Embed Size (px)
Citation preview
1
DEP SOUTHWEST REGIONAL OFFICE MEMO
TO Air Quality Permit File: OP-65-00840
Dominion Energy Transmission, Inc. / South Oakford Compressor Station
FROM Martin L. Hochhauser, P.E. Air Quality Engineer Air Quality Program
THROUGH Thomas J. Joseph, P.E. Mark R. Gorog, P.E.
Facilities Engineering Manager Environmental Program Manager Air Quality Program Air Quality Program
DATE March 1, 2018 RE Review of Application for Renewed Title V Operating Permit & Minor Mod.
Dominion Energy Transmission, Inc. / South Oakford Compressor Station Hempfield Township, Westmoreland County APS #769944; AUTH #910218; PF #276148 Renewal APS #927348; AUTH #1159101; PF #276148 Minor Modification
Background:
The South Oakford Compressor Station is a natural gas compressor station, with two, NG-fired, 6,350-bhp, compressor engines, one, NG-fired, 778-bhp, emergency generator engine, and one, NG-fired, 3.347 MMBtu/hr boiler. The Department’s earliest records of the station are from 1994.
On November 16, 1995, CNG Transmission Corporation submitted an application for an initial Title V Operating Permit (TVOP) for the South Oakford Compressor Station. On October 13, 1996, the Department issued a Reasonably Available Control Technology Permit, RACT-65-000-840 for the station. On July 17, 1998, the initial TVOP, which was the first facility-wide permit for the station, was issued with an expiration date of July 17, 2003.
During the year 2000, Consolidated Natural Gas Company (the parent company of CNGT) was merged with Dominion Resources Inc., and Dominion became the owner of the facility. On December 26, 2002, Dominion submitted an application to renew the TVOP. On October 31, 2007, the renewed permit was issued with an expiration date of October 31, 2012. The two parts washers (Source ID 111) at the facility were added as a subfacility, as part of this renewal.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
2
On January 11, 2012, Dominion Transmission, Inc. submitted an application to, again renew the TVOP for the South Oakford Compressor Station. Since that time, the name of the owner has changed to Dominion Energy Transmission, Inc.
On June 3, 2016, Dominion submitted an application to install a Clean Burn System on each of the two compressor engines (Source IDs 101 and 102). This included improved engine components which included cylinder heads, pistons, cylinder liners, and turbochargers. In addition, on June 16, 2016, the Department received a petition for an Alternate Compliance Schedule for compliance with the requirements of RACT II for the compressor engines. The final compliance date requested in the petition was February 16, 2018. On April 18, 2017, the Department mailed its approval of both of these requests to the company in the form of a reply to a Request for Determination RFD - 65 - 00840A.
On October 24, 2016, the company submitted an application for a Modification, to incorporate the requirements of RACT II into the Title Operating Permit. This application requested that a limit be placed on the annual operating time of the Aux. Emergency Generator Engine (Source ID 103). No other changes have been made to the sources or controls at the facility since December 2002. These applications are the subject of the Technical Review Document (TRD). The proposed TVOP renewal incorporates both applications.
On December 19 and 20, 2017, both compressor engines (Source IDs 101 and 102) were tested for NOx, CO, and VOC. The results demonstrated compliance with the presumptive NOx and VOC emission limits established to comply with the requirements of RACT II. The testing completed all changes, whose delayed performance was authorized by the Alternate Compliance Schedule, prior to the final performance date of February 16, 2018.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
3
Sources, Control Devices, and Emissions:
The South Oakford Compressor Station is a natural gas compressor station, which is part of a NG transmission and storage system. The system processes pipeline quality natural gas. Its primary sources are two, Cooper, Model No. 14W-330, SI, 2SLB, NG-fired, 6,350-bhp engines, powering two, natural gas compressors, two, additional, 5,750-bhp Cooper, Model No. LM5, natural gas compressors driven by electric motors, one, Waukesha, Model No. L-5790-550, SI, 4SRB, NG-fired, 778-bhp, emergency generator engine, and one, Ajax Model No. WGEFD-4000, NG-fired, 3.347 MMBtu/hr boiler.
The main emission processes at the South Oakford Compressor Station and their control are listed in Table 1. Emissions from other sources are insignificant and listed in Section H of the proposed permit:
Table 1: Emission Sources and Control Dominion Energy Transmission, Inc. - South Oakford Compressor Station (TVOP-65-
00840)
ID Source Name Emission Control Installation or Startup
031 Ajax Boiler 1 (3.347 MMBtu/hr, NG, Model WGEFD-4000)
1992
101 Cooper Engine 1 (6,350-bhp, NG, SI, 2SLB, Model 14W-330)
High Energy Plasma Ignition and Clean Burn Technology1, operated to lower NOx emissions.
1/15/1973
102 Cooper Engine 2 (6,350-bhp, NG, SI, 2SLB, Model 14W-330)
High Energy Plasma Ignition and Clean Burn Technology1, operated to lower NOx emissions.
1/15/1973
103 Waukesha Aux. Emergency Generator Engine 1 (778-bhp, NG, SI, 4SRB, Model L-5790-550)
Annual operating limit of fewer than 500-hours.
1/1/1972
105 Glycol Dehydration System Flare. 1/1/1973
110 Storage Tank P-1, Produced Fluids; 10,000-Gal
111 2 Parts Washers
112 2 NG Compressors #1 and #2 (Driven by Source IDs 101 & 102)
1/15/1973
113 2 Cooper, NG Compressors #3 and 4 (Driven by 5,750-bhp, electric motors)
1996
P01 Facility Pumps, Valves, Flanges, etc. 1/15/1973 1On December 19, 2017, compliance using Clean Burn Technology was demonstrated on these engines. This initiated permanent
operation of the control.
4
Total potential annual air criteria emissions from the sources at the facility are listed in Tables 2A and 2B:
Table 2A: Potential Criteria Emissions prior to installation of Clean Burn Technology on the Compressor Engines and RACT II Requirements
Dominion Energy Transmission, Inc. - South Oakford Compressor Station (TVOP-65-00840) Emissions
PM2.5 PM10 NOx CO VOC
ID Source Name Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY
031 Ajax Boiler 1 (3.347 MMBtu/hr, NG)1
0.025 0.11 0.025 0.11 0.33 1.44 0.28 1.21 0.0180 0.08
101 Cooper Engine 1 (6,350-bhp, NG, SI, 2SLB)2
0.178 2.5 10.89 0.178 2.5 10.89 9.0 125.99 551.80 4.0 56.00 245.30 2.0 28.00 122.60
102 Cooper Engine 2 (6,350-bhp, NG, SI, 2SLB)2
0.178 2.5 10.89 0.178 2.5 10.89 9.0 125.99 551.80 4.0 56.00 245.30 2.0 28.00 122.60
103 Waukesha Aux. Emergency Generator Engine 1 (778-bhp, NG, SI, 4SRB)3
0.071 0.122 0.03 0.071 0.122 0.03 11.0 18.9 82.60 13.7 23.46 5.87 8.1 13.94 3.48
105 Glycol Dehydration System4 0.0091 0.04 0.0091 0.04 0.116 0.51 0.098 0.43 0.90 3.96
110 Storage Tank P-1, 10,000-Gal5
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.0070 0.03
111 2 Parts Washers6 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.112 0.49
112 2 NG Compressors #1 and #2 (Driven by Source IDs 101 & 102)7
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.171 0.75
113 2 Cooper, NG Compressors #3 and 4 (Driven by 5,750-bhp, electric motors)7
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.171 0.75
P01 Facility Pumps, Valves, Flanges, etc.5
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 2.9 12.50
Facility Total 5.1 21.96 5.1 21.96 271 1,188.15 136 498.10 74 267.24 All emission sources, except the emergency generator engine (Source ID 104), at the facility operate 8,760 hours per year. For emissions, the emergency generator is assumed to
operate 500 hours per year. 2For Table 2A: Emission of NOx, CO, and VOC are based on emission limits. Other emissions are based on AP-42.
5
Dominion Energy Transmission, Inc. - South Oakford Compressor Station (TVOP-65-00840)
Footnotes common to both Tables 2A and 2B. 1Emissions are based on AP-42. 3Emission of NOx is based on permit limits. Other emissions are based on AP-42. 4Emissions are peak annual emissions reported by Dominion for South Oakford over the period of 2012 - 2016. 5Emissions were supplied by the company. 6Emissions for 2 parts washers, together, were assumed to be the same as the single parts washer at JB Tonkin (Permit # TVOP-65-00634). 7Blow-by emissions from the compressor are based on 23 (11.5*2) scfh/piston rod (EPA EnergyStar), 4 piston rods, and NG analysis supplied by the company, in its 2015 annual report. Values reported in this table were rounded from calculations performed elsewhere. Total facility emissions are a combination of regulated potential emissions and estimated emissions.
6
Table 2B: Potential Criteria Emissions after installation of Clean Burn Technology on the Compressor Engines and RACT II Requirements.
Dominion Transmission, Inc - South Oakford Compression Station (TVOP-65-00840) Emissions PM2.5 PM10 NOx CO VOC
ID Source Name Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY Gm/ bhp-hr
lb/ hr TPY
031 Ajax Boiler 1 (3.347 MMBtu/hr, NG)1
0.025 0.11 0.025 0.11 0.33 1.44 0.28 1.21 0.018 0.08
101 Cooper Engine 1 (6,350-bhp, NG, SI, 2SLB)2, 8
0.178 2.5 10.89 0.178 2.5 10.89 3.0 42 183.95 0.85 11.2 49.13 1.00 14.0 61.32
102 Cooper Engine 2 (6,350-bhp, NG, SI, 2SLB)2, 8
0.178 2.5 10.89 0.178 2.5 10.89 3.0 42 183.95 0.85 11.2 49.13 1.00 14.0 61.32
103 Waukesha Aux. Emergency Generator Engine 1 (778-bhp, NG, SI, 4SRB)3, 9
0.071 0.122 0.03 0.071 0.122 0.03 11.0 18.9 4.72 13.7 23.5 5.87 8.1 13.9 3.48
105 Glycol Dehydration System4 0.0091 0.04 0.009 0.04 0.116 0.51 0.098 0.43 0.90 3.96
110 Storage Tank P-1, 10,000-Gal5
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.0068 0.03
111 2 Parts Washers6 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.112 0.49
112 2 NG Compressors #1 and #2 (Driven by Source IDs 101 & 102)7
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.171 0.75
113 2 Cooper, NG Compressors #3 and #4 (Driven by 5,750-bhp, electric motors)7
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.171 0.75
P01 Facility Pumps, Valves, Flanges, etc.4
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 2.9 12.50
Facility Total 5.1 21.96 5.1 21.96 103 374.56 46 105.76 46 144.68 All emission sources, except the emergency generator engine (Source ID 104), at the facility operate 8,760 hours per year. The emergency generator, is limited to a maximum
operation of less than 500 hours per year. 2For Table 2B: Emission of NOx and VOC are based on emission limits. CO is based on stack testing. Other emissions are based on AP-42. 8Cooper Engines 1 & 2 are subject to RACT II presumptive emission limits of 3.0 grams NOx and 1.0 gram of VOC/bhp-hr, during normal operation at rated load. 9Hourly and annual NOx emissions are based on permit limits.
7
Total potential annual Hazardous Air Pollutant (HAP) emissions from the sources at the facility, after incorporation of the requirements for RACT II, are shown in Table 3. No credit was taken for any reduction in organic HAP emissions from the use of Clean Burn Technology on the compressor engines. However, the new limit on the hours of operation of the emergency engine did reduce its emissions:
Table 3: Potential Hazardous Air Pollutant Emissions Dominion Energy Transmission, Inc. - South Oakford Compressor Station (TVOP-65-00840)
Source ID 031 101 & 102 103 105 112 & 113 110, 111, & P01
Facility
Description Boiler1 Compressor
Engines2
Emergency Generator Engine3
Glycol Dehydration
System4
4 NG Compressors5
Storage Tank, Parts Washers,
Piping6, 7, 8
HAP Tons per Year
Formaldehyde 0.00 18.79 0.03 0.00 0.00 0.00 18.82
GLYET 0.00 0.00 0.00 0.00 0.00 4.13 4.13
Acrolein 0.00 3.51 0.00 0.00 0.00 0.00 3.51
Acetaldehyde 0.00 3.50 0.00 0.00 0.00 0.00 3.50
Benzene 0.00 0.87 0.00 0.81 0.00 0.00 1.69
Methanol 0.00 1.12 0.00 0.00 0.00 0.00 1.12
Other HAPS 0.03 1.60 0.00 0.26 0.16 0.08 2.13
Sum of All HAPs 0.03 29.39 0.05 1.07 0.16 4.21 34.92 All emission sources, except the emergency generator, at the facility operate 8,760 hours per year. The emergency generator, which was is assumed to operate 500 hours per year,
prior to issuance of this proposed TVOP, is limited to a maximum of less than 500 hr/yr. 1Emissions from the boiler are based on AP-42. Table 1.4-2. 2Except for formaldehyde from the compressor engine, emissions are based on AP-42, Table 3.2-1 (2SLB). Formaldehyde emissions from the Compressors are based on March
13, 2013 testing. 3Emissions are based on AP-42, Table 3.2-3 (4SRB). 4Emissions are peak annual emissions reported by Dominion for South Oakford over period of 2012 - 2016. 5Blow-by emissions from the compressor are based on 23 (11.5*2) scfh/piston rod (EPA EnergyStar), 4 piston rods, and NG analysis supplied by the company, in its 2015 annual
report. 6Emissions were reported by the company. 7The value for facility fugitive emissions was reported in the 1995 application for an initial TVOP. 8Emissions for 2 parts washers, together, were assumed to be the same as the single parts washer at JB Tonkin (Permit # TVOP-65-00634). Values reported in this table were rounded from calculations performed elsewhere.
8
Total potential annual emissions of Greenhouse Gases (GHG) from the sources at the facility, after incorporation of the requirements for RACT II, are shown in Table 4:
Table 4: Potential Greenhouse Gas Emissions (GHGs) Dominion Energy Transmission, Inc. - South Oakford Compressor Station (TVOP-65-00840)
Greenhouse Gas
CO2 CH4 N2O Total CO2e1
ID Source Name Lb/Hr Ton/Yr Lb/ Hr Ton/ Yr Lb/ Hr Ton/ Yr Lb/ Hr Ton/ Yr
031 Ajax Boiler 12 394 1,725 0.0075 0.033 0.0072 0.032 396 1,735
101 Cooper Engine 13 5,662 24,800 75 327 0.00 0.00 7,528 32,972
102 Cooper Engine 23 5,662 24,800 75 327 0.00 0.00 7,528 32,972
103 Waukesha Aux. Emergency Generator Engine 13 694 173 1.5 .036 0.00 0.00 730 182
105 Glycol Dehydration System 136 596 0.0023 0.0100 0.00 0.00 136 596
110 Storage Tank P-1 0.00 0.00 0.00 0.00 0.00 0.00 0 0
111 2 Parts Washers 0.00 0.00 0.00 0.00 0.00 0.00 0 0
112 2 NG Compressors #1 and #24 0.194 1 14.2 62 0.00 0.00 356 1,558
113 2 Cooper, NG Compressors #3 and #4 0.194 1 14.2 62 0.00 0.00 356 1,558
P01 Facility Pumps, Valves, Flanges, etc.5 0.00 0.00 237 1,038 0.00 0.00 5,923 25,943
Facility Total 12,548 52,095 416 1,817 0.0072 0.032 22,953 97,518 All emission sources, except the emergency generator, at the facility operate 8,760 hours per year. The emergency generator, which was is assumed to operate 500 hours per year,
prior to issuance of this proposed TVOP, will be limited to a maximum of less than 500 hr/yr, when the permit is issued. 1Emission estimates of CO2e are based on 100-year horizon Global Warming Potentials (1 ton CH4 = 25 ton CO2 and 1 ton N2O = 298 ton CO2) in Table A-1 to Part A of Part 98.
(Values effective January 1, 2014.) 2Emissions from the boiler are based on AP-42, Table 1.4-2. 3Emissions from the engines are based on AP-42, Table 3.2-1 & Table 3.2-3. 4Blow-by emissions from the compressor are based on 23 (11.5 * 2) scfh/piston rod (EPA EnergyStar), 8 piston rods, and NG analysis supplied by the company, in its 2015 annual
report. 5Methane emissions from P01 are based on CH4 emissions from the natural gas compressors and the ratio of VOC from the two sources. Values reported in this table were rounded from calculations performed elsewhere. Total facility emissions are a combination of regulated potential emissions and estimated emissions.
The use of Clean Burn Technology has a negligible effect on emissions of CO2e. However, the reduction in authorized operation of the emergency engine lowered emissions from this source.
9
The change in potential emissions from the facility, since the TVOP was last evaluated is shown in Table 5:
Table 5: Change in Emissions Since the TVOP was last Renewed Dominion Transmission, Inc - South Oakford Compression Station (TVOP-65-00840)
PM2.5 PM10 NOx CO VOC HAPs CO2e
Date Tons per Year
10/31/2007 Potential Emissions at Last Renewal
21.96 21.96 1,188.15 498.10 267.24 35.92 97,518
1/1/2017 Addition of Operating Time Limit on the Aux. Generator1
0.00 0.00 -77.88 0.00 0.00 0.00 0
11/7/2017 Addition of Clean Burn Technology on the Compressor Engines1
0.00 0.00 -735.70 -392.34 -122.57 0.00 0
Total Change over Period 0.00 0.00 -813.59 -392.34 -122.57 0.00 0
Issue Date of Renewal
Potential Emissions 21.96 21.96 374.56 105.76 144.68 34.92 97,518
1Both changes were made to comply with the requirements of RACT II.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
10
Regulatory Analysis:
The South Oakford Compressor Station is a Title V source, because its potential emissions of NOx and CO are greater than the Major Source threshold of 100 tons per year and VOC are greater than the Major Source threshold of 50 tons per year. Its annual emissions of PM2.5, PM10, and SO2 from the facility are less than the Major Source threshold of 100 tons per year. For Hazardous Air Pollutant (HAP) emissions, the facility has a single HAP (Formaldehyde) with an emission potential greater than the 10 TPY major source threshold. This means that South Oakford is also a Major Source of HAP emissions. Finally, CO2e emissions from South Oakford are less than the Major Source threshold of 100,000 tpy. Therefore, South Oakford is a minor source of CO2e.
The facility was evaluated for the applicability of New Source Performance Standards (NSPS), National Emission Standards for Hazardous Air Pollutants (NESHAP), other Federal Standards, and applicable requirements of 25 Pa. Code Chapters 121 - 145, of the Commonwealth of Pennsylvania. The following standards were considered:
Table 5: Regulatory Analysis Dominion Energy Transmission, Inc.
South Oakford Compressor Station (TVOP-65-00840) Federal Regulations
NSPS
40 CFR Part 60, Subpart Kb - Standards of Performance for Volatile Organic Liquid Storage Vessels (Including Petroleum Liquid Storage Vessels) for Which Construction, Reconstruction, or Modification Commenced After July 23, 1984.
Any condensate stored in storage vessels at the South
Oakford Compressor Station does not have sufficient
vapor pressure for Subpart Kb to have any applicable
requirements for these tanks.
40 CFR Part 60, Subpart LLL - Standards of Performance for SO2 Emissions From Onshore Natural Gas Processing for Which Construction, Reconstruction, or Modification Commenced After January 20, 1984, and on or Before August 23, 2011.
South Oakford compresses pipeline quality natural gas,
and does not have equipment which “sweetens” the
natural gas. This Subpart regulates removal of acid gas
(H2S and SO2). No source at the facility has applicable
requirements under the Subpart.
40 CFR Part 60, Subpart JJJJ - Standards of Performance for Stationary Spark Ignition Internal Combustion Engines.
This Subpart applies to SI engines larger than 500-bhp,
constructed after July 1, 2007, and lean burn SI engines,
rated greater than 1,350 HP, manufactured after
January 1, 2008. The SI engines at South Oakford pre-
date this Subpart, and have no applicable requirements
under it. (Continued)
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
11
(Table 5 NSPS - Continued)
40 CFR Part 60, Subpart KKKK - Standards of Performance for Stationary Combustion Turbines.
The facility has no combustion turbines. No source at
the facility has applicable requirements under the
Subpart.
40 CFR Part 60, Subpart OOOO - Standards of Performance for Crude Oil and Natural Gas Production, Transmission and Distribution for which Construction, Modification or Reconstruction Commenced after August 23, 2011, and on or before September 18, 2015.
South Oakford is not a natural gas processing plant, and
only its compressors could have requirements under the
subpart. The natural gas compressors were constructed
before this time. This Subpart is not applicable to any
source at South Oakford.
40 CFR Part 60, Subpart OOOOa - Standards of Performance for Crude Oil and Natural Gas Facilities for which Construction, Modification or Reconstruction Commenced After September 18, 2015.
The South Oakford Compressor Station was constructed
before this date, and the Subpart is not applicable.
NESHAPS
40 CFR Part 63, Subpart H - National Emission Standards for Organic Hazardous Air Pollutants for Equipment Leaks.
This Subpart has requirements for equipment at
Major Sources of HAPs1, which includes compressors.
However, it is only applicable for sources that have
requirements under a NSPS or MACT standard that
call for this Subpart, which is not the case for any
source at the South Oakford Compressor Station.
Therefore, this Subpart has no requirements for any
source at this facility.
40 CFR Part 63, Subpart HH - National Emission Standards for Hazardous Air Pollutants From Oil and Natural Gas Production Facilities.
This subpart has differing requirements for both
facilities that are a Major Source of HAPs, and
facilities that are area sources. South Oakford is a
Major Source of HAP emissions, but has no
equipment of the types affected by this Subpart.
Also, the South Oakford Station compresses natural
gas that was processed to pipeline quality standards,
prior to entering the station. Therefore, this Subpart
has no applicable requirements for any source at
South Oakford.
(Continued)
1 Maximum potential emissions of the highest individual HAP and combined HAPs are greater than either, 10 TPY, or 25 TPY, respectively.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
12
(Table 5 NESHAPS - Continued)
40 CFR Part 63 Subpart HHH - National Emission Standards for Hazardous Air Pollutants From Natural Gas Transmission and Storage Facilities.
This subpart applies to natural gas storage facilities
that are Major Sources of HAPs, and this is true for
South Oakford. This NESHAPs deals with the glycol
dehydration unit and its associated control device
(flare). BTEX emissions from the flare exhaust must
be lower than the value calculated by Equation 1 in
§40 CFR 63.1275(b)(1)(iii). The Glycol Dehydration
System (Source ID 105) is an existing, small, glycol
dehydration unit, equipped with a flare, and must
have achieved compliance with this Subpart by
October 15, 2015. All pertinent requirements of
Subpart HHH have been included in this renewal
Title V permit, including provisions for monitoring,
recordkeeping and reporting.
40 CFR Part 63, Subpart ZZZZ - National Emissions Standards for Hazardous Air Pollutants for Stationary Reciprocating Internal Combustion Engines.
This MACT was initially promulgated during June 2004
and covers all stationary RICE. It was revised during
both, January 2008 and March 2010, with
requirements for additional classes of engines. The
compressor engines (Source IDs 101 & 102) are
existing, non-emergency, Spark Ignition, two-stroke,
Lean Burn (LB), reciprocating internal combustion
engines (RICE) with a rated capacity greater than 500-
bhp, and located at a Major Source of HAP emissions.
The auxiliary generator engine (Source ID 103) is an
existing, emergency, Spark Ignition, four-stroke, Rich
Burn (RB), reciprocating internal combustion engine
(RICE) with a rated capacity greater than 500-bhp, and
located at a Major Source of HAP emissions, which
does not produce power for sale. 40 CFR
63.6590(b)(3) exempts the compressor engines,
which meet the description in (i), and auxiliary engine
which is covered in (iii).
Therefore, the compressor engines (Source IDs 101 &
102) and the auxiliary generator engine (Source ID
103) have no requirements under Subpart ZZZZ. No
source at South Oakford has any requirements under
this Subpart. (Continued)
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
13
(Table 5 NESHAPS - Continued)
40 CFR Part 63, Subpart DDDDD - National Emission Standards for Hazardous Air Pollutants for Major Sources: Industrial, Commercial, and Institutional Boilers and Process Heaters
Some Industrial, Commercial, Institutional (ICI) Boilers
and Process Heaters at major sources of HAPs are
subject to Subpart DDDDD. The natural gas-fired,
3.347 MMBtu/hr Ajax Boiler 1 (Source ID 031) does
have applicable requirements under Subpart DDDDD.
The effective date of this subpart was January 16,
2016, under the subpart. The operator is required to
submit an initial notification, perform a one-time
energy assessment, tune-up the boiler once every five
years, and operate the boiler in a manner to minimize
emissions.
Other Air Programs
40 CFR Part 64 - Compliance Assurance Monitoring (CAM)
Each of the compressor engines (Source IDs 101 &
102) have NOx and VOC emission limits, add-on
controls, and uncontrolled potential emissions of NOx
and VOC greater than the major source amounts.
However, the definition of control device for CAM in
§64.1 Definitions excludes controls that prevent
pollutants from forming, which is the case for both,
the High Energy Ignition and the Clean Burn
Technology on the engines. Therefore, no source at
South Oakford is subject to CAM.
40 CFR Part 98 - Mandatory Greenhouse Gas Reporting
The South Oakford Compressor Station has potential
emissions in excess of 25,000 of CO2e per year. If it
emits greater than this amount, the owner/operator
must report those emissions to EPA.
However, the preamble of the final version of the
GHG MRR, located at 74 Fed Reg 209, pp. 56287-
56288, states that the GHG MRR is not considered an
“applicable requirement” under the Title V Operating
Permit program. Therefore, this Subpart, while an
obligation for the South Oakford, is not considered an
applicable requirement for this TVOP.
(Continued)
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
14
(Table 5 Pa. Code - Continued)
Pennsylvania Air Pollution Control Regulations
25 Pa Code 121.7 (Prohibition of Air Pollution) Section is applicable.
25 Pa Code § 123.1 (Prohibition of Certain Fugitive Emissions)
Section is applicable.
25 Pa Code § 123.2 (Fugitive Particulate Matter) Section is applicable.
25 Pa Code § 123.11 (Combustion Units) Section is applicable.
(25 Pa Code § 123.13 (Processes) Section is applicable.
25 Pa Code § 123.21 (General) [Related to SO2] Section is applicable.
25 Pa Code § 123.22 (Combustion units) [Related to SO2]
Section is applicable.
25 Pa Code § 123.31 (Odor Emissions) Section is applicable.
25 Pa Code § 123.41 (Limitations - Visible Emissions)
Section is applicable.
25 Pa Code § 123.42 (Exceptions - Visible Emissions)
Section is applicable.
25 Pa Code § 123.43 (Measuring Techniques) Section is applicable.
25 Pa Code Chapter § 127.441 (Operating permit terms and conditions)
Section is applicable. Emission control, workpractice,
recordkeeping, and reporting restrictions for the
facility were created under the authority of this
section. Also, restrictions relating to emission of SO2
were removed, since they are non-applicable. This is
because no source at the facility is capable of
generating SO2 emissions that approach regulatory
limits.
25 Pa Code Chapter § 129.14 (Open Burning Operations)
Section is applicable. The facility is not in an air basin,
and open burning is allowed, with certain exceptions.
25 Pa Code Chapter § 129.63 (Degreasing Operations)
The facility has two parts washers (Source ID 111)
which have applicable requirements under this
Section.
25 Pa Code 129.91 - 129.95 (Stationary Sources of NOx and VOCs)
Sources at the Station had requirements under
RACT I. However, except for the NOx emission limits
on the emergency generator engine (Source ID 103),
these were superseded by RACT II requirements.
Also, the existing permit contained limits on CO
emissions from the compressor engines, added under
the authority of RACT I (§ 129.91 - 129.95). This
authority does not exist, and these limits were not
carried forward into the proposed permit. (Continued)
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
15
(Table 5 Pa. Code - Continued)
25 Pa Code 129.96 - 129.100 (Additional RACT Requirements for Major Sources of NOx and VOCs)
The Station in a Major Source of both NOx and VOCs.
Sources at the Station were constructed before July
20, 2012, and emit NOx and VOC in excess of 1 tpy.
These are the boiler (Source ID 031), compressor
engines (Source IDs 101 & 102), and emergency
generator engine (Source ID 103). The compressor
engines (Source IDs 101 & 102) are subject to a
presumptive, maximum, NOx emission limit of 3
gram/hp-hr and a presumptive, maximum, VOC
emission limit of 1 gram/hp-hr, during normal
operation, under 25 Pa. Code § 129.97(g)(3)(i). The
compressor engines required an alternate compliance
schedule, which is now complete, to meet this limit.
The boiler (Source ID 031) with potential NOx
emissions of less than 5 TPY and potential VOC
emissions of less than 2.7 TPY and the emergency
generator engine (Source ID 103), with the addition of
a fewer than 500-hour annual operation limit are
required to be maintained and operated in
accordance with manufacturer’s specifications and
good operating practices, as presumptive RACT, under
25 Pa. Code § 129.97(c)(1) and (8). These
requirements were added to the proposed permit.
25 Pa Code Chapter 135.3 (Reporting) South Oakford is a Title V facility, and the
owners/operators must submit annual emission
reports.
25 Pa Code Chapter 135.5 (Recordkeeping)
Dominion Energy Transmission, Inc. must fulfill the
following requirements: 1. The permittee shall
maintain comprehensive, accurate records which, at a
minimum, shall include: a. The number of hours per
month that each piece of equipment operated; and b.
The amount of fuel used per month, in each piece of
equipment; 2. The owner/operator shall keep daily
records of all product delivery. 3. These records shall
be kept on site for a period of five years, and be made
available to the Department upon request.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
16
Changes from Existing Operating Permit:
1. The name of the owner has changed from Dominion Transmission, Inc., to Dominion Energy Transmission, Inc. The names of the Responsible Official and Permit Contact have also been updated.
2. The general prohibition against air pollution 25 Pa. Code § 121.7 has been added (Section C, Condition #001, New).
3. Since the natural gas compressors have blow-by emissions of natural gas, the compressors (Source ID 112 for Compressors #1 and #2 and Source ID 113 for Compressors #3 and #4) at the station, were added as sources in the proposed permit.
4. A requirement for weekly surveys of the facility for visible stack emissions, visible fugitive emissions, and malodors, when it is active and manned, and to keep records of these surveys, was added (Section C, Condition #010, New).
5. The applicable requirements of 40 CFR Part 63, Subpart DDDDD were added for the boiler (Section D, Source ID 031, Conditions #002 - #015, New).
6. The applicable requirements for 40 CFR Part 63, Subpart HHH, which have become effective for sources at the facility since the last permit renewal, were added to the permit (Section D, Source ID 105, Conditions #003 - #011, New). Old permit requirements for Subpart HHH were removed (Section C, Conditions #007 and #020 - #024, Old), because the dehydration unit is a small unit, and at the time the previous TVOP was issued, it was exempt from the Subpart.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
17
7. The applicable requirements for RACT II, which have become effective for sources at the facility since the last permit renewal, were added to the permit (Section C, Conditions #026 - #027; Section D, Source ID 031, Condition #001; Section D, Source ID 103, Condition #004; Section E, Source Group G01, Conditions #001 - #002 and #005, New). Clean Burn Technology, a proprietary, very high Air/Fuel ratio combustion process, was added to the compressor engines, and a voluntary limit on the hours of operation of the auxiliary generator engine was added to meet RACT II requirements (Section D, Source ID 103, Condition #002, New). RACT I requirements were removed (Section C, Conditions #008 - #010; Section D, Source ID 031, Conditions #003 - #004; Section D, Source ID 101, Conditions #003 - #007; Section D. Source ID 102, Conditions #003 - #007, Old), except for limits on NOx emission from the aux. generator engine (Section D, Source ID 103, Condition #003, Old), since they were superseded by RACT II. Annual NOx emissions from Source ID 103 were proportioned to its new hourly operation limit (Section D, Source ID 103, Condition #002, New).
8. Limits on CO emissions imposed under RACT I were removed, since the authority to impose these limits did not exist (Section D, Source ID 101, Condition #003 and Section D, Source ID 102, Condition #003, Old).
9. Limits on SO2 emissions have been removed (Section D, Source ID 031, Condition #002; Section D, Source ID 101, Condition #002; Section D, Source ID 102, Condition #002, Old), since emissions are negligible. The natural gas processed and used at the station is of pipeline quality.
10. The language of other conditions in the permit was updated.
Dominion Energy Transmission, Inc. South Oakford Compressor Station TVOP-65-00840
Permit Authorized by this Authorization Quantity Facility Name PF ID: 276148
2 Dominion Energy Transmission, Inc. / South Oakford Compressor Station (OP-65-00840)
Renewal APS ID: 769944 Auth. ID: 910218 Minor Mod. To add RACT II APS ID: 927348 Auth. ID: 1159101
Short Descr. Operating Permit for a natural gas compressor station.
Permits Inactivated by this Authorization Permit #
APS ID Auth. ID
18
Conclusions and Recommendations:
An inspection of South Oakford Compressor Station for a Full Compliance Evaluation was last conducted on April 3, 2016, by Anna Fabrizi, Air Quality Specialist of PA DEP. Ms. Fabrizi determined that the plant met all of the requirements of the existing TVOP. The Compressor Engines (Source IDs 101 and 102) were last tested for NOx, CO, and VOC emissions on December 19, 2017, and found to be in compliance with both, the limits in the current permit and the new limits in the proposed permit. These engines were last tested for formaldehyde on March 13, 2013. The notice of the intent to issue a renewed TVOP, incorporating a Minor Permit Modification with the applicable requirements of RACT II appeared in the Greensburg Tribune-Review on January 18, 19, and 20, 2018. Copies of the proposed permit were sent to Judi W. Fox, Environmental Specialist III, for Dominion, EPA, George Traister, the Department’s Air Quality inspector for the facility, and Tom Norris, Air Quality District Supervisor for the District.
The Dominion Energy Transmission, Inc. has proposed, in this application, to continue to operate a natural gas compressor station in Hempfield Township, Westmoreland County. I recommend the issuance of a five-year Operating Permit for this facility, subject to the conditions in the proposed Title V Operating Permit.
Att
ach
me
nt
1
Do
min
ion
Tra
nsm
issi
on
-So
uth
Oa
kfo
rd S
tati
on
(T
VO
P-6
5-0
08
40
)M
LH
PA
DE
P
2/6
/20
18
Tab
le 1
: E
mis
sion
Sou
rces
and
Con
trol
Dom
inio
n T
rans
mis
sion
, Inc
. - S
outh
Oak
ford
Com
pres
sor
Stat
ion
(TV
OP
-65-
0084
0)
IDS
our
ce N
ame
Em
issi
on
Co
ntro
l
Inst
alla
tion
or
Sta
rtup
31A
jax
Bo
iler
1 (3
.347
M
MB
tu/h
r, N
G,
Mo
del
WG
EF
D-4
000)
Prio
r to
19
95
101
Co
ope
r E
ngin
e 1
(6,3
50-b
hp,
NG
, S
I, 2
SLB
, M
ode
l 14W
-33
0)
Hig
h E
nerg
y P
lasm
a Ig
nitio
n,
ope
rate
d to
lo
wer
NO
x
emis
sio
ns.
1/15
/197
3
102
Co
ope
r E
ngin
e 2
(6,3
50-b
hp,
NG
, S
I, 2
SLB
, M
ode
l 14W
-33
0)
Hig
h E
nerg
y P
lasm
a Ig
nitio
n,
ope
rate
d to
lo
wer
NO
x
emis
sio
ns.
1/15
/197
3
103
Wau
kesh
a A
ux.
Em
erge
ncy
Gen
erat
or
Eng
ine
1 (7
78-b
hp,
NG
, S
I, 4
SR
B,
Mo
del L
-579
0-55
0)
1/1/
1972
105
Gly
col D
ehyd
ratio
n S
yste
mF
lare
1/1/
1973
110
Sto
rage
Tan
k P
-1,
Pro
duce
d F
luid
s; 1
0,00
0-G
al11
12
Par
ts W
ashe
rs
112
2 N
G C
om
pres
sors
#1
and
#2
(Driv
en b
y S
our
ce I
Ds
101
&
102)
1/15
/197
3
113
2 C
oo
per,
NG
Co
mpr
esso
rs
#3 a
nd 4
(D
riven
by
5,75
0-bh
p, e
lect
ric m
oto
rs)
1996
P01
Fac
ility
Pum
ps,
Val
ves,
F
lang
es,
etc.
1/15
/197
3
IA.
Cri
teri
a E
mis
sio
ns
pri
or
to i
nst
all
ati
on
of
Cle
an
Bu
rn C
on
tro
l o
n t
he
Co
mp
ress
or
En
gin
es
an
d R
AC
T I
I re
qu
ire
me
nts
.
Co
mp
ress
or
En
gin
e E
mis
sio
ns
Na
tura
l G
as
Co
mp
ress
or
En
gin
es
(So
urc
e I
Ds
10
1 &
10
2)
6,3
50
bh
p8
76
0h
ou
rs/y
ea
r
Fo
r e
ach
en
gin
e:
Co
op
er
Be
sse
me
r 1
4W
-33
0-C
2,
2S
LB Ca
lcu
lati
on
of
he
at
inp
ut
rate
fo
r th
e e
ng
ine
s fr
om
7/3
1/1
98
6 J
B T
on
kin
en
gin
e t
est
Ou
tpu
t p
ow
er
60
13
bh
p
NG
bu
rne
d d
uri
ng
te
st2
2.3
MS
CF
Te
st d
ura
tio
n2
8m
inu
tes
NG
he
at
va
lue
10
20
Btu
/ft^
3fr
om
EP
A A
P-4
2,
Ta
ble
1.4
-1
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
1 o
f 1
33
/2/2
01
8
He
at
Inp
ut-
test
48
.74
14
28
57
MM
Btu
/hr
8,1
06
B
tu/b
hp
-hr
He
at
Inp
ut@
6,3
50
-bh
p5
1.4
7
MM
Btu
/hr
NG
in
pu
t@6
,35
0-b
hp
0.0
50
5
M
MC
F/h
r
Em
issi
on
Lim
its
Lim
its
in C
urr
en
t P
erm
it
NO
x1
25
.99
lb/h
r5
51
.8tp
y(E
qu
iv t
o9
.0g
ram
/hp
-hr)
CO
56
.00
lb/h
r2
45
.3tp
y(E
qu
iv t
o4
.0g
ram
/hp
-hr)
VO
C2
8.0
0lb
/hr
12
2.6
tpy
(Eq
uiv
to
2.0
gra
m/h
p-h
r)
Fo
r P
M1
0 &
PM
2.5
Em
issi
on
s3
.84
E-0
2lb
PM
2.5
-FIL
/MM
Btu
3.8
4E
-02
lb P
M1
0-F
IL/M
MB
tuA
P-4
2 T
able
3.2
-1 U
nco
ntro
lled
2SLB
9.9
1E
-03
lb P
M2
.5-C
ON
D/M
MB
tu9
.91
E-0
3lb
PM
10-C
ON
D/M
MB
tuA
P-4
2 T
able
3.2
-1 U
nco
ntro
lled
2SLB
4.8
3E
-02
lb P
M2
.5/M
MB
tu4
.83
E-0
2lb
PM
10/M
MB
tu
(Fo
r e
ng
ine
s P
M-F
IL =
PM
10-F
IL =
PM
2.5
-FIL
)
or
0.1
77
6G
m P
M2
.5/b
hp
-hr
0.1
77
6G
m P
M1
0/b
hp
-hr
Em
issi
on
Te
stin
g R
esu
lts
for
En
gin
es
#1
an
d #
2
NO
xC
OV
OC
FO
RM
En
gin
e #
lb/h
rlb
/hr
lb/h
rlb
/hr
2/2
4/1
99
71
22
.31
6.8
2.2
Sta
ck T
est
ing
(No
t in
clu
de
d i
n a
vera
ge
s.)
2/2
4/1
99
72
16
.41
4.6
2.8
Sta
ck T
est
ing
(No
t in
clu
de
d i
n a
vera
ge
s.)
3/1
6/1
99
81
11
2.6
10
0.0
0P
ort
ab
le E
mis
sio
ns
Te
st(N
ot
incl
ud
ed
in
ave
rag
es.
)
3/1
6/1
99
82
10
2.6
11
.30
.00
Po
rta
ble
Em
issi
on
s T
est
(No
t in
clu
de
d i
n a
vera
ge
s.)
3/1
8/2
00
81
36
.39
5.3
10
.52
0.6
6S
tack
Te
stin
g
3/1
8/2
00
82
12
4.9
99
.71
0.9
21
.25
Sta
ck T
est
ing
2/3
/20
09
11
20
.83
11
.85
0.4
9P
ort
ab
le E
mis
sio
ns
Te
st
2/3
/20
09
21
22
.34
10
.49
0.4
5P
ort
ab
le E
mis
sio
ns
Te
st
2/2
3/2
01
01
87
11
.04
0.2
7P
ort
ab
le E
mis
sio
ns
Te
st
2/2
3/2
01
02
11
6.8
99
.79
0.2
1P
ort
ab
le E
mis
sio
ns
Te
st
2/2
2/2
01
11
97
.36
11
.35
Po
rta
ble
Em
issi
on
s T
est
2/2
2/2
01
12
11
6.1
51
0.3
2P
ort
ab
le E
mis
sio
ns
Te
st
2/1
9/2
01
31
11
4.7
51
2.3
7P
ort
ab
le E
mis
sio
ns
Te
st
2/1
9/2
01
32
11
8.2
10
.39
Po
rta
ble
Em
issi
on
s T
est
3/1
3/2
01
31
10
2.3
11
2.2
41
.18
2.2
4S
tack
Te
stin
g
3/1
3/2
01
32
10
0.7
91
0.3
50
.15
2.0
5S
tack
Te
stin
g
2/1
1/2
01
41
59
.88
15
.13
Po
rta
ble
Em
issi
on
s T
est
2/1
1/2
01
42
68
.92
13
.37
Po
rta
ble
Em
issi
on
s T
est
10
/15
/20
15
17
3.2
12
.76
Po
rta
ble
Em
issi
on
s T
est
10
/15
/20
15
26
4.3
91
1.6
5P
ort
ab
le E
mis
sio
ns
Te
st
2/9
/20
16
17
7.2
11
1.4
9P
ort
ab
le E
mis
sio
ns
Te
st
2/9
/20
16
28
4.9
11
0.2
5P
ort
ab
le E
mis
sio
ns
Te
st
12
/20
/20
16
10
.28
Sta
ck T
est
ing
12
/20
/20
16
20
.00
Sta
ck T
est
ing
4/4
/20
17
18
6.9
71
2.5
70
03
.96
Sta
ck T
est
ing
4/4
/20
17
29
6.1
41
1.9
10
03
.64
Sta
ck T
est
ing
Av
era
ge
93
.48
11
.22
1.3
32
.15
All
Te
sts
All
Te
sts
Sta
ck T
est
Sta
ck T
est
On
lyO
nly
To
De
term
ine
Po
ten
tia
l E
mis
sio
ns: U
se e
mis
sio
n l
imit
fo
r N
Ox
an
d V
OC
.
Fo
rma
lde
hy
de
ha
s n
o l
imit
. U
se t
est
ing
av
era
ge
.
Fo
r C
O b
efo
re R
AC
T I
I, u
se e
mis
sio
n l
imit
.
Fo
r C
O a
fte
r R
AC
T I
I, e
mis
sio
n l
imit
s w
ere
re
mo
ve
d.
Use
te
stin
g a
ve
rag
e.
Co
mp
ress
or
Em
issi
on
s (F
rom
pis
ton
ro
d p
ack
ing
blo
w-b
y.
87
60
ho
urs
/ye
ar
Co
mp
osi
tio
n o
f N
atu
ral
Ga
sfr
om
20
15
To
nk
in A
nn
ua
l R
ep
ort
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
2 o
f 1
33
/2/2
01
8
MW
(g/g
mo
le)
Co
mp
osi
tio
n'
(mo
le %
)
De
nsi
ty o
f
Co
nst
itu
en
t
Ga
ses
(WO
Co
ntr
ibu
tio
n
to O
ve
rall
Sa
mp
le
De
nsi
ty
by
Sp
eci
es
(0)
Co
mp
osi
tio
n
(we
igh
t %
)
Ca
lcu
lati
on
of
Av
era
ge
MW
Me
tha
ne
16
93
.10
5%
0.6
75
0.6
29
87
.17
%1
4.8
96
8
Eth
an
e3
05
.42
5%
1.2
66
0.0
69
9.5
2%
1.6
27
5
Pro
pa
ne
44
0.2
62
%1
.85
70
.00
50
.67
%0
.11
52
8
Iso
bu
tan
e5
80
.02
4%
2.4
48
0.0
01
0.0
8%
0.0
13
92
n-B
uta
ne
58
0.0
37
%2
.44
80
.00
10
.13
%0
.02
14
6
Iso
pe
nta
ne
72
0.0
10
%3
.03
90
.00
00
.04
%0
.00
72
n-P
en
tan
e7
20
.00
6%
3.0
39
0.0
00
0.0
3%
0.0
04
32
He
xan
es+
86
0.0
21
%3
.63
00
.00
10
.11
%0
.01
80
6
Oxy
ge
n1
60
.00
0%
0.6
75
0.0
00
0.0
0%
0.0
00
00
Nit
rog
en
28
0.6
47
%1
.18
20
.00
81
.06
%0
.18
11
6
CO
24
40
.46
3%
1.8
57
0.0
09
1.1
9%
0.2
03
72
TO
TA
L1
00
.00
0%
0.7
21
10
0.0
00
%A
v.
MW
:1
7.0
89
42
1.0
00
00
.72
30
1.0
00
0
8N
um
be
r o
f P
isto
n R
od
s
11
.5sc
fh (
Av
era
ge
Blo
w-b
y f
rom
ea
ch r
od
, w
he
n p
ack
ing
is
ne
w.)
2M
ult
ipli
cati
on
Fa
cto
r fo
r co
mp
ress
ors
th
at
are
no
t su
bje
ct t
o 4
0 C
FR
Pa
rt 6
0,
Su
bp
art
OO
OO
.)
To
tal
Blo
w-b
y1
84
scfh
8.1
58
lb b
low
-by
/hr
87
60
ho
urs
/ye
ar
Ga
s d
en
sity
45
,03
8lb
/MM
scf
fro
m 2
01
5 T
on
kin
An
nu
al
Re
po
rt
VO
C c
on
ten
t1
.05
%w
eig
ht
%
HA
P c
on
ten
t0
.11
%w
eig
ht
%
Em
erg
en
cy G
en
era
tor
En
gin
e E
mis
sio
ns
Na
tura
l G
as
Ge
ne
rato
r E
ng
ine
(S
ou
rce
ID
10
3)
77
8
b
hp
50
0h
ou
rs/y
ea
r
Wa
uk
esh
a,
Mo
de
l N
o.
L-5
79
0-5
50
, S
I, 4
SR
B(N
ot
a l
imit
pri
or
to R
AC
T I
I.
Li
mit
ed
to
le
ss t
ha
n b
y R
AC
T I
I.)
Ou
tpu
t p
ow
er
77
8
bh
p
He
at/
Po
we
r R
ati
o8
,10
6
Btu
/bh
p-h
r(f
rom
Co
op
er
En
gin
e)
He
at
Inp
ut
6.3
06
47
45
43
MM
Btu
/hr
0.0
06
18
28
18
MM
CF
NG
/hr
Em
issi
on
Lim
its
NO
x1
8.8
7lb
/hr
82
.6tp
y(E
qu
iv t
o1
1.0
gra
m/h
p-h
r)
CO
3.7
2E
+0
0lb
/MM
Btu
fro
m A
P-4
2 T
ab
le 3
.2-3
VO
C2
.21
E+
00
lb/M
MB
tu f
rom
AP
-42
Ta
ble
3.2
-3
Fo
r P
M1
0 &
PM
2.5
Em
issi
on
s9
.50
E-0
3lb
PM
2.5
-FIL
/MM
Btu
9.5
0E
-03
lb P
M1
0-F
IL/M
MB
tuA
P-4
2 T
able
3.2
-3 U
nco
ntro
lled
4SR
B
9.9
1E
-03
lb P
M2
.5-C
ON
D/M
MB
tu9
.91
E-0
3lb
PM
10-C
ON
D/M
MB
tuA
P-4
2 T
able
3.2
-3 U
nco
ntro
lled
4SR
B
1.9
4E
-02
lb P
M2
.5/M
MB
tu1
.94
E-0
2lb
PM
10/M
MB
tu
(PM
-FIL
= P
M1
0-F
IL =
PM
2.5
-FIL
)
or
0.0
71
4G
m P
M2
.5/b
hp
-hr
0.0
71
4G
m P
M1
0/b
hp
-hr
NG
-fir
ed
Bo
ile
r E
mis
sio
ns
3.3
47
MM
Btu
/hr
87
60
ho
urs
/ye
ar
0.0
03
28
13
73
MM
CF
/hr
NO
x1
00
lb/M
MC
F N
G f
rom
AP
-42
Ta
ble
1.4
-1
CO
84
lb/M
MC
F N
G f
rom
AP
-42
Ta
ble
1.4
-1
VO
C5
.5lb
/MM
CF
NG
fro
m A
P-4
2 T
ab
le 1
.4-2
PM
10
7.6
lb/M
MC
F N
G f
rom
AP
-42
Ta
ble
1.4
-2
PM
2.5
7.6
lb/M
MC
F N
G f
rom
AP
-42
Ta
ble
1.4
-2
De
hy
Sti
ll &
Fla
re
87
60
ho
urs
/ye
ar
Co
nst
itu
en
t
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
3 o
f 1
33
/2/2
01
8
Fro
m A
IMs
EI
(TP
Y)
PM
10
NO
xC
OV
OC
CH
4C
O2
N2
OH
exa
ne
To
lue
ne
FO
RM
Be
nze
ne
20
16
0.0
40
.51
0.4
33
.96
0.0
15
96
.00
00
00
.12
49
0.1
40
0.8
1
20
15
0.0
30
.45
0.3
83
.95
0.0
15
29
00
.12
46
0.1
40
0.8
1
20
14
0.0
40
.50
.42
3.9
50
.01
58
30
0.1
24
60
.14
00
.81
20
13
0.0
40
.49
0.4
12
.97
0.0
15
74
00
.11
0.1
40
0.5
3
20
12
0.0
30
.36
0.3
2.1
70
.01
41
60
0.1
0.1
40
.52
Use
Hig
he
st V
alu
e f
or
Po
ten
tia
l E
mis
sio
n0
.04
0.5
10
.43
3.9
60
.01
59
60
0.1
24
90
.14
00
.81
Sto
rag
e T
an
k E
mis
sio
ns
0.0
3T
PY
VO
C(1
99
5 T
VO
P a
pp
lica
tio
n)
87
60
ho
urs
/ye
ar
0.0
3T
PY
G
LYE
T(1
99
5 T
VO
P a
pp
lica
tio
n)
Pa
rts
Wa
she
r E
mis
sio
ns
VO
C0
.49
tpy
(fro
m 2
00
8 J
B T
on
kin
TR
D)
87
60
ho
urs
/ye
ar
Xy
len
e1
%0
.00
49
tpy
HA
Ps
we
re p
rop
ort
ion
ed
fro
m V
OC
, u
sin
g 4
0 C
FR
Pa
rt 6
3,
Su
bp
art
VV
V,
Ta
ble
6.
To
lue
ne
1%
0.0
04
9tp
y
Eth
ylb
en
zen
e1
%0
.00
49
tpy
Fo
r th
is e
mis
sio
n e
stim
ate
, a
ssu
me
th
at
the
ir t
ota
l e
mis
sio
ns
are
eq
ua
l to
th
e s
ing
le p
art
s w
ash
er
at
JB T
on
kin
.
Fa
cili
ty P
um
ps,
Va
lve
s, F
lan
ge
s, e
tc.
Em
issi
on
s
VO
Cs
12
.50
00
tpy
(fro
m 1
99
5 T
VO
P a
pp
lica
tio
n)
87
60
ho
urs
/ye
ar
Be
nze
ne
0.0
04
0
To
lue
ne
0.0
07
0
Eth
ylb
en
zen
e0
.00
04
Xy
len
es
0.0
02
0
He
xan
e0
.05
50
GLY
ET
4.1
00
0
To
tal
HA
Ps
4.1
68
4
IDS
ou
rce
Na
me
Gm
/ b
hp
-hr
lb/
hr
TP
YG
m/
bh
p-h
rlb
/ h
rT
PY
Gm
/ b
hp
-hr
lb/
hr
TP
YG
m/
bh
p-h
rlb
/ h
rT
PY
Gm
/ b
hp
-hr
lb/
hr
TP
Y
31
Aja
x B
oil
er
1 (
3.3
47
MM
Btu
/hr,
NG
)10
.02
50
.11
0.0
25
0.1
10
.33
1.4
40
.28
1.2
10
.01
80
0.0
8
10
1C
oo
pe
r E
ng
ine
1 (
6,3
50
-bh
p,
NG
, S
I, 2
SLB
)20
.17
82
.51
0.8
90
.17
82
.51
0.8
99
.01
25
.99
55
1.8
04
.00
56
.00
24
5.3
02
.00
28
.00
12
2.6
0
10
2C
oo
pe
r E
ng
ine
2 (
6,3
50
-bh
p,
NG
, S
I, 2
SLB
)20
.17
82
.51
0.8
90
.17
82
.51
0.8
99
.01
25
.99
55
1.8
04
.00
56
.00
24
5.3
02
.00
28
.00
12
2.6
0
10
3
Wa
uk
esh
a A
ux.
Em
erg
en
cy
Ge
ne
rato
r E
ng
ine
1 (
77
8-b
hp
,
NG
, S
I, 4
SR
B)3
0.0
71
0.1
22
0.0
30
.07
10
.12
20
.03
11
.01
8.8
78
2.6
01
3.6
82
3.4
65
.87
8.1
13
.94
3.4
8
10
5G
lyco
l D
eh
yd
rati
on
Sy
ste
m4
0.0
09
10
.04
0.0
09
10
.04
0.1
16
0.5
10
.09
80
.43
0.9
03
.96
11
0S
tora
ge
Ta
nk
P-1
, 1
0,0
00
-Ga
l50
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
70
.03
11
12
Pa
rts
Wa
she
rs6
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
12
0.4
9
11
2
2 N
G C
om
pre
sso
rs #
1 a
nd
#2
(Dri
ve
n b
y S
ou
rce
ID
s 1
01
&
10
2)7
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
71
0.7
5
11
3
2 C
oo
pe
r, N
G C
om
pre
sso
rs #
3
an
d #
4 (
Dri
ve
n b
y 5
,75
0-b
hp
,
ele
ctri
c m
oto
rs)7
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
71
0.7
5
P0
1F
aci
lity
Pu
mp
s, V
alv
es,
Fla
ng
es,
etc
.40
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
02
.91
2.5
0
Fa
cili
ty T
ota
l5
.12
1.9
65
.12
1.9
62
71
11
88
.15
13
64
98
.10
74
26
7.2
4
Th
e t
wo
Pa
rts
Wa
she
rs (
So
urc
e I
D 1
11
) w
ere
no
t in
clu
de
d i
n t
he
in
itia
l 1
99
7 T
VO
P.
Th
ey
we
re n
ot
me
nti
on
ed
in
th
e 2
00
2 T
VO
P r
en
ew
al
ap
pli
cati
on
. H
ow
ev
er,
th
ey
we
re a
dd
ed
in
th
e 2
00
7 T
VO
P r
en
ew
al.
Tab
le 2
A:
Pot
enti
al C
rite
ria
Em
issi
ons
prio
r to
inst
alla
tion
of
Cle
an B
urn
Con
trol
on
the
Com
pres
sor
Eng
ines
and
RA
CT
II
Req
uire
men
tsD
omin
ion
Tra
nsm
issi
on, I
nc -
Sou
th O
akfo
rd C
ompr
essi
on S
tati
on (
TV
OP
-65-
0084
0)E
mis
sio
ns
PM
2.5
PM
10
NO
xC
OV
OC
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
4 o
f 1
33
/2/2
01
8
1E
mis
sio
ns
are
ba
sed
on
AP
-42
.2E
mis
sio
n o
f N
Ox,
CO
, a
nd
VO
C a
re b
ase
d o
n p
erm
it l
imit
s.
Oth
er
em
issi
on
s a
re b
ase
d o
n A
P-4
2.
3E
mis
sio
n o
f N
Ox
is b
ase
d o
n p
erm
it l
imit
s.
Oth
er
em
issi
on
s a
re b
ase
d o
n A
P-4
2.
4E
mis
sio
ns
we
re s
up
pli
ed
by
th
e c
om
pa
ny
an
d a
re t
he
pe
ak
an
nu
al
em
issi
on
s o
ve
r 2
01
2 -
20
16
.5E
mis
sio
ns
we
re s
up
pli
ed
by
th
e c
om
pa
ny
.6E
mis
sio
ns
for
2 p
art
s w
ash
ers
, to
ge
the
r, w
ere
ass
um
ed
to
be
th
e s
am
e a
s th
e s
ing
le p
art
s w
ash
er
at
JB T
on
kin
.7B
low
-by
em
issi
on
s fr
om
th
e c
om
pre
sso
r a
re b
ase
d o
n 2
3 (
11
.5*
2)
scfh
/pis
ton
ro
d (
EP
A E
ne
rgy
Sta
r),
4 p
isto
n r
od
s, a
nd
NG
an
aly
sis
sup
pli
ed
by
th
e c
om
pa
ny
, in
its
20
15
an
nu
al
rep
ort
.
Va
lue
s re
po
rte
d i
n t
his
ta
ble
we
re r
ou
nd
ed
fro
m c
alc
ula
tio
ns
pe
rfo
rme
d e
lse
wh
ere
.
To
tal
faci
lity
em
issi
on
s a
re a
co
mb
ina
tio
n o
f re
gu
late
d p
ote
nti
al
em
issi
on
s a
nd
est
ima
ted
em
issi
on
s.
IB.
Cri
teri
a E
mis
sio
ns
aft
er
inst
all
ati
on
of
Cle
an
Bu
rn C
on
tro
l o
n t
he
Co
mp
ress
or
En
gin
es
an
d R
AC
T I
I re
qu
ire
me
nts
.
A
. C
lea
n B
urn
Co
ntr
ol
wa
s a
dd
ed
as
a c
on
tro
l o
n e
ach
of
two
co
mp
ress
or
en
gin
es
(So
urc
e I
Ds
10
1 &
10
2)
on
Ap
ril
18
, 2
01
7,
to l
ow
er
NO
x e
mis
sio
ns.
B
. T
he
ad
de
d c
on
tro
l e
na
ble
s th
ese
en
gin
es
to u
se t
he
pre
sum
pti
ve
RA
CT
II
em
issi
on
lim
it i
n 1
29
. 9
7(g
)(3
)(A
) &
(B
) o
f:
3.0
gra
ms
NO
x/b
hp
-hr
An
d
1.0
gra
ms
VO
C/b
hp
-hr
Th
is l
imit
s w
ere
ad
de
d t
o t
he
pro
po
sed
TV
OP
.
C
. N
eit
he
r R
AC
T I
no
r R
AC
T I
I, r
eg
ula
te C
O.
Th
ere
fore
, th
e C
O e
mis
sio
n l
imit
s w
ere
im
pro
pe
rly
ad
de
d i
n t
he
old
TV
OP
, a
nd
th
e C
O l
imit
s h
av
e b
ee
n r
em
ov
ed
fro
m t
he
pro
po
sed
pe
rmit
.
IDS
ou
rce
Na
me
Gm
/ b
hp
-hr
lb/
hr
TP
YG
m/
bh
p-h
rlb
/ h
rT
PY
Gm
/ b
hp
-hr
lb/
hr
TP
YG
m/
bh
p-h
rlb
/ h
rT
PY
Gm
/ b
hp
-hr
lb/
hr
TP
Y
31
Aja
x B
oil
er
1 (
3.3
47
MM
Btu
/hr,
NG
)10
.02
5
0.1
1
0.0
25
0.1
1
0.3
3
1
.44
0
.28
1.2
1
0.0
18
0.0
8
10
1C
oo
pe
r E
ng
ine
1 (
6,3
50
-bh
p,
NG
, S
I, 2
SLB
)20
.17
82
.5
10
.89
0
.17
82
.5
10
.89
3
.04
2
1
83
.95
0
.85
11
.2
49
.13
1
.00
14
.0
61
.32
10
2C
oo
pe
r E
ng
ine
2 (
6,3
50
-bh
p,
NG
, S
I, 2
SLB
)20
.17
82
.5
10
.89
0
.17
82
.5
10
.89
3
.04
2
1
83
.95
0
.85
11
.2
49
.13
1
.00
14
.0
61
.32
10
3
Wa
uk
esh
a A
ux.
Em
erg
en
cy
Ge
ne
rato
r E
ng
ine
1 (
77
8-b
hp
,
NG
, S
I, 4
SR
B)3
0.0
71
0.1
22
0
.03
0
.07
10
.12
2
0
.03
1
1.0
18
.9
4
.72
1
3.7
23
.5
5
.87
8
.11
3.9
3.4
8
10
5G
lyco
l D
eh
yd
rati
on
Sy
ste
m4
0.0
09
1
0.0
4
0.0
09
0.0
4
0.1
16
0.5
1
0.0
98
0.4
3
0.9
0
3
.96
11
0S
tora
ge
Ta
nk
P-1
, 1
0,0
00
-
Ga
l50
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
68
0.0
3
11
12
Pa
rts
Wa
she
rs6
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
12
0.4
9
11
2
2 N
G C
om
pre
sso
rs #
1 a
nd
#2
(Dri
ve
n b
y S
ou
rce
ID
s 1
01
&
10
2)7
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
71
0.7
5
11
3
2 C
oo
pe
r, N
G C
om
pre
sso
rs #
3
an
d #
4 (
Dri
ve
n b
y 5
,75
0-b
hp
,
ele
ctri
c m
oto
rs)7
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.1
71
0.7
5
P0
1F
aci
lity
Pu
mp
s, V
alv
es,
Fla
ng
es,
etc
.40
.00
0.0
00
.00
0.0
00
.00
0.0
00
.00
0.0
02
.9
12
.50
Fa
cili
ty T
ota
l5
.1
21
.96
5
.1
21
.96
1
03
37
4.5
64
6
1
05
.76
4
6
1
44
.68
All
em
issi
on
so
urc
es,
exc
ep
t th
e e
me
rge
ncy
ge
ne
rato
r e
ng
ine
(S
ou
rce
ID
10
4),
at
the
fa
cili
ty o
pe
rate
8,7
60
ho
urs
pe
r y
ea
r.
Th
e e
me
rge
ncy
ge
ne
rato
r, i
s li
mit
ed
to
a m
axi
mu
m o
pe
rati
on
le
ss t
ha
n 5
00
ho
urs
pe
r y
ea
r.8C
oo
pe
r E
ng
ine
s 1
& 2
are
su
bje
ct t
o t
he
RA
CT
II
pre
sum
pti
ve
NO
x e
mis
sio
n l
imit
of
3.0
gra
ms/
bh
p-h
r d
uri
ng
no
rma
l o
pe
rati
on
at
rate
d l
oa
d.
9W
hil
e h
ou
rly
NO
x e
mis
sio
ns
are
sti
ll b
ase
d o
n t
he
em
issi
on
lim
it,
an
nu
al
em
issi
on
s o
f N
Ox
are
ba
sed
on
th
e h
ou
rly
lim
it a
nd
50
0 h
r/y
r o
pe
rati
on
.
II.
HA
P E
mis
sio
ns
All
em
issi
on
so
urc
es,
exc
ep
t th
e e
me
rge
ncy
ge
ne
rato
r, a
t th
e f
aci
lity
op
era
te 8
,76
0 h
ou
rs p
er
ye
ar.
F
or
em
issi
on
s fr
om
th
e e
me
rge
ncy
ge
ne
rato
r o
the
r th
an
NO
x, w
hil
e n
ot
lim
ite
d,
is a
ssu
me
d t
o o
pe
rate
50
0 h
ou
rs p
er
ye
ar.
Tab
le 2
B:
Pot
enti
al C
rite
ria
Em
issi
ons
afte
r in
stal
lati
on o
f C
lean
Bur
n C
ontr
ol o
n th
e C
ompr
esso
r E
ngin
es a
nd R
AC
T I
I re
quir
emen
ts.
Dom
inio
n T
rans
mis
sion
, Inc
- S
outh
Oak
ford
Com
pres
sion
Sta
tion
(T
VO
P-6
5-00
840)
Em
issi
on
s
PM
2.5
PM
10
NO
xC
OV
OC
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
5 o
f 1
33
/2/2
01
8
HA
Ps
fro
m N
G-f
ire
d b
oil
er
AP
-42
, C
ha
pte
r 1
-4 N
atu
ral
Ga
s F
ire
d B
oil
ers
Ta
ble
s 1
.4-3
& 4
No
.
Use
th
ese
nu
me
ric
fact
ors
(Va
lue
s)
HA
P E
mis
sio
n F
act
ors
lb/M
MC
Flb
/hr
tpy
2-M
eth
yln
ap
hth
ale
ne
2.4
0E
-05
7.8
8E
-08
3.4
5E
-07
3-M
eth
ylc
hlo
ran
thre
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
7,1
2-D
ime
thy
lbe
nz(
a)a
nth
race
ne
8.0
0E
-06
2.6
3E
-08
1.1
5E
-07
Ace
na
ph
the
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
Ace
na
ph
thy
len
e9
.00
E-0
72
.95
E-0
91
.29
E-0
8
An
thra
cen
e1
.20
E-0
63
.94
E-0
91
.72
E-0
8
Be
nz(
a)a
nth
race
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
Be
nze
ne
2.1
0E
-03
6.8
9E
-06
3.0
2E
-05
Be
nzo
(a)p
yre
ne
6.0
0E
-07
1.9
7E
-09
8.6
2E
-09
Be
nzo
(b)f
luo
ran
the
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
Be
nzo
(g,h
,i)p
ery
len
e6
.00
E-0
71
.97
E-0
98
.62
E-0
9
Be
nzo
(k)f
luo
ran
the
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
Ch
ryse
ne
9.0
0E
-07
2.9
5E
-09
1.2
9E
-08
Dib
en
zo(a
,h)a
nth
race
ne
6.0
0E
-07
1.9
7E
-09
8.6
2E
-09
Dic
hlo
rob
en
zen
e1
.20
E-0
33
.94
E-0
61
.72
E-0
5
Flu
ora
nth
en
e3
.00
E-0
69
.84
E-0
94
.31
E-0
8
Flu
ore
ne
2.8
0E
-06
9.1
9E
-09
4.0
2E
-08
Fo
rma
lde
hy
de
7.5
0E
-02
2.4
6E
-04
1.0
8E
-03
He
xan
e1
.80
E+
00
5.9
1E
-03
2.5
9E
-02
Ind
en
o(1
,2,3
-cd
)py
ren
e9
.00
E-0
72
.95
E-0
91
.29
E-0
8
Na
ph
tha
len
e6
.10
E-0
42
.00
E-0
68
.77
E-0
6
Ph
en
an
ath
ren
e1
.70
E-0
55
.58
E-0
82
.44
E-0
7
Py
ren
e5
.00
E-0
61
.64
E-0
87
.19
E-0
8
To
lue
ne
3.4
0E
-03
1.1
2E
-05
4.8
9E
-05
Ars
en
ic2
.00
E-0
46
.56
E-0
72
.87
E-0
6
Be
ryll
ium
6.0
0E
-06
1.9
7E
-08
8.6
2E
-08
Ca
dm
ium
1.1
0E
-03
3.6
1E
-06
1.5
8E
-05
Ch
rom
ium
1.4
0E
-03
4.5
9E
-06
2.0
1E
-05
Co
ba
lt8
.40
E-0
52
.76
E-0
71
.21
E-0
6
Ma
ng
an
ese
3.8
0E
-04
1.2
5E
-06
5.4
6E
-06
Me
rcu
ry2
.60
E-0
48
.53
E-0
73
.74
E-0
6
Nic
ke
l2
.10
E-0
36
.89
E-0
63
.02
E-0
5
Se
len
ium
1.2
0E
-05
3.9
4E
-08
1.7
2E
-07
HA
Ps
fro
m C
om
pre
sso
r E
ng
ine
s (S
ou
rce
ID
s 1
01
an
d 1
02
)
HA
P
AP
-42
Un
con
tro
lle
d
Em
issi
on
Fa
cto
r
lb/M
MB
tulb
/hr
tpy
1,1
,2,2
-Te
tra
chlo
roe
tha
ne
6.6
3E
-05
6.8
3E
-03
2.9
9E
-02
1,1
,2-T
rich
loro
eth
an
e0
.00
00
52
75
.43
E-0
32
.38
E-0
2
1,3
-Dic
hlo
rop
rop
en
e0
.00
00
43
84
.51
E-0
31
.97
E-0
2
2,2
,4-T
rim
eth
ylp
en
tan
e0
.00
08
46
8.7
1E
-02
3.8
1E
-01
2-M
eth
yln
ap
hth
ale
ne
0.0
00
02
14
2.2
0E
-03
9.6
5E
-03
Ace
na
ph
the
ne
0.0
00
00
13
31
.37
E-0
46
.00
E-0
4
Ace
na
ph
thy
len
e0
.00
00
03
17
3.2
6E
-04
1.4
3E
-03
Ace
tald
eh
yd
e0
.00
77
67
.99
E-0
13
.50
E+
00
Acr
ole
in0
.00
77
88
.01
E-0
13
.51
E+
00
An
thra
cen
e0
.00
00
00
71
87
.39
E-0
53
.24
E-0
4
Be
nz(
a)a
nth
race
ne
0.0
00
00
03
36
3.4
6E
-05
1.5
2E
-04
Be
nze
ne
0.0
01
94
2.0
0E
-01
8.7
5E
-01
Be
nzo
(a)p
yre
ne
5.6
8E
-09
5.8
5E
-07
2.5
6E
-06
Be
nzo
(b)f
luo
ran
the
ne
8.5
1E
-09
8.7
6E
-07
3.8
4E
-06
Be
nzo
(e)p
yre
ne
2.3
4E
-08
2.4
1E
-06
1.0
6E
-05
Be
nzo
(g,h
,i)p
ery
len
e2
.48
E-0
82
.55
E-0
61
.12
E-0
5
Be
nzo
(k)f
luo
ran
the
ne
4.2
6E
-09
4.3
9E
-07
1.9
2E
-06
Bip
he
ny
l0
.00
00
03
95
4.0
7E
-04
1.7
8E
-03
Ca
rbo
n T
etr
ach
lori
de
0.0
00
06
07
6.2
5E
-03
2.7
4E
-02
Bo
ile
r (
So
urc
e I
D 0
31
)
(Un
con
tro
lle
d E
Fs
fro
m A
P-4
2,
Ta
ble
3.2
-1,
2S
LB)
Su
m o
f C
om
pre
sso
r E
ng
ine
s 1
& 2
(S
ou
rce
ID
s 1
01
& 1
02
)
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
6 o
f 1
33
/2/2
01
8
Ch
loro
be
nze
ne
0.0
00
04
44
4.5
7E
-03
2.0
0E
-02
Ch
loro
form
0.0
00
04
71
4.8
5E
-03
2.1
2E
-02
Ch
ryse
ne
0.0
00
00
06
72
6.9
2E
-05
3.0
3E
-04
Eth
ylb
en
zen
e0
.00
01
08
1.1
1E
-02
4.8
7E
-02
Eth
yle
ne
Dib
rom
ide
0.0
00
07
34
7.5
6E
-03
3.3
1E
-02
Flu
ora
nth
en
e0
.00
00
00
36
13
.72
E-0
51
.63
E-0
4
Flu
ore
ne
0.0
00
00
16
91
.74
E-0
47
.62
E-0
4
Fo
rma
lde
hy
de
0.0
55
25
.68
E+
00
2.4
9E
+0
1
Ind
en
o(1
,2,3
-c,d
)py
ren
e9
.93
E-0
91
.02
E-0
64
.48
E-0
6
Me
tha
no
l0
.00
24
82
.55
E-0
11
.12
E+
00
Me
thy
len
e C
hlo
rid
e0
.00
01
47
1.5
1E
-02
6.6
3E
-02
n-H
exa
ne
0.0
00
44
54
.58
E-0
22
.01
E-0
1
Na
ph
tha
len
e0
.00
00
96
39
.91
E-0
34
.34
E-0
2
PA
H0
.00
01
34
1.3
8E
-02
6.0
4E
-02
Pe
ryle
ne
4.9
7E
-09
5.1
2E
-07
2.2
4E
-06
Ph
en
an
thre
ne
0.0
00
00
35
33
.63
E-0
41
.59
E-0
3
Ph
en
ol
0.0
00
04
21
4.3
3E
-03
1.9
0E
-02
Py
ren
e0
.00
00
00
58
46
.01
E-0
52
.63
E-0
4
Sty
ren
e0
.00
00
54
85
.64
E-0
32
.47
E-0
2
To
lue
ne
0.0
00
96
39
.91
E-0
24
.34
E-0
1
Vin
yl
Ch
lori
de
0.0
00
02
47
2.5
4E
-03
1.1
1E
-02
Xy
len
e0
.00
02
68
2.7
6E
-02
1.2
1E
-01
TH
AP
s0
.07
87
15
12
To
tal
8.1
03
43
35
.49
30
3
Co
mp
ress
or
En
gin
e -
Sta
ck T
est
ing
fo
r F
orm
ald
eh
yd
e
lb/h
rtp
y@
full
uti
liza
tio
n
3/1
3/2
01
3E
ng
ine
12
.24
9.8
1
3/1
3/2
01
3E
ng
ine
22
.05
8.9
8
Use
th
is t
est
ing
va
lue
fo
r F
OR
M i
nst
ea
d o
f A
P-4
2T
ota
l4
.29
18
.79
HA
Ps
fro
m E
me
rge
ncy
Au
xil
iary
En
gin
e (
So
urc
e I
D 1
03
)
HA
P
AP
-42
Un
con
tro
lle
d
Em
issi
on
Fa
cto
r
lb/M
MB
tulb
/MM
Btu
lb/h
rtp
y
1,1
,2,2
-Te
tra
chlo
roe
tha
ne
2.5
3E
-05
0.0
00
02
53
1.6
0E
-04
3.9
9E
-05
1,1
,2-T
rich
loro
eth
an
e<
1.5
3E
-05
7.6
5E
-06
4.8
2E
-05
1.2
1E
-05
1,1
-Dic
hlo
roe
tha
ne
<1
.13
E-0
55
.65
E-0
63
.56
E-0
58
.91
E-0
6
1,2
-Dic
hlo
roe
tha
ne
<1
.13
E-0
55
.65
E-0
63
.56
E-0
58
.91
E-0
6
1,2
-Dic
hlo
rop
rop
an
e<
1.3
0E
-05
0.0
00
00
65
4.1
0E
-05
1.0
2E
-05
1,3
-Bu
tad
ien
e6
.63
E-0
40
.00
06
63
4.1
8E
-03
1.0
5E
-03
1,3
-Dic
hlo
rop
rop
en
e<
1.2
7E
-05
6.3
5E
-06
4.0
0E
-05
1.0
0E
-05
Ace
tald
eh
yd
e2
.79
E-0
30
.00
27
91
.76
E-0
24
.40
E-0
3
Acr
ole
in2
.63
E-0
30
.00
26
31
.66
E-0
24
.15
E-0
3
Be
nze
ne
1.5
8E
-03
0.0
01
58
9.9
6E
-03
2.4
9E
-03
Bu
tyr/
iso
bu
tyra
lde
hy
de
4.8
6E
-05
0.0
00
04
86
3.0
6E
-04
7.6
6E
-05
Ca
rbo
n T
etr
ach
lori
de
<1
.77
E-0
58
.85
E-0
65
.58
E-0
51
.40
E-0
5
Ch
loro
be
nze
ne
<1
.29
E-0
56
.45
E-0
64
.07
E-0
51
.02
E-0
5
Ch
loro
form
<1
.37
E-0
56
.85
E-0
64
.32
E-0
51
.08
E-0
5
Eth
ylb
en
zen
e<
2.4
8E
-05
0.0
00
01
24
7.8
2E
-05
1.9
6E
-05
Eth
yle
ne
Dib
rom
ide
<2
.13
E-0
51
.06
5E
-05
6.7
2E
-05
1.6
8E
-05
Fo
rma
lde
hy
de
2.0
5E
-02
0.0
20
51
.29
E-0
13
.23
E-0
2
Me
tha
no
l3
.06
E-0
30
.00
30
61
.93
E-0
24
.82
E-0
3
Me
thy
len
e C
hlo
rid
e4
.12
E-0
50
.00
00
41
22
.60
E-0
46
.50
E-0
5
Na
ph
tha
len
e<
9.7
1E
-05
4.8
55
E-0
53
.06
E-0
47
.65
E-0
5
PA
H1
.41
E-0
40
.00
01
41
8.8
9E
-04
2.2
2E
-04
Sty
ren
e<
1.1
9E
-05
5.9
5E
-06
3.7
5E
-05
9.3
8E
-06
To
lue
ne
5.5
8E
-04
0.0
00
55
83
.52
E-0
38
.80
E-0
4
Vin
yl
Ch
lori
de
<7
.18
E-0
63
.59
E-0
62
.26
E-0
55
.66
E-0
6
Xy
len
e1
.95
E-0
40
.00
01
95
1.2
3E
-03
3.0
7E
-04
To
tal
0.2
04
12
0.0
51
03
HA
Ps
fro
m C
om
pre
sso
r E
mis
sio
ns
(Fro
m p
isto
n r
od
pa
ckin
g b
low
-by
.)
Fo
rma
lde
hy
de
(Un
con
tro
lle
d E
Fs
fro
m A
P-4
2,
Ta
ble
3.2
-3,
4S
RB
)
Em
issi
on
s fr
om
Em
erg
en
cy
Au
xili
ary
En
gin
e (
So
urc
e I
D
10
3)
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
7 o
f 1
33
/2/2
01
8
lb/h
rtp
y
To
tal
HA
Ps
0.0
08
97
0.0
39
30
56
66
HA
Ps
in P
art
s W
ash
er
(So
urc
e I
D 5
00
)
Xy
len
e0
.00
49
(fro
m 2
00
8 J
B T
on
kin
TR
D)
To
lue
ne
0.0
04
9
Eth
ylb
en
zen
e0
.00
49
To
tal
0.0
14
7
HA
Ps
in F
aci
lity
Pu
mp
s, V
alv
es,
Fla
ng
es,
etc
. E
mis
sio
ns
(So
urc
e I
D P
01
)(f
rom
19
95
TV
OP
ap
pli
cati
on
)
Be
nze
ne
0.0
04
To
lue
ne
0.0
07
Xy
len
es
0.0
02
He
xan
e0
.05
5
GLY
ET
4.1
To
tal
HA
Ps
4.1
68
4
031
101
&
102
103
10
51
12
& 1
13
11
0,
11
1,
&
P0
1F
aci
lity
To
tal
Bo
ile
r
Co
mpr
ess
or
Eng
ines
Em
erge
ncy
Gen
erat
or
Eng
ine
Gly
col
De
hy
dra
tio
n
Sy
ste
m
4 N
G
Co
mp
ress
ors
Sto
rag
e T
an
k,
Pa
rts
Wa
she
rs,
Pip
ing
2-M
eth
yln
ap
hth
ale
ne
3.4
49
38
E-0
7
3-M
eth
ylc
hlo
ran
thre
ne
1.2
93
52
E-0
8
7,1
2-D
ime
thy
lbe
nz(
a)a
nth
race
ne
1.1
49
79
E-0
7
Ace
na
ph
the
ne
1.2
93
52
E-0
8
Ace
na
ph
thy
len
e1
.29
35
2E
-08
An
thra
cen
e1
.72
46
9E
-08
Be
nz(
a)a
nth
race
ne
1.2
93
52
E-0
8
Be
nze
ne
3.0
18
21
E-0
5
Be
nzo
(a)p
yre
ne
8.6
23
45
E-0
9
Be
nzo
(b)f
luo
ran
the
ne
1.2
93
52
E-0
8
Be
nzo
(g,h
,i)p
ery
len
e8
.62
34
5E
-09
Be
nzo
(k)f
luo
ran
the
ne
1.2
93
52
E-0
8
Ch
ryse
ne
1.2
93
52
E-0
8
Dib
en
zo(a
,h)a
nth
race
ne
8.6
23
45
E-0
9
Dic
hlo
rob
en
zen
e1
.72
46
9E
-05
Flu
ora
nth
en
e4
.31
17
2E
-08
Flu
ore
ne
4.0
24
28
E-0
8
Fo
rma
lde
hy
de
0.0
01
07
79
31
He
xan
e0
.02
58
70
34
1
Ind
en
o(1
,2,3
-cd
)py
ren
e1
.29
35
2E
-08
Na
ph
tha
len
e8
.76
71
7E
-06
Ph
en
an
ath
ren
e2
.44
33
1E
-07
Py
ren
e7
.18
62
1E
-08
To
lue
ne
4.8
86
62
E-0
5
Ars
en
ic2
.87
44
8E
-06
Be
ryll
ium
8.6
23
45
E-0
8
Ca
dm
ium
1.5
80
97
E-0
5
Ch
rom
ium
2.0
12
14
E-0
5
Co
ba
lt1
.20
72
8E
-06
Ma
ng
an
ese
5.4
61
52
E-0
6
Me
rcu
ry3
.73
68
3E
-06
Nic
ke
l3
.01
82
1E
-05
Se
len
ium
1.7
24
69
E-0
7
1,1
,2,2
-Te
tra
chlo
roe
tha
ne
2.9
9E
-02
1,1
,2-T
rich
loro
eth
an
e2
.38
E-0
2
1,3
-Dic
hlo
rop
rop
en
e1
.97
E-0
2
2,2
,4-T
rim
eth
ylp
en
tan
e3
.81
E-0
1
tpy
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
8 o
f 1
33
/2/2
01
8
2-M
eth
yln
ap
hth
ale
ne
9.6
5E
-03
Ace
na
ph
the
ne
6.0
0E
-04
Ace
na
ph
thy
len
e1
.43
E-0
3
Ace
tald
eh
yd
e3
.50
E+
00
Acr
ole
in3
.51
E+
00
An
thra
cen
e3
.24
E-0
4
Be
nz(
a)a
nth
race
ne
1.5
2E
-04
Be
nze
ne
8.7
5E
-01
Be
nzo
(a)p
yre
ne
2.5
6E
-06
Be
nzo
(b)f
luo
ran
the
ne
3.8
4E
-06
Be
nzo
(e)p
yre
ne
1.0
6E
-05
Be
nzo
(g,h
,i)p
ery
len
e1
.12
E-0
5
Be
nzo
(k)f
luo
ran
the
ne
1.9
2E
-06
Bip
he
ny
l1
.78
E-0
3
Ca
rbo
n T
etr
ach
lori
de
2.7
4E
-02
Ch
loro
be
nze
ne
2.0
0E
-02
Ch
loro
form
2.1
2E
-02
Ch
ryse
ne
3.0
3E
-04
Eth
ylb
en
zen
e4
.87
E-0
2
Eth
yle
ne
Dib
rom
ide
3.3
1E
-02
Flu
ora
nth
en
e1
.63
E-0
4
Flu
ore
ne
7.6
2E
-04
Fo
rma
lde
hy
de
1.8
8E
+0
1
Ind
en
o(1
,2,3
-c,d
)py
ren
e4
.48
E-0
6
Me
tha
no
l1
.12
E+
00
Me
thy
len
e C
hlo
rid
e6
.63
E-0
2
n-H
exa
ne
2.0
1E
-01
Na
ph
tha
len
e4
.34
E-0
2
PA
H6
.04
E-0
2
Pe
ryle
ne
2.2
4E
-06
Ph
en
an
thre
ne
1.5
9E
-03
Ph
en
ol
1.9
0E
-02
Py
ren
e2
.63
E-0
4
Sty
ren
e2
.47
E-0
2
To
lue
ne
4.3
4E
-01
Vin
yl
Ch
lori
de
1.1
1E
-02
Xy
len
e1
.21
E-0
1
1,1
,2,2
-Te
tra
chlo
roe
tha
ne
3.9
9E
-05
1,1
,2-T
rich
loro
eth
an
e1
.21
E-0
5
1,1
-Dic
hlo
roe
tha
ne
8.9
1E
-06
1,2
-Dic
hlo
roe
tha
ne
8.9
1E
-06
1,2
-Dic
hlo
rop
rop
an
e1
.02
E-0
5
1,3
-Bu
tad
ien
e1
.05
E-0
3
1,3
-Dic
hlo
rop
rop
en
e1
.00
E-0
5
Ace
tald
eh
yd
e4
.40
E-0
3
Acr
ole
in4
.15
E-0
3
Be
nze
ne
2.4
9E
-03
Bu
tyr/
iso
bu
tyra
lde
hy
de
7.6
6E
-05
Ca
rbo
n T
etr
ach
lori
de
1.4
0E
-05
Ch
loro
be
nze
ne
1.0
2E
-05
Ch
loro
form
1.0
8E
-05
Eth
ylb
en
zen
e1
.96
E-0
5
Eth
yle
ne
Dib
rom
ide
1.6
8E
-05
Fo
rma
lde
hy
de
3.2
3E
-02
Me
tha
no
l4
.82
E-0
3
Me
thy
len
e C
hlo
rid
e6
.50
E-0
5
Na
ph
tha
len
e7
.65
E-0
5
PA
H2
.22
E-0
4
Sty
ren
e9
.38
E-0
6
To
lue
ne
8.8
0E
-04
Vin
yl
Ch
lori
de
5.6
6E
-06
Xy
len
e3
.07
E-0
4
He
xan
e1
.25
E-0
1
To
lue
ne
1.4
0E
-01
FO
RM
0.0
0E
+0
0
Be
nze
ne
8.1
0E
-01
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
9 o
f 1
33
/2/2
01
8
To
tal
HA
Ps
1.5
7E
-01
GLY
ET
3.0
0E
-02
Xy
len
e4
.90
E-0
3
To
lue
ne
4.9
0E
-03
Eth
ylb
en
zen
e4
.90
E-0
3
Be
nze
ne
4.0
0E
-03
To
lue
ne
7.0
0E
-03
Eth
ylb
en
zen
e4
.00
E-0
4
Xy
len
es
2.0
0E
-03
He
xan
e5
.50
E-0
2
GLY
ET
4.1
0E
+0
0
031
101
&
102
103
10
51
12
& 1
13
11
0,
11
1,
&
P0
1F
aci
lity
To
tal
Bo
ile
r
Co
mpr
ess
or
Eng
ines
Em
erge
ncy
Gen
erat
or
Eng
ine
Gly
col
De
hy
dra
tio
n
Sy
ste
m
4 N
G
Co
mp
ress
ors
Sto
rag
e T
an
k,
Pa
rts
Wa
she
rs,
Pip
ing
Fo
rma
lde
hy
de
0.0
01
07
79
31
1.8
8E
+0
13
.23
E-0
20
.00
E+
00
18
.82
35
98
61
GLY
ET
4.1
3E
+0
04
.13
Acr
ole
in3
.51
E+
00
3.2
1E
-03
3.5
11
24
89
26
Ace
tald
eh
yd
e3
.50
E+
00
4.4
0E
-03
3.5
03
42
01
99
Be
nze
ne
3.0
18
21
E-0
58
.75
E-0
12
.49
E-0
38
.10
E-0
14
.00
E-0
31
.69
12
76
59
8
Me
tha
no
l1
.12
E+
00
4.8
2E
-03
1.1
23
06
84
16
To
lue
ne
4.8
86
62
E-0
54
.34
E-0
18
.80
E-0
41
.40
E-0
11
.19
E-0
20
.58
70
49
96
5
2,2
,4-T
rim
eth
ylp
en
tan
e3
.81
E-0
10
.38
14
65
48
1
He
xan
e0
.02
58
70
34
11
.25
E-0
15
.50
E-0
20
.20
57
70
34
1
n-H
exa
ne
2.0
1E
-01
0.2
00
65
26
47
To
tal
HA
Ps
1.5
7E
-01
0.1
57
22
26
64
Xy
len
e1
.21
E-0
13
.07
E-0
46
.90
E-0
30
.12
80
49
93
3
Me
thy
len
e C
hlo
rid
e6
.63
E-0
26
.50
E-0
50
.06
63
47
96
6
PA
H6
.04
E-0
22
.22
E-0
40
.06
06
43
55
Eth
ylb
en
zen
e4
.87
E-0
21
.96
E-0
55
.30
E-0
30
.05
40
17
27
1
Na
ph
tha
len
e8
.76
71
7E
-06
4.3
4E
-02
7.6
5E
-05
0.0
43
50
74
47
Eth
yle
ne
Dib
rom
ide
3.3
1E
-02
1.6
8E
-05
0.0
33
11
32
05
1,1
,2,2
-Te
tra
chlo
roe
tha
ne
2.9
9E
-02
3.9
9E
-05
0.0
29
93
48
78
Ca
rbo
n T
etr
ach
lori
de
2.7
4E
-02
1.4
0E
-05
0.0
27
38
38
76
Sty
ren
e2
.47
E-0
29
.38
E-0
60
.02
47
18
96
5
1,1
,2-T
rich
loro
eth
an
e2
.38
E-0
21
.21
E-0
50
.02
37
74
74
5
Ch
loro
form
2.1
2E
-02
1.0
8E
-05
0.0
21
24
84
17
Ch
loro
be
nze
ne
2.0
0E
-02
1.0
2E
-05
0.0
20
03
03
43
1,3
-Dic
hlo
rop
rop
en
e1
.97
E-0
21
.00
E-0
50
.01
97
59
64
3
Ph
en
ol
1.9
0E
-02
0.0
18
98
30
93
Vin
yl
Ch
lori
de
1.1
1E
-02
5.6
6E
-06
0.0
11
14
30
09
2-M
eth
yln
ap
hth
ale
ne
3.4
49
38
E-0
79
.65
E-0
30
.00
96
49
70
8
Bip
he
ny
l1
.78
E-0
30
.00
17
81
07
4
Ph
en
an
ath
ren
e2
.44
33
1E
-07
1.5
9E
-03
0.0
01
59
19
38
Ace
na
ph
thy
len
e1
.29
35
2E
-08
1.4
3E
-03
0.0
01
42
93
81
1,3
-Bu
tad
ien
e1
.05
E-0
30
.00
10
45
29
8
Flu
ore
ne
4.0
24
28
E-0
87
.62
E-0
40
.00
07
62
06
9
Ace
na
ph
the
ne
1.2
93
52
E-0
86
.00
E-0
40
.00
05
99
71
6
An
thra
cen
e1
.72
46
9E
-08
3.2
4E
-04
0.0
00
32
37
67
Ch
ryse
ne
1.2
93
52
E-0
83
.03
E-0
40
.00
03
03
02
1
Py
ren
e7
.18
62
1E
-08
2.6
3E
-04
0.0
00
26
34
Flu
ora
nth
en
e4
.31
17
2E
-08
1.6
3E
-04
0.0
00
16
28
2
Be
nz(
a)a
nth
race
ne
1.2
93
52
E-0
81
.52
E-0
40
.00
01
51
51
7
Bu
tyr/
iso
bu
tyra
lde
hy
de
7.6
6E
-05
7.6
62
37
E-0
5
Nic
ke
l3
.01
82
1E
-05
3.0
18
21
E-0
5
Ch
rom
ium
2.0
12
14
E-0
52
.01
21
4E
-05
Dic
hlo
rob
en
zen
e1
.72
46
9E
-05
1.7
24
69
E-0
5
Ca
dm
ium
1.5
80
97
E-0
51
.58
09
7E
-05
tpy
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
10
of
13
3/2
/20
18
1,1
-Dic
hlo
roe
tha
ne
8.9
1E
-06
8.9
07
9E
-06
Be
nzo
(g,h
,i)p
ery
len
e8
.62
34
5E
-09
1.1
2E
-05
1.1
19
11
E-0
5
Be
nzo
(e)p
yre
ne
1.0
6E
-05
1.0
55
12
E-0
5
1,2
-Dic
hlo
rop
rop
an
e1
.02
E-0
51
.02
48
E-0
5
Ma
ng
an
ese
5.4
61
52
E-0
65
.46
15
2E
-06
Ind
en
o(1
,2,3
-c,d
)py
ren
e1
.29
35
2E
-08
4.4
8E
-06
4.4
90
42
E-0
6
Be
nzo
(b)f
luo
ran
the
ne
1.2
93
52
E-0
83
.84
E-0
63
.85
01
4E
-06
Me
rcu
ry3
.73
68
3E
-06
3.7
36
83
E-0
6
Ars
en
ic2
.87
44
8E
-06
2.8
74
48
E-0
6
Be
nzo
(a)p
yre
ne
8.6
23
45
E-0
92
.56
E-0
62
.56
97
6E
-06
Pe
ryle
ne
2.2
4E
-06
2.2
41
E-0
6
Be
nzo
(k)f
luo
ran
the
ne
1.2
93
52
E-0
81
.92
E-0
61
.93
37
9E
-06
Co
ba
lt1
.20
72
8E
-06
1.2
07
28
E-0
6
Se
len
ium
1.7
24
69
E-0
71
.72
46
9E
-07
7,1
2-D
ime
thy
lbe
nz(
a)a
nth
race
ne
1.1
49
79
E-0
71
.14
97
9E
-07
Be
ryll
ium
8.6
23
45
E-0
88
.62
34
5E
-08
3-M
eth
ylc
hlo
ran
thre
ne
1.2
93
52
E-0
81
.29
35
2E
-08
Dib
en
zo(a
,h)a
nth
race
ne
8.6
23
45
E-0
98
.62
34
5E
-09
Su
m o
f O
the
r H
AP
s0
.03
1.6
00
.00
0.2
60
.16
0.0
82
.13
Su
m o
f A
ll H
AP
s 0
.03
29
.39
0.0
51
.07
0.1
64
.21
34
.92
So
urc
e I
D03
110
1 &
10
210
31
05
11
2 &
11
31
10
, 1
11
, &
P0
1
Em
issi
on
Pro
cess
Bo
ile
r1
Co
mpr
ess
or
Eng
ines
2
Em
erge
ncy
Gen
erat
or
Eng
ine3
Gly
col
De
hy
dra
tio
n
Sy
ste
m4
4 N
G
Co
mp
ress
ors
5
Sto
rag
e T
an
k,
Pa
rts
Wa
she
rs,
Pip
ing
6,
7,
8
HA
P
Fo
rma
lde
hy
de
0.0
01
8.7
90
.03
0.0
00
.00
0.0
01
8.8
2
GLY
ET
0.0
00
.00
0.0
00
.00
0.0
04
.13
4.1
3
Acr
ole
in0
.00
3.5
10
.00
0.0
00
.00
0.0
03
.51
Ace
tald
eh
yd
e0
.00
3.5
00
.00
0.0
00
.00
0.0
03
.50
Be
nze
ne
0.0
00
.87
0.0
00
.81
0.0
00
.00
1.6
9
Me
tha
no
l0
.00
1.1
20
.00
0.0
00
.00
0.0
01
.12
Su
m o
f A
ll O
the
r H
AP
S0
.03
1.6
00
.00
0.2
60
.16
0.0
82
.13
Su
m o
f A
ll H
AP
s0
.03
29
.39
0.0
51
.07
0.1
64
.21
34
.92
Va
lue
s re
po
rte
d i
n t
his
ta
ble
we
re r
ou
nd
ed
fro
m c
alc
ula
tio
ns
pe
rfo
rme
d e
lse
wh
ere
.
III.
Gre
en
ho
use
Ga
s E
mis
sio
ns
GH
Gs
fro
m t
he
Co
mp
ress
or
En
gin
es
(So
urc
e I
Ds
10
1 &
10
2)
2E
xce
pt
for
form
ald
eh
yd
e f
rom
th
e c
om
pre
sso
r e
ng
ine
, e
mis
sio
ns
are
ba
sed
on
AP
-42
, T
ab
le 3
.2-1
(2
SLB
).
Fo
rma
lde
hy
de
em
issi
on
s fr
om
th
e
Co
mp
ress
ors
are
ba
sed
on
Ma
rch
13
, 2
01
3 t
est
ing
.
8E
mis
sio
ns
for
2 p
art
s w
ash
ers
, to
ge
the
r, w
ere
ass
um
ed
to
be
th
e s
am
e a
s th
e s
ing
le p
art
s w
ash
er
at
JB T
on
kin
.
7T
he
va
lue
fo
r fa
cili
ty f
ug
itiv
e e
mis
sio
ns
wa
s re
po
rte
d i
n t
he
19
95
ap
pli
cati
on
fo
r a
n i
nit
ial
TV
OP
.
To
ns
pe
r Y
ea
r
Tab
le 3
: P
oten
tial
Haz
ardo
us A
ir P
ollu
tant
Em
issi
ons
All
em
issi
on
so
urc
es,
exc
ep
t th
e e
me
rge
ncy
ge
ne
rato
r, a
t th
e f
aci
lity
op
era
te 8
,76
0 h
ou
rs p
er
ye
ar.
T
he
em
erg
en
cy g
en
era
tor,
wh
ich
wa
s is
ass
um
ed
to
op
era
te 5
00
ho
urs
pe
r y
ea
r, p
rio
r to
iss
ua
nce
of
this
pro
po
sed
TV
OP
, w
ill
be
lim
ite
d t
o a
ma
xim
um
le
ss t
ha
n 5
00
hr/
yr,
wh
en
th
e p
erm
it i
s is
sue
d.
3E
mis
sio
ns
are
ba
sed
on
AP
-42
, T
ab
le 3
.2-3
(4
SR
B).
5B
low
-by
em
issi
on
s fr
om
th
e c
om
pre
sso
r a
re b
ase
d o
n 2
3 (
11
.5*
2)
scfh
/pis
ton
ro
d (
EP
A E
ne
rgy
Sta
r),
4 p
isto
n r
od
s, a
nd
NG
an
aly
sis
sup
pli
ed
by
th
e c
om
pa
ny
, in
its
20
15
an
nu
al
rep
ort
.
1E
mis
sio
ns
fro
m t
he
bo
ile
r a
re b
ase
d o
n A
P-4
2.
Ta
ble
1.4
-2.
6E
mis
sio
ns
we
re r
ep
ort
ed
by
th
e c
om
pa
ny
.
4E
mis
sio
ns
are
pe
ak
an
nu
al
em
issi
on
s re
po
rte
d b
y D
om
inio
n f
or
So
uth
Oa
kfo
rd o
ve
r 2
01
2 -
20
16.
Dom
inio
n T
rans
mis
sion
, Inc
- S
outh
Oak
ford
Com
pres
sion
Sta
tion
(T
VO
P-6
5-00
840)
Fa
cili
ty
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
11
of
13
3/2
/20
18
AP
-42
Un
con
tro
lle
d
Em
issi
on
Fa
cto
r
(Un
con
tro
lle
d E
Fs
fro
m A
P-4
2,
Ta
ble
3.2
-1
lb/M
MB
tu
CO
21
10
.00
Me
tha
ne
1.4
5
GH
Gs
fro
m t
he
Em
erg
en
cy E
ng
ine
(S
ou
rce
ID
s 1
03
) AP
-42
Un
con
tro
lle
d
Em
issi
on
Fa
cto
r
(Un
con
tro
lle
d E
Fs
fro
m A
P-4
2,
Ta
ble
3.2
-3
lb/M
MB
tu
CO
21
10
.00
Me
tha
ne
0.2
3
GH
Gs
fro
m t
he
Bo
ile
r (S
ou
rce
ID
03
1)
lb/1
0^
6 s
cfA
P-4
2,
Ta
ble
1.4
-2
CO
21
20
00
0
Nit
rou
s O
xid
e2
.2
Me
tha
ne
2.3
GH
Gs
fro
m e
ach
Co
mp
ress
or
(2 e
ach
, S
ou
rce
ID
s 1
12
& 1
13
)
lbm
/hr
TP
Y
CO
20
.09
70
81
24
20
.42
52
15
8
Me
tha
ne
7.1
11
40
49
51
31
.14
79
54
Glo
ba
l W
arm
ing
Po
ten
tia
ls (
10
0 y
ea
r h
ori
zon
) T
ab
le A
-1 t
o P
art
A o
f P
art
98
(V
alu
es
eff
ect
ive
on
Ja
nu
ary
1,
20
14
.)
GH
GC
AS
No
GW
P
CO
21
24
-38
-91
N2O
10
02
4-9
7-2
29
8
CH
47
4-8
2-8
25
IDS
ou
rce
Na
me
Lb/H
rT
on
/Yr
Lb/
Hr
To
n/
Yr
Lb/
Hr
To
n/
Yr
Lb/
Hr
To
n/
Yr
31
Aja
x B
oil
er
12
39
41
,72
50
.00
75
0.0
33
0.0
07
20
.03
23
96
1,7
35
10
1C
oo
pe
r E
ng
ine
13
5,6
62
24
,80
07
53
27
0.0
00
.00
7,5
28
32
,97
2
10
2C
oo
pe
r E
ng
ine
23
5,6
62
24
,80
07
53
27
0.0
00
.00
7,5
28
32
,97
2
10
3W
au
ke
sha
Au
x. E
me
rge
ncy
Ge
ne
rato
r E
ng
ine
13
69
41
73
1.5
0.3
60
.00
0.0
07
30
18
2
10
5G
lyco
l D
eh
yd
rati
on
Sy
ste
m1
36
59
60
.00
23
0.0
10
00
.00
0.0
01
36
59
6
11
0S
tora
ge
Ta
nk
P-1
0.0
00
.00
0.0
00
.00
0.0
00
.00
00
11
12
Pa
rts
Wa
she
rs0
.00
0.0
00
.00
0.0
00
.00
0.0
00
0
11
22
NG
Co
mp
ress
ors
#1
an
d #
24
0.1
94
11
4.2
62
0.0
00
.00
35
61
,55
8
11
32
Co
op
er,
NG
Co
mp
ress
ors
#3
an
d #
44
0.1
94
11
4.2
62
0.0
00
.00
35
61
,55
8
P0
1F
aci
lity
Pu
mp
s, V
alv
es,
Fla
ng
es,
etc
.50
.00
02
37
1,0
38
0.0
00
.00
5,9
23
25
,94
3
Fa
cili
ty T
ota
l1
2,5
48
52
,09
54
16
1,8
17
0.0
07
20
.03
22
2,9
53
97
,51
8
2E
mis
sio
ns
fro
m t
he
bo
ile
r a
re b
ase
d o
n A
P-4
2,
Ta
ble
1.4
-2.
1E
mis
sio
n e
stim
ate
s o
f C
O2e
are
ba
sed
on
AP
-42
, T
ab
le 3
.2-2
an
d 1
00
ye
ar
ho
rizo
n G
lob
al
Wa
rmin
g P
ote
nti
als
(1
to
n C
H 4 =
25
to
n C
O2 a
nd
1 t
on
N2O
= 2
98
to
n C
O2)
in T
ab
le A
-1
to P
art
A o
f P
art
98
. (V
alu
es
eff
ect
ive
Ja
nu
ary
1,
20
14
.)
Do
min
ion
Tra
nsm
issi
on
, In
c -
So
uth
Oa
kfo
rd C
om
pre
ssio
n S
tati
on
(T
VO
P-6
5-0
08
40
)
CO
2C
H4
N2O
To
tal
CO
2e
1
Gre
en
ho
use
Ga
s
All
em
issi
on
so
urc
es,
exc
ep
t th
e e
me
rge
ncy
ge
ne
rato
r, a
t th
e f
aci
lity
op
era
te 8
,76
0 h
ou
rs p
er
ye
ar.
T
he
em
erg
en
cy g
en
era
tor,
wh
ich
wa
s is
ass
um
ed
to
op
era
te
50
0 h
ou
rs p
er
ye
ar,
pri
or
to i
ssu
an
ce o
f th
is p
rop
ose
d T
VO
P,
wil
l b
e l
imit
ed
to
a m
axi
mu
m l
ess
th
an
50
0 h
r/y
r, w
he
n t
he
pe
rmit
is
issu
ed
.
Ta
ble
4:
Po
ten
tia
l G
ree
nh
ou
se G
as
Em
issi
on
s
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
12
of
13
3/2
/20
18
3E
mis
sio
ns
fro
m t
he
en
gin
es
are
ba
sed
on
AP
-42
, T
ab
le 3
.2-1
& T
ab
le 3
.2-3
.
5M
eth
an
e e
mis
sio
ns
fro
m P
01
are
ba
sed
on
CH
4 e
mis
sio
ns
fro
m t
he
na
tura
l g
as
com
pre
sso
rs a
nd
th
e r
ati
o o
f V
OC
fro
m t
he
tw
o s
ou
rce
s.
Va
lue
s re
po
rte
d i
n t
his
ta
ble
we
re r
ou
nd
ed
fro
m c
alc
ula
tio
ns
pe
rfo
rme
d e
lse
wh
ere
.
To
tal
faci
lity
em
issi
on
s a
re a
co
mb
ina
tio
n o
f re
gu
late
d p
ote
nti
al
em
issi
on
s a
nd
est
ima
ted
em
issi
on
s.
IV.
Ch
an
ge
in
Em
issi
on
s S
ince
th
e T
VO
P w
as
last
Re
ne
we
d
PM
2.5
PM
10
NO
xC
OV
OC
HA
Ps
CO
2e
Da
te
10
/31
/20
07
Po
ten
tia
l E
mis
sio
ns
at
Last
Re
ne
wa
l2
1.9
6
2
1.9
6
1
,18
8.1
5
4
98
.10
2
67
.24
3
4.9
29
7,5
18
1/1
/20
17
Ad
dit
ion
of
Op
era
tin
g T
ime
Lim
it o
n t
he
Au
x. G
en
era
tor1
0.0
00
.00
-77
.88
0.0
00
.00
0.0
00
11
/7/2
01
7
Ad
dit
ion
of
Cle
an
Bu
rn
Te
chn
olo
gy
on
th
e C
om
pre
sso
r
En
gin
es
an
d i
mp
osi
tio
n o
f R
AC
T
II e
mis
sio
n l
imit
s1
0.0
00
.00
-73
5.7
0-3
92
.34
-12
2.5
70
.00
0
To
tal
Ch
an
ge
ov
er
Pe
rio
d0
.00
0.0
0-8
13
.59
-39
2.3
4-1
22
.57
0.0
00
Da
te o
f
Cu
rre
nt
Re
ne
wa
l
Cu
rre
nt
Po
ten
tia
l E
mis
sio
ns
21
.96
21
.96
37
4.5
6
1
05
.76
1
44
.68
3
4.9
29
7,5
18
1B
oth
ch
an
ge
s w
ere
ma
de
to
co
mp
ly w
ith
th
e r
eq
uir
em
en
ts o
f R
AC
T I
I.
To
ns
pe
r Y
ea
r
Do
min
ion
Tra
nsm
issi
on
, In
c -
So
uth
Oa
kfo
rd C
om
pre
ssio
n S
tati
on
(T
VO
P-6
5-0
08
40
)
Ta
ble
5:
Ch
an
ge
in
Em
issi
on
s S
ince
th
e T
VO
P w
as
last
Re
ne
we
d
4B
low
-by
em
issi
on
s fr
om
th
e c
om
pre
sso
r a
re b
ase
d o
n 2
3 (
11
.5*
2)
scfh
/pis
ton
ro
d (
EP
A E
ne
rgy
Sta
r),
8 p
isto
n r
od
s, a
nd
NG
an
aly
sis
sup
pli
ed
by
th
e c
om
pa
ny
, in
its
20
15
an
nu
al
rep
ort
.
Do
min
ion
-So
uth
Oa
kfo
rd (
TV
OP
-65
-00
84
0)
em
issi
on
ca
lcs
Pa
ge
13
of
13
3/2
/20
18
