heat input = PM lbhr

0029 lbMMBtu 125 MMBtuhr = 036 lbhr

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

Fuel Consumption

Heat Rate 7780 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 125 MMBtuhr Heat Rate hp

Fuel consumption 139 Mscfhr Heat input fuel heat value

Annual fuel usage 1220 MMcfyr 8760 hrsyr operation

Exhaust Parameters

Exhaust temp 1152 deg F Mfg Data

11140 lbhr Mfg Data

Stack diameter 117 ft Mfg Data

Stack height 30 ft Mfg Data

Stack flow 7981 acfm Mfg Data Flow(lbhr)Exhaust Temp(oR)2250

Stack velocity 1245 fts Mfg Data

PM

New Mexico Gas Company -Redonda Compressor Station

Waukesha 7042 GL Emission Unit 1

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model 7042 GL

Type Turbocharged four-cycle lean burn engine

3-Year Average Operating Hours 2458 hrs years 201020112012

Engine speed 1200 rpm

Sea level hp 1478 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1417 hp

Potential Emission Calculations

PM25

NOx CO VOC SO2 PM10

15 265 1 ghp-hr Mfg data

47 83 31 02 01 lbhr Hourly emission rate

62 91 31 02 01 Hourly Emission rate with safety factor

273 399 137 07 05 tpy

SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

PM based on AP-42 EF Heat input = PM lbhr

(EF is the sum of PM25 PM10 and PM condensable)

001 lbMMBtu 103 MMBtuhr = 01 lbhr

Allowable Emission Calculations equal PTE (no controls)

Actual Emission Calculations (three year average 2010-2012)

NOx CO VOC SO2 PM25PM10

62 91 31 02 01 lbhr

77 112 38 02 01 tpy

Sample Calculations

NOx Emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1417 hp 4536 glb = 62 lbhr

62 lbhr 8760 hrsyr 2000 lbton = 273 tonsyr

CO Emission factor manufaturer data =265 ghp-hr

265 ghp-hr 11 = 83 ghp-hr (safety factor)

83 ghp-hr 1417 hp 4536 glb = 91 lbhr

91 lbhr 8760 hrsyr 2000 lbton = 399 tonsyr

VOC Emission factor manufaturer data =10 ghp-hr

10 ghp-hr 1417 hp 4536 glb = 31 lbhr

31 lbhr 8760 hrsyr 2000 lbton = 137 tonsyr

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 133 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 7292 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

New Mexico Gas Company --Redonda Compressor Station

Waukesha L7044 GSI Emission Unit 2

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model L7044 GSI

Type Naturally-aspirated four-cycle rich-burn engine with catalytic converter

Fuel Consumption

Heat Rate 7780 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 125 MMBtuhr Heat Rate hp

Fuel consumption 139 Mscfhr Heat input fuel heat value

Annual fuel usage 1220 MMcfyr 8760 hrsyr operation

Exhaust Parameters

Exhaust temp 1152 deg F Mfg Data

11140 lbhr Mfg Data

Stack diameter 117 ft Mfg Data

Stack height 30 ft Mfg Data

Stack flow 7981 acfm Mfg Data Flow(lbhr)Exhaust Temp(oR)2250

Stack velocity 1245 fts Mfg Data

PM

New Mexico Gas Company -Redonda Compressor Station

Waukesha 7042 GL Emission Unit 1

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model 7042 GL

Type Turbocharged four-cycle lean burn engine

3-Year Average Operating Hours 2458 hrs years 201020112012

Engine speed 1200 rpm

Sea level hp 1478 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1417 hp

Potential Emission Calculations

PM25

NOx CO VOC SO2 PM10

15 265 1 ghp-hr Mfg data

47 83 31 02 01 lbhr Hourly emission rate

62 91 31 02 01 Hourly Emission rate with safety factor

273 399 137 07 05 tpy

SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

PM based on AP-42 EF Heat input = PM lbhr

(EF is the sum of PM25 PM10 and PM condensable)

001 lbMMBtu 103 MMBtuhr = 01 lbhr

Allowable Emission Calculations equal PTE (no controls)

Actual Emission Calculations (three year average 2010-2012)

NOx CO VOC SO2 PM25PM10

62 91 31 02 01 lbhr

77 112 38 02 01 tpy

Sample Calculations

NOx Emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1417 hp 4536 glb = 62 lbhr

62 lbhr 8760 hrsyr 2000 lbton = 273 tonsyr

CO Emission factor manufaturer data =265 ghp-hr

265 ghp-hr 11 = 83 ghp-hr (safety factor)

83 ghp-hr 1417 hp 4536 glb = 91 lbhr

91 lbhr 8760 hrsyr 2000 lbton = 399 tonsyr

VOC Emission factor manufaturer data =10 ghp-hr

10 ghp-hr 1417 hp 4536 glb = 31 lbhr

31 lbhr 8760 hrsyr 2000 lbton = 137 tonsyr

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 133 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 7292 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

PM

New Mexico Gas Company -Redonda Compressor Station

Waukesha 7042 GL Emission Unit 1

Source Description Natural gas-fired reciprocating engine

Manufacturer Waukesha

Model 7042 GL

Type Turbocharged four-cycle lean burn engine

3-Year Average Operating Hours 2458 hrs years 201020112012

Engine speed 1200 rpm

Sea level hp 1478 hp

Elevation 5370 msl

Derate 41 3 per 1000 ft over 4000 ft

Site hp 1417 hp

Potential Emission Calculations

PM25

NOx CO VOC SO2 PM10

15 265 1 ghp-hr Mfg data

47 83 31 02 01 lbhr Hourly emission rate

62 91 31 02 01 Hourly Emission rate with safety factor

273 399 137 07 05 tpy

SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

PM based on AP-42 EF Heat input = PM lbhr

(EF is the sum of PM25 PM10 and PM condensable)

001 lbMMBtu 103 MMBtuhr = 01 lbhr

Allowable Emission Calculations equal PTE (no controls)

Actual Emission Calculations (three year average 2010-2012)

NOx CO VOC SO2 PM25PM10

62 91 31 02 01 lbhr

77 112 38 02 01 tpy

Sample Calculations

NOx Emission factor manufaturer data =15 ghp-hr

15 ghp-hr 133 = 20 ghp-hr (safety factor)

20 ghp-hr 1417 hp 4536 glb = 62 lbhr

62 lbhr 8760 hrsyr 2000 lbton = 273 tonsyr

CO Emission factor manufaturer data =265 ghp-hr

265 ghp-hr 11 = 83 ghp-hr (safety factor)

83 ghp-hr 1417 hp 4536 glb = 91 lbhr

91 lbhr 8760 hrsyr 2000 lbton = 399 tonsyr

VOC Emission factor manufaturer data =10 ghp-hr

10 ghp-hr 1417 hp 4536 glb = 31 lbhr

31 lbhr 8760 hrsyr 2000 lbton = 137 tonsyr

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 133 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 7292 Btuhp-hr Mfg data

Fuel heat value 900 Btuscf Nominal natural gas

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Heat Input 103 MMBtuhr

Fuel consumption 115 Mscfhr

Annual fuel usage 1006 MMcfyr

Exhaust Parameters

Exhaust temp 7250 deg F

147600 lbhr

Exhaust flow 76882 acfm

Stack diameter 117 ft

Exhaust velocity 1192 ftsec

Stack height 45 ft

Heat Rate hp

Heat input fuel heat value

8760 hrsyr operation

Mfg Data

Mfg Data

Flow(lbhr)Exhaust Temp(oR)2275

Design

Exhaust flow stack area

Design

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

New Mexico Gas Company -Redonda Compressor Station

PTE Total - Emission Summary

Potential Emission Calculations (uncontrolled 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

8168 35778 4972 21778 089 389 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105

018

001

-

-

461

077

005

-

-

547

152

007

002

-

PM25

PM10

(lbhr) 010

036

000

-

-

PM25

PM10

(tpy) 045

159

000

-

-

CO2e

(facility

wide tpy)

8850 38628 6119 25891 414 1808 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Allowables Total - Emission Summary

Allowables Emission Calculations (controlled emissions 8760 operating hours)

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy)

623 2730 911 3989 312 1369 016 072

2 7044 GSI

1 7042 GL

709 3103 1073 4702 176 770 020 087

Baldor

3 Emergency

Gen 058 014 236 059 001 000 000 000

Tanks - - - - 012 051 - -

SSM (Unit 2) - 106 - 065 - - - -

105 461 547 010 045

018 077 152 036 159

001 005 007 000 000

- - 002 - -

- - - - -

PM25

PM10

(lbhr)

PM25

PM10

(tpy)

CO2e

(facility

wide tpy)

1390 5954 2220 8815 501 2190 036 159 124 543 708 047 205 136233

Formaldehdye (tpy) and total HAPs come from GRI-HAPCalc 301 Report Tpy is converted to lbhr

Assumes 500 hours of operation per year except for CH20 and HAP which assumes 8760 hours

Total

Actual Total - Emission Summary

Actual Emission Calculations (based on 3-year average operating hours)

PM25 PM25 CO2e

NOx NOx CO CO VOC VOC SO2 SO2 CH2O CH2O HAPs PM10 PM10 (facility

(lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (lbhr) (tpy) (tpy) (lbhr) (tpy) wide tpy)

2459

1 7042 GL 623 766 911 1119 312 384 016 020 105 129 154 010 045 hours

709 092 1073 140 176 023 020 003 018 002 005 036 159 261 hours 2 7044 GSI

Baldor

3 Emergency

Gen 000 000 000 000 000 000 000 000 000 000 000 000 000 0 hrs

Tanks - - - - 012 051 - - - - 002 - -

1332 859 1984 1260 500 458 036 023 123 132 160 42301

Emissions are provided for informational purposes only and are not intended to be an enforceable limit Total

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

-

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

NMGC--Redonda Compressor Station

CAT G3516 Emission Unit

Source Description

Manufacturer

Model

Type

NA- previous unit

Natural gas-fired reciprocating engine

Caterpillar

3516

Turbocharged four-cycle lean burn engine

Engine speed

Sea level hp

Elevation

Derate

Site hp

Hours of Operation

1200

1151

5000

00

1151

8760

rpm

hp

msl

hp

hryr

3 per 1000 ft over 4000 ft

Emission Calculations

Uncontrolled Emissions

NOx CO NMHC SO2 1 HCHO

15 18 05 034 ghp-hr Mfg data

Hourly Emissions 38 46 12 0021 09 lbhr hpghp-hr4536 glb

Annual Emissions 167 200 54 009 38 tonsyr

1 SO2 emissions based on fuel sulfur content of 5 gr S100 scf or 000714 lb SMscf

000714 lb SMscf fuel consumption (Mscfhr) 64 lb SO232 lb S = lbhr SO2

Engine BMEP

Displacement 7040 cubic in Mfg data Engine BMEP 108 psia (hp 792000) (rpm displacement)

Fuel Consumption

Heat Rate 2370 Btuhp-hr Mfg data

Fuel heat value 920 Btuscf Nominal natural gas

Heat Input 27 MMBtuhr Heat Rate hp

Fuel consumption 30 Mscfhr Heat input fuel heat value

Annual fuel usage 260 MMcfyr 8760 hrsyr operation

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Pre-Control Post-Control Nox Major Minor CO Major Minor VOC Minor Minor Formaldehyde Minor Minor Total HAPs Minor Minor Greenhouse Gas Minor Minor

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

Use one spreadsheet for each fuel Make additional copies as needed

This spreadsheet is protected and contains locked cells to ensure that you do not inadvertently alter any of the included formulas andor calculations To

remove this protection and alter this spreadsheet right-click the worksheet tab near the bottom of the screen and select ldquoUnprotect Sheetrdquo When prompted

for the password type ldquoGHGrdquo and click OK Please note that making changes to an unprotected sheet could result in incorrect calculations and that you are

responsible for the accuracy of the data you report to EPA For additional help visit the Microsoft Excel Support website (httpofficemicrosoftcomen-usexcel-

help)

Equation C-1

Equation C-8

EFHHVFuelxCO 101 3

2

EFHHVFuelxONorCH 101 3

24

Facility Name Redonda Compressor Station

Reporter Name New Mexico Gas Company

Unit or Group Name ID

Configuration Type

Fuel Fuel Type Natural Gas

Reporting Period

Comments

General Stationary Fuel Combustion Unit Type

Fuel Input Data

[Fuel] = Mass or volume of fuel

combusted per year from company

records as defined in sect986 (express

mass in short tons for solid fuel volume

in standard cubic feet for gaseous fuel

and volume in gallons for liquid fuel)

22634695541429

[HHV] = Default High heat value of the

fuel from Table C-1 (mmBtumass or

mmBtuvolume)

000103

Constants

[1 x 10-3

] = Conversion Factor from kg

to metric tons (constant) 0001

Annual CO2 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-1

[EF] = Fuel-Specific Default CO2

Emission Factor from Table C-1 (kg

CO2mmBtu)

5306

[CO2] = Annual CO2 emissions from

combustion of the specified fuel (metric

tons)

123462485990

Enter this value in e-GGRT

Annual CH4 Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for CH4 from Table C-2 (kg 0001

CH4mmBtu)

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric 02326847

tons)

Note If you are reporting CH4 emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Annual N2O Mass Emissions For the Specific Fuel Type (metric tons) from Equation C-8

[EF] = Fuel-Specific Default Emission

Factor for N2O from Table C-2 (kg 00001

N2OmmBtu)

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric 00232685

tons)

Note If you are reporting N2O emissions from a pulp mill

lime kiln located at a kraft or soda facility under subpart

AA you are required to use the emission factors in Table

AA-2 per 98273(c)(2)

Enter this value in e-GGRT

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Subpart C - General Stationary Fuel Combustion - Tier 1 Calculation Methodology Using Equations C-1 and C-8 OPTIONAL SPREADSHEET FOR FACILITY RECORDKEEPING PURPOSES

Version e-GGRT RY2011R01 Todays date 9282016

INFORMATION ONLY Annual CH4 Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPCH4] = Global Warming Potential

for CH4

21

[CH4] = Annual CH4 emissions from

combustion of the specified fuel (metric

tons CO2e)

4886378073

INFORMATION ONLY Annual N2O Mass Emissions For the Specific Fuel Type Converted to Carbon Dioxide Equivalent (metric tons CO2e)

[GWPN2O] = Global Warming Potential

for N2O 310

[N2O] = Annual N2O emissions from

combustion of the specified fuel (metric

tons CO2e)

7213224775

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Coal and Coke mmBtushort ton kg CO2 mmBtu

Anthracite 2509 10354

Bituminous 2493 9340

Subbituminous 1725 9702

Lignite 1421 9636

Coke 2480 10204

Mixed (Commercial sector) 2139 9526

Mixed (Industrial coking) 2628 9365

Mixed (Industrial sector) 2235 9391

Mixed (Electric Power sector) 1973 9438

Natural Gas mmBtuscf kg CO2 mmBtu

(Weighted US Average) 1028E-03 5302

Petroleum Products mmBtugallon kg CO2 mmBtu

Distillate Fuel Oil No 1 0139 7325

Distillate Fuel Oil No 2 0138 7396

Distillate Fuel Oil No 4 0146 7504

Residual Fuel Oil No 5 0140 7293

Residual Fuel Oil No 6 0150 7510

Used Oil 0135 7400

Kerosene 0135 7520

Liquefied petroleum gases (LPG) 0092 6298

Propane 0091 6146

Propylene 0091 6595

Ethane 0069 6264

Ethanol 0084 6844

Ethylene 0100 6743

Isobutane 0097 6491

Isobutylene 0103 6774

Butane 0101 6515

Butylene 0103 6773

Naphtha (lt401 deg F) 0125 6802

Natural Gasoline 0110 6683

Other Oil (gt401 deg F) 0139 7622

Pentanes Plus 0110 7002

Petrochemical Feedstocks 0129 7097

Petroleum Coke 0143 10241

Special Naphtha 0125 7234

Unfinished Oils 0139 7449

Heavy Gas Oils 0148 7492

Lubricants 0144 7427

Motor Gasoline 0125 7022

Aviation Gasoline 0120 6925

Kerosene-Type Jet Fuel 0135 7222

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Table C-1 to Subpart C - Default CO2 Emission Factors and High Heat Values for Various Types of Fuel

Fuel Type Default High

Heat Value

Default CO2 Emission

Factor

Asphalt and Road Oil 0158 7536

Crude Oil 0138 7449

Other Fuels (Solid) mmBtushort ton kg CO2 mmBtu

Municipal Solid Waste 1 995 9070

Tires 2687 8597

Plastics 3800 7500

Petroleum Coke 3000 10241

Other Fuels (Gaseous) mmBtuscf kg CO2 mmBtu

Blast Furnace Gas 920E-05 27432

Coke Oven Gas 599E-04 4685

Propane Gas 252E-03 6146

Fuel Gas 2 139E-03 5900

Biomass Fuels - Solid mmBtushort ton kg CO2 mmBtu

Wood and Wood Residuals 1538 9380

Agricultural Byproducts 825 11817

Peat 800 11184

Solid Byproducts 2583 10551

Biomass Fuels - Gaseous mmBtuscf kg CO2 mmBtu

Biogas (Captured methane) 841E-04 5207

Biomass Fuels - Liquid mmBtugallon kg CO2 mmBtu

Ethanol 0084 6844

Biodiesel 0128 7384

Rendered Animal Fat 0125 7106

Vegetable Oil 0120 8155

1 Use of this default HHV is allowed only for (a) units that

combust MSW do not generate steam and are allowed to use Tier

1 (b) units that derive no more than 10 percent of their annual

heat input from MSW andor tires and (c) small batch

incinerators that combust no more than 1000 tons of MSW per

year

2 Reporters subject to subpart X of this part that are complying

with sect98243(d) or subpart Y of this part may only use the

default HHV and the default CO2 emission factor for fuel gas

combustion under the conditions prescribed in sect98243(d)(2)(i)

and (d)(2)(ii) and sect98252(a)(1) and (a)(2) respectively

Otherwise reporters subject to subpart X or subpart Y shall use

either Tier 3 (Equation Cndash5) or Tier 4

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Table C-2 to Subpart C - Default CH4 and N2O Emission Factors for Various Types of Fuel

Fuel Type

Default CH4

Emission Factor

(kg CH4mmBtu)

Default N2O

Emission Factor

(kg N2OmmBtu)

Coal and Coke (All fuel types

in Table C-1) 11E-02 16E-03

Natural Gas 10E-03 10E-04

Petroleum (All fuel types in

Table C-1) 30E-03 60E-04

Municipal Solid Waste 32E-02 42E-03

Tires 32E-02 42E-03

Blast Furnace Gas 22E-05 10E-04

Coke Oven Gas 48E-04 10E-04

Biomass Fuels - Solid (All fuel

types in Table C-1) 32E-02 42E-03

Biogas 32E-03 63E-04

Biomass Fuels ndash Liquid (All

fuel types in Table C-1) 11E-03 11E-04

Note Those employing this table are assumed to fall under the IPCC

definitions of the ldquoEnergy Industryrdquo or ldquoManufacturing Industries and

Constructionrdquo In all fuels except for coal the values for these two

categories are identical For coal combustion those who fall within

the IPCC ldquoEnergy Industryrdquo category may employ a value of 1 g of

CH4mmBtu

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

H4 and N2O

pulp mill lime kilns The emission factors in the table below should only be used for calculating CH4 and N2O emissions from

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

Fuel

Fossil fuel-based emissions factors (kgmmBtu HHV)

Kraft lime kilns Kraft calciners

CH4 N2O CH4

Residual Oil

00027 0

NA

00027 Distillate Oil

Natural Gas

Biogas

Petroleum coke

a Emission factors for kraft calciners are not available

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Table ndash2 to Subpart of Part 98mdash Kraft Lime Kiln and alciner Emissions Factors for Fossil Fuel-ased

The emission factors in the table below should only be used for calculating CH4 and N2O emissions fro

located at a kraft or soda facilities under subpart AA per 98273(c)(2)

Fossil fuel-based emissions factors

m pulp mill lime kilns

H4 and N2O

(kgmmBtu HHV)

Kraft calciners

N2O

00003

00004

00001

00001

a NA

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709

Redonda

Total

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

Fuel Usage

CO2 Emissions

CH4 Emissions

N2O Emissions

total GHG

2010

2011

2012

Mcf fuel used

36482

19423

1472

57377

2010

365 MMcfyr

3283380 MMBtuyr

174216143 kgyr

191638 tonyr

004 tonyr

000 tonyr

2011

194 MMcfyr

1748070 MMBtuyr

92752594 kgyr

102028 tonyr

002 tonyr

000 tonyr

2012

15 MMcfyr

132480 MMBtuyr

7029389 kgyr

7732 tonyr

000 tonyr

000 tonyr

301709