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HomeMy WebLinkAboutFINAL_HOR_Attachment_Fcont'd-Northampton_Compressor_Station4.0 4.1 FEDERAL REGULATORY REQUIREMENTS NEW SOURCE PERFORMANCE STANDARDS (NSPS) NSPS have been established by the EPA to limit air pollutant emissions from certain categories of new and modified stationary sources. The NSPS regulations are contained in 40 CFR Part 60 and cover many different source categories, and applicable categories are described below. 4.1.1 40 CFR 60 Subpart De -Standards of Perfonnance for Small Industrial­ Commercial-Institutional Steam Generating Units Subpart De applies to steam generating units for which construction, modification, or reconstruction is commenced after June 9, 1989 and that have a maximum design heat capacity of 100 MMBtu/hr or less, but greater than or equal to 10 MMBtu/hr. The new boiler will have a heat input capacity of 6.3 MMBtu/hr and thus is not subject to this regulation. 4.1.2 40 CFR 60 Subpart Kb -Standards of Perfonnance for Volatile Organic Liquid Storage Vessels This regulation applies to volatile organic liquid storage vessels with storage capacities greater than or equal to 75 cubic meters (19,812 gallons) for which construction, reconstruction, or modification commenced after July 23, 1984. There are no petroleum storage vessels with capacities greater than 19,812 gallons planned at the Northampton Compressor Station, and this regulation is therefore not applicable to the facility. 4.1.3 40 CFR 60 Subpart JJJJ -Standards of Perfonnance for StationanJ Spark Ign,ition Internal Combustion Engines NSPS Subpart JID was promulgated on Jan 8, 2008 and is applicable to new stationary spark ignition internal combustion engines depending upon model year and size category. The new emergency generator is subject to the NOx, CO and VOC requirements of this subpart and will comply with the emission standards under this subpart. 4.1.4 40 CFR 60 Subpart KKKK -Standards of Perfonnance for Stationary Combustion Turbines NSPS 40 CFR Part 60 Subpart KKKK regulates stationary combustion turbines with a heat input rating of 10 MMBtu/hr or greater that commence construction, modification, or reconstruction after February 18, 2005. Subpart KKKK limits emissions of NOx as well as the sulfur content of fuel that is combusted from subject units. ERM 16 ACP, LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-58 Attachment F. Air Quality Permit Application Review Documents • 4.1.5 The proposed Solar combustion turbines will be subject to the requirements of this subpart. Subpart KKKK specifies several subcategories of turbines, each with different NOx emissions limitations. The proposed turbines fall within the "medium sized"(> 50MMBtu/hr, < 850 MMBtu/hr) category for natural gas turbines. "Medium sized" turbines must meet a NOx limitation of 25 parts per million by volume (ppmv) at 15 percent oxygen (02), and "small sized, mechanical drive" turbines must meet a NOx limitation of 100 ppmv at 15 percent 02 under the requirements of Subpart KKKK and units must minimize emissions consistent with good air pollution control practices during startup, shutdown and malfunction. Solar provides an emissions guarantee of 9 parts per million volume dry (ppmvd) NOx at 15 percent 02 for the proposed SoLoNOx equipped units. These guarantees apply at all times except during periods of start-up and shutdown and periods with ambient temperatures below 0°F. In addition, SCR will be installed to lower emissions for all turbines to further reduce NOx emissions to 5 ppmvd at 15 % 02, except during periods of start-up and shutdown and periods with ambient temperatures below 0°F. ACP, LLC plans to conduct stack tests for NOx emissions to demonstrate compliance with the Subpart KKKK emissions limits . The NSPS Subpart KKKK emission standard for SO2 is the same for all turbines, regardless of size and fuel type. All new turbines are required to meet an emission limit of 110 nanogram per joule (ng/J) (0.90 pounds [lbs]/megawatt­ hr) or a sulfur limit for the fuel combusted of 0.06 lbs/MMBtu. The utilization of natural gas as fuel ensures compliance with the SO2 standard due to the low sulfur content of natural gas. 40 CFR 60 Subparts 0000 and 0000a -Standards of Performance for Crude Oil and Natural Gas Production, Transmission and Distribution Subpart 0000 currently applies to affected facilities that commenced construction, reconstruction, or modification after August 23, 2011. Subpart 0000 establishes emissions standards and compliance schedules for the control of VOCs and SO2 emissions for affected facilities producing, transmitting, or distributing natural gas. Compressors located between the wellhead and the point of custody transfer to the natural gas transmission and storage segment are subject to this Subpart. Custody transfer is defined as the transfer of natural gas after processing and/ or treatment in the producing operations. The station is located after the point of custody transfer, and therefore centrifugal compressors driven by the proposed turbines are not currently subject to this regulation. Storage vessels located in the natural gas transmission and storage segment that have the potential for VOC emissions equal to or greater than 6 tpy are also subject to this Subpart. All storage vessels will emit less than this threshold, and thus will not be subject to this regulation. ERM 17 ACP, LLC -NORTHAMPTON COMPRESSOR Sf A TION Page F-59 Attachment F. Air Quality Permit Application Review Documents 4.2 On August 18, 2015, EPA proposed amendments to 40 CFR 60, Subpart 0000 and proposed an entirely new Subpart 0000a. If finalized, revisions proposed for Subpart 0000 would apply to oil and natural gas production, transmission, and distribution affected facilities that were constructed, reconstructed, and modified between August 23, 2011 and the Federal Register publication date (anticipated September 2015). Conversely, if finalized, Subpart 0000a will apply to oil and natural gas production, transmission, and distribution affected facilities that are constructed, reconstructed, and modified after the Federal Register date. The proposed NSPS Subpart 0000a would establish standards for both voe and methane. Based on the expected date of publication in the Federal Register, it is anticipated this project will be required to comply with the requirements of NSPS Subpart 0000a. There is uncertainty if Subpart 0000a will become final or what the final requirements will specifically include; however, the proposal contains provisions that would affect additional sources at the proposed facilities beyond Subpart 0000. While storage tanks remain covered, Subpart 0000a also includes provisions intended to reduce emissions from centrifugal compressors and equipment leaks from transmission and storage facilities. For centrifugal compressors, Subpart 0000a proposes the use of dry seals or the control of emissions if wet seals are used. Dry seals are already planned for use in all proposed compressors. For equipment leaks, Subpart 0000a proposes requiring periodic surveys using optical gas imaging (OGI) technology and subsequent repair of any identified leaks. The project will comply with all applicable leak detection provisions of proposed Subpart 0000a. NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS (NESHAP) NESHAP regulations established in 40 CFR Part 61 and Part 63 regulate emission of air toxics. NFSHAP standards primarily apply to major sources of Hazardous Air Pollutants (HAPs), though some Subparts of Part 63 have been revised to include area (non-major) sources. The NESHAP regulations under 40 CFR Part 61 establish emission standards on the pollutant basis whereas 40 CFR Part 63 establishes the standards on a source category basis. The Northampton Compressor Station will not emit any single HAP in excess of 10 tpy and will not emit combined HAPS in excess of 25 tpy, and will therefore be designated as an area source of HAPs. ERM 18 ACP, LLC-NORTHAMPTON COMPRESSOR STA TJON Page F-60 Attachment F. Air Quality Permit Application Review Documents 4.2.1 40 CFR 63 Subpart HRH -National Emissions Standards for Hazardous Air Pollutants from Natural Gas Transmission and Storage Facilities This regulation applies to certain affected facilities at major HAP sources. The Station will be an area HAP source. Therefore, this regulation is not applicable. 4.2.2 40 CFR 63 Subpart DDDDD -National Emission Standards for Hazardous Air Pollutants for Major Sources: Industrial, Commercial, and Institutional Boilers And Process Heaters Industrial, commercial, or institutional boilers or process heaters located at a major source of HAPs are subject to this Subpart. The Northampton Compressor Station will not be a major source of HAPs, and therefore will not be subject to this Subpart. 4.2.3 40 CFR 63 Subpart Jlllll -National Emission Standards for Hazardous Air Pollutants for Industrial, Commercial, and Institutional Boilers Area Sources This Subpart applies to area sources of HAPs. The Northampton Compressor Station will be an area source of HAPs; however, gas-fired boilers as defined by this Subpart are not subject to any requirements under this rule. As such, this subpart does not apply. 4.2.4 40 CFR 63 Subpart YYYY -National Emissions Standards for Hazardous Air Pollutants for Stationary Combustion Turbines Stationary combustion turbines located at major sources of HAP emissions are subject to this Subpart. The Northampton Compressor Station will be an area HAP source. Therefore, this regulation is not applicable. 4.2.5 40 CFR 63 Subpart ZZZZ -National Emissions Standards for Hazardous Air Pollutants for Stationary Reciprocating Internal Combustion Engines The emergency generator is subject to the NESHAP requirements under 40 CFR Part 63 Subpart ZZZZ (and applies to both major and area sources of HAPs). However, the NESHAP refers to the NSPS for all applicable requirements. Therefore, compliance with the NSPS requirements ensures compliance with the NESHAP requirements. 4.3 PREVENTION OF SIGNIFICANT DETERIORATION (PSD) AND NON­ ATTAINMENT NEW SOURCE REVIEW The NC DENR State Regulations address federal regulations where the state of North Carolina has been delegated enforcement authority, including Prevention of Significant Deterioration (PSD) permitting (15A NCAC 02D.0530). ERM 19 ACP, LLC -NORTHAMPTON COMPRESSOR Sf A TION Page F-61 Attachment F. Air Quality Permit Application Review Documents 4.4 4.5 • 4.6 The Northampton Compressor Station will be located in Northampton County. The air quality of Northampton County is designated by the U.S. EPA as either "better than normal standards" or "unclassified/ attainment" for all criteria pollutants ( 40 CFR 81.318). As such, new construction or modifications that result in emission increases are potentially subject to the PSD permitting regulation s. PSD applicability depends on the existing status of a facility (i.e. major or minor source) and the net emissions increase associated with the project. The major source threshold for PSD applicability for a facility is 250 tons per year (tpy) of each regulated pollutant unless the source is included on a list of 28 specifically defined industrial source categories for which the PSD "major" source threshold is 100 tpy. Since the Northampton Compressor Station is not one of the 28 listed sources, the PSD major source threshold is 250 tpy of any pol lutant regulated by the Clean Air Act (CAA). Potential emissions of each criteria pollutant from the proposed facility will not exceed 250 tpy, as shown in Section 3. Therefore, the facility and project are not subject to PSD review. TITLE V OPERATING PERMIT See Section 5.0 for Title V applicability information. MAINTENANCE EMISSIONS AND FEDERAL ROUTINE MAINTENANCE, REPAIR AND REPLACEMENT PROVISIONS (RMRR) As part of normal operations of the Northampton Compressor Station, ACP, LLC will routinely conduct activities associated with maintenance and repair of the facility equipment. These maintenance and repair activities will include, but will not be limited to, compressor engine startup/ shutdowns, calibrating equipment, changing orifice plates, dead weight testing, emergency power generator run times, changing equipment filters (e.g., oil filters, separator filters), and use of portable gas/ diesel engines for air compressors and lube guns. Furthermore, in order to ensure the reliability of natural gas deliveries to their customers, ACP, LLC may conduct equipment and component replacement activities that conform to the currently applicable federal laws and regulations. CHEMICAL ACCIDENT PREVENTION AND RISK MANAGEMENT PROGRAMS (RMP) The Northampton Compressor Station will not be subject to the Chemical Accident Prevention Provisions (40 CFR 68.1), as no chemicals subject to regulation under this Subpart will be present onsite. The aqueous ammonia stored in TK-3 will have a concentration of less than 20%. ERM 20 ACP, LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-62 Attachment F. Air Quality Permit Application Review Documents • 4.7 ACID RAIN REGULATIONS 4.8 4.9 The Northampton Compressor Station will not sell electricity and is a non-utility facility. Therefore, the facility will not be subject to the federal acid rain regulations found at 40 CFR Parts 72 through 77. STRATOSPHERIC OZONE PROTECTION REGULATIONS Subpart F, Recycling and Emissions Reductions, of 40 CFR Part 82, Protection of Stratospheric Ozone, generally requires that all repairs, service, and disposal of appliances containing Class I or Class II ozone depleting substances be conducted by properly certified technicians. The facility will comply with this regulation as applicable. GREENHOUSE GAS REPORTING On November 8, 2010, the USEPA finalized GHG reporting requirements under 40 CFR Part 98. Subpart W of 40 CFR Part 98 requires petroleum and natural gas facilities with actual annual GHG emissions equal to or greater than 25,000 metric tons CO2e to report GHG from various processes within the facility. Following this project, is expected that the station will be subject to GHG emissions reporting. If the emissions threshold is met or exceeded, ACP, LLC will comply with the applicable GHG reporting requirements. ERM 21 ACP, LLC-NORTHAMPTON COMPRESSOR STATION Page F-63 Attachment F. Air Quality Permit Application Review Documents 5.0 • STATE REGULATORY APPLICABILITY This section outlines the NC State air quality regulations that could be reasonably expected to apply to the Northampton Compressor Station, and presents an applicability determination for each of these regulations based on activities planned at the Station and the emissions of regulated air pollutants associated with this project. This review is presented to supplement and/ or add clarification to the information provided in the NC DENR permit application forms. The NC DENR State Regulations address federal regulations where the state of North Carolina has been delegated enforcement authority, including Prevention of Significant Deterioration (PSD) permitting, Title V permitting, New Source Performance Standards (NSPS), and National Emission Standards for Hazardous Air Pollutants (NESHAP). The regulatory requirements in reference to the Northampton Compressor Station are described in Table 5.1 below . ERM 22 ACP, LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-64 Attachment F. Air Quality Permit Application Review Documents • TABLES.1 STATE REGULATORY APPLICABILITY Regulatory Citation Construction and Operation Permits (15A NCAC 02Q.0300) Sulfur Dioxide Emissions from Combustion Sources (15A NCAC 02D.0516) Control of Nitrogen Dioxide and Nitrogen Oxides Emissions (15A NCAC 02D.0519) Control of Visible Emissions (15A NCAC 02D.0521) Prevention of Significant Deterioration (15A NCAC 02D.0530) Excess Emissions Reporting and Malfunctions (15A NCAC 02D.0535) ERM Applicable Requirement Requires sources to obtain air permits via the guidelines and rules established in 02Q.0300 prior to construction. Limits SO2 from any source of combustion that is discharged to the atmosphere to no more than 2.3 pounds of SO2 per MMBtu input. Limits NO, emissions from sulfuric acid plants and boilers with a capacity of 250 MMBtu/hour or more combusting oil, gas, coal, or a combination of these fuels. Limits opacity emissions from fuel burning operations and industrial processes, including testing of emergency generators. For sources manufactured after July 1, 1971, visible emissions shall not be more than 20 percent opacity when averaged over a six-minute period. In addition, if a source is subject to an NSPS or NESHAP opacity emission standard, the source shall comply with the NSPS or NESHAP opacity emission standard rather than this Rule. Establishes Prevention of Significant Deterioration regulations. Establishes State-specific requirements, definitions, and reporting requirements for equipment and emission control device excess emissions. 23 Compliance Approach The enclosed permit application for a combined construction and operating permit satisfies the requirements of this regulation for the proposed Northampton Compressor Station. The use of pipeline quality natural gas as fuel for all of the facility's fuel combustion sources constitutes compliance with this rule. In addition, if a source is subject to an NSPS or NESHAP SO2 emission standard, the source shall comply with the NSPS or NESHAP SO2 emission standard rather than this Rule. The new boiler will have a maximum heat input capacity of 6.3 MMBtu/hr, and thus is not subject to this regulation. All sources will comply with the provisions of this rule by the combustion of pipeline quality natural gas. The facility and project are not subject to PSD review. See Section 4 for the PSD regulatory evaluation for Northampton Compressor Station. The Northampton Compressor Station will comply with these requirements as applicable. In addition, sources subject to an NSPS or NESHAP rule are not subject to this regulation, unless excess emissions exceed an emission limit established in a permit limit issued under 15A NCAC 02Q.0700 that is more stringent than the applicable NSPS or NESHAP rule. ACP. LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-65 Attachment F. Air Quality Permit Application Review Documents • Regulatory Citation Particulates from Fugitive Dust Emission Sources (15A NCAC 02D.0540) Monitoring, Recordkeeping, and Reporting 15A NCAC 02D.0600 Volatile Organic Compounds (15A NCAC 02D.0900) Control of Toxic Air Pollutants (15A NCAC 02D.1100 and 02Q.0700) Nitrogen Oxides (15A NCAC 020.1400) ERM Applicable Requirement Facilities required to obtain a permit under 15A NCAC 02Q or subject to requirements under 15A NCAC 02D shall not cause or allow fugitive dust emissions to cause or contribute to substantive complaints. This regulation sets forth general monitoring, recordkeeping, and reporting requirements applicable to sources subject to the requirements of 15A NCAC 02D or 15A NCAC 02Q. This regulation sets forth work practice requirements for sources (e.g., solvents) emitting voes. This regulation requires facilities emitting toxic air pollutants greater than designated thresholds to obtain air toxics permits. This regulation sets forth various requirements for sources emitting NOx. 24 Compliance Approach The Northampton Compressor Station will comply with all applicable requirements, including reporting requirements in the event of substantive fugitive dust complaints. The Northampton Compressor Station will comply with all applicable requirements in this regulation. The Northampton Compressor Station is not expected to emit greater than 15 pounds voe per day, and is therefore only potentially subject to sections .0925 and .0958 of this regulation. However, all storage tanks at the facility will have a capacity less than 39,000 gallons, and the facility is therefore not subject to section .0925. The facility will comply with all applicable requirements of section .0958 . The Northampton Compressor Station 's natural gas fired combustion sources will have an aggregate allowable heat input value less than 450 MMBtu/hour and will be the only sources of benzene at the facility. As such, no air dispersion modeling has been included with this permit application and a permit to emit toxic air pollutants will not be required (15 NCAC 02Q.0702). 15A NCAC 02D.1408 applies to stationary combustion turbines located at major sources of NO, emissions located in certain counties. As Northampton County is excluded from this list, the proposed turbines are not subject to these requirements. 15A NCAC 02D.1409 and .1423 apply to internal combustion engines (ICE), which are defined as "reciprocating ICE". As the turbines do not meet this definition, these requirements do not apply. Emergency generators are not subject to this rule (15A NCAC 02D.1402(h)(3)). The boiler is exempt from air permitting requirements, and is therefore also exempt from these requirements (15A NCAC 02D.1402(h)(l)). ACP, LLC -NORTHAMPTON COMPRESSOR Sf A T!ON Page F-66 Attachment F. Air Quality Permit Application Review Documents Regulatory Citation Title V Procedures (15A NCAC 02Q.0500) ERM Applicable Requirement This regulation outlines the NC DENR Title V Permitting Program. 25 Compliance Approach The Northampton Compressor Station's criteria pollutant PTE will not exceed the applicable Title V major source threshold of 100 tpy per criteria pollutant. In addition, the facility's HAP PTE will not exceed 10 tpy per individual HAP, and will not exceed 25 tpy for combined HAPs. Therefore, the Northampton Compressor Station will be a minor source of emissions with respect to the Title V Operating Program. ACP, LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-67 Attachment F. Air Quality Permit Application Review Documents 6.0 PROPOSED COMPLIANCE DEMONSTRATIONS The following methods are proposed for demonstrating ongoing compliance for the sources described in this application: Compressor Turbines (CT-01 through CT-03) NOx Annual stack testing (or semi-annual testing as allowed) will be completed to demonstrate compliance with the NSPS Subpart KKKK emissions limits (NO2 emissions). Compliance with the combustion turbines potential to emit will be demonstrated on a 12-month rolling total basis by the sum of the following emissions: •Normal Operation: The average emission rate from the most recent stack test (lb/hour) times the number of hours operating in SoLoNOx mode (mode indication provided and recorded by control logic on turbine). •Low Temperature(< 0° F) Operation: The proposed controlled emission rates (lb/hr, see Table 3.2) determined using the Solar provided emissions factor multiplied by the control efficiency of the SCR times the number of hours when inlet combustion air for turbine was measured to be below 0 degrees F. •Startup and Shutdown Emissions(< 50% load): The Solar-provided emission rates (see Tables 3.3 and 3.4) divided by Solar-assumed duration for startups and shutdowns (1/ 6 of an hour each) times the number of hours operating in non-SoLoNOx mode (mode indication provided and recorded by control logic on the turbine). CO, VOC, PM10/PM2.s: Initial stack testing will be completed to determine PM10/PM2.s emission rates (lb/MMBtu). Fuel firing will be tracked and used to calculate annual (rolling 12- month total) ton per year emissions. Initial stack testing will be competed to determine VOC and CO emission rates. Compliance with the combustion turbines potential to emit will be demonstrated on a 12-month rolling total basis by the sum of the following emissions: ERM 26 ACP, LLC -NORTHAMPTON COMPRESSOR ST A TION Page F-68 Attachment F. Air Quality Permit Application Review Documents •Normal Operation: The average emission rate from the most recent stack test (lb/hour) times the number of hours operating in SoLoNOx mode (mode indication provided and recorded by control logic on turbine). •Low Temperature(< 0° F) Operation: The proposed controlled emission rates (lb/hr, see Table 3.2) determined using the Solar provided emissions factor multiplied by the control efficiency of the oxidation catalyst times the number of hours when inlet combustion air for turbine was measured to be below O degrees F. •Startup and Shutdown Emissions(< 50% load): The Solar-provided emission rates (see Tables 3.3 and 3.4) divided by Solar-assumed duration for startups and shutdowns (1/ 6 of an hour each) times the number of hours operating in non-SoLoNOx mode (mode indication provided and recorded by control logic on the turbine). GHG: Total annual fuel volume will be tracked to determine total MMBtu of firing. This value times the EPA Mandatory Reporting Rule natural gas emission factor (40 CFR Part 98 Subpart C) times the Global Warming Potential (40 CFR Part 98 Subpart A) will be used to calculate ton per year CO2e emissions. Emergency Generator Records of the monthly emergency and non-emergency use will be maintained to confirm compliance with the annual limit for non-emergency operation. If a non-certified engine is installed or if a certified engine is installed but operated as non-certified an initial stack test and testing every 8760 operating hours or three years (whichever comes first) will be conducted. Other Combustion Sources If not otherwise specified above, the amount of fuel fired in units and/ or hours of operation will be tracked and multiplied by the appropriate emission factor to calculate emissions on an annual basis. ERM 27 ACP, LLC -NORTHAMPTON COMPRESSOR STATION Page F-69 Attachment F. Air Quality Permit Application Review Documents APPENDICES • • ERM ACP, LLC-ACMSfATION Page F-70 Attachment F. Air Quality Permit Application Review Documents • APPENDIX A NC DENR PERMIT APPLICATION FORMS • ERM ACP, I.LC-ACP-3STATION Page F-71 Attachment F. Air Quality Permit Application Review Documents FORM A1 FACILITY (General Information) aSED 05/25/12 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I A1 -NOTE-APPLICATION WILL NOT l;lE PROCESSED WITHOUT THE FOI.JLOWING: 0 Local Zoning Consistency Determination (if required) Oacility Reduction & Recycling Survey Form (Form A4) l:!Jl!lpplication Fee 0 Responsible Official/Authorized Contact Signature 8,propriate Number of Copies of Applicatio1-� .. SJ�(i!.!:!tqu�) --·--GENE� INli�ll�IC:>N '�- Legal Corporate/Owner Name: Atlantic Coast Pipeline, LLC t:\ ;\ J Site Name: Norhampton Compressor Station mi = Site Address (911 Address) Line 1: l�\d Site Address Line 2: City: Pleasant Hill State: North Carolina - c\ e• ,"J I 7 '11 . -- � ,: I ti I 1 <.::.'�I I � Zip Code: County: Northampton I.II" l"\C:I\ID O,:,loi�I-. p,,,,,;,.. ...... 1 r'lm---CONTACT INFORMATION . -..- Permlt/Technlcal Contact: FacflltyHnspectfon Contact: Name/TiUe: William Scarpinato Name/Title: Mailing Address Line 1: 5000 Dominion Boulevard Mailing Address Line 1: Mailing Address Line 2: 2 NE Mailing Address Line 2: City: Glen Allen State: VA Zip Code: 23060 City: State: Zip Code: Phone No. (area code) 804-273-3019 I Fax No. (area code) 804-273-2601 Phone No. ( area code ) I Fax No. ( area code) Email Address: �111111m il,:11&wla111Q@.dcim.,cim Email Address: . Responsible Offlcfal/Authorlzed Contact: Invoice Contact: Name/TiUe: Leslie Hartz NamefTitle: William Scarpinato Mailing Address Line 1: 707 E. Main Street Mailing Addrjss Line 1: 5000 Dominion Boulevard Mailing Address Line 2: Mailing Address Line 2: 2NE City: Richmond State: VA Zip Code: 23219 City: Glen Allen State: VA Zip Code: 23060 Phone No. (area code) 804-771-4468 I Fax No. ( area code ) Phone No. (area code) 804-273-3019 I Fax No. (area code) 804-273-2601 �ail Address: l!1:1li!!,b11Jl&@!lcim ,cim Email Address: wllllilm II li!dlllliCIIIC!@!lcim i;cim _,1---APPLICATION IS BEING MADE FOR ·- 0 New Non-permitted Facility/Greenfield D Modification of Facility (permitted) D Renewal with Modification D Renewal (TV Only) --FACILITY CLASSIFICATION AFTER APPLICATION (Check Only, One) D General 0 Small D Prohibitory Small D Synthetic Minor D TitleV -FACILITY (Plant Site) INFORMATION Describe nature of (plant site) operation(s): Facility ID No. TBD Proposed new (greenfield) natural gas pipeline compressor station. Primary SIC/NAICS Code: 4922/486210 Current/Previous Air Permit No. N/A Expiration Date: Facility Coordinates: Latitude: 36.543874 Longitude: -77.505712 Does this application contain confidential YESO N00 ***If yes, please contact the DAQ Regional Office prior to submitting this application.*** data? (See Instructions) PERS<:>N 0R 1 FIRM THA;'f PREPARES APPI.JIC::ATl<:>N Person Name: Robert Sawyer Firm Name: Environmental Resources Management Mailing Address Line 1: 75 Valley Stream Parkway Mailing Address Line 2: Suite 200 City: Malvern !state: PA Zip Code: 19355lcounty: Chester Phone No. ( area code ) 410-266-0006 I Fax No. ( area code ) Email Address: IJlb!l!:l :111�c@!l[l!J ,cim SIGNATURE OF RESPC:>NSIBLE OFFICIAL/AUTHORIZED CONTACT Name (typed): Leslie Hartz Title: VP Pipeline Construction X Signature(Blue Ink): ( 'Y)1 )/ cw'! Date: ?/1/� L/'Attach Additional Sheets As Necessary Page F-72 Attachment F. Air Quality Permit Application Review Documents _VISED 04/10/07 EMISSION SOURCE I IDNO. FORMs A2, A3 EMISSION SOURCE LISTING FOR THIS APPLICATION-A2 112r APPLICABILITY INFORMATION -A3 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate EMISSION SOURCE LISTING: New, Modified, Previously Unpermitted, Replaced, Deleted EMISSION SOURCE I CONTROL DEVICE I CONTROL DEVICE DESCRIPTION ID NO. DESCRIPTION Equipment To Be ADDED By This Application (New, Previously Unpennitted, or Replacement) CT-01 Taurus 70-10802S Compressor Turbine CT-01-SCR Selective Catalvst Reduction CT-01-0C Oxidation Catalyst CT-02 Centaur 50-6200LS Compressor Turbine CT-02-SCR Selective Catalyst Reduction CT-02-0C Oxidation Catalvst CT-03 Centaur 40-47D0S Compressor Turbine CT-03-SCR Selective Catalyst Reduction CT-03-0C Oxidation Catalvst EG-01 Caterpillar G3516 Emeraencv Generator N/A TK-1 Accumulator Storage Tank N/A Fui:i-01 Fuaitive Leaks -Slowdowns NIA Fua-02 Fugitive Leaks -Piping N/A Existing Pennitted Equit>ment To Be NIODIFIED B This Application N/A CJ Equipment To Be DELETED By This Aoolication N/A 112(r) APPLICABILITY INFORMATION Is your facility subject to 40 CFR Part 68 "Prevention of Accidental Releases" -Section 112(r) of the Federal Clean Air Act? No If No, please specify in detail how your facility avoided ap plicability: No chemicals subject to regulation under this Subpart will be present onsite. The aqueous ammonia stored in TK-3 (exempt from permitting) will have an ammonia concentration of less than 20%. If your facility is Subject to 112(r), please complete the following: A. Have you already submitted a Risk Management Plan (RMP) to EPA Pursuant to 40 CFR Part 68.1 0 or Part 68.150? Yes No Specify required RMP submittal date: If submitted, RMP submittal date: B. Are you using administrative controls to subject your facility to a lesser 112(r) program standard? Yes No If yes, please specify: Attach Additional Sheets As Necessary I A2 - I A3 Page F-73 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) YISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ,SSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-01 Taurus 70-10802S Compressor Turbine CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-01 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) O Manufact. of chemicals/coatingsflnks (Form B7) 0 Int.combustion engine/generator (Form B2) O Coating/finishing/printing (Form BS) 0 Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) 0 Other (Form B9) START CONSTRUCTION DATE: April 2011IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Taurus 70-10802S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 SULFUR DIOXIDE (S02) AP-42 0.33 1.43 0.33 1.43 0.33 1.43 NITROGEN OXIDES (NOx) Mfg 1.91 8.35 3.41 14.95 1.91 8.35 BON MONOXIDE (CO) Mfg 2.99 13.08 7.33 32.11 2.99 13.08 ..../...ATILE ORGANIC COMPOUNDS (VOC) Mfg 0.18 0.78 0.33 1.46 0.18 0.78 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00002 0.0001 0.00003 0.0001 0.00002 0.0001 Acetaldehyde 75-07-0 AP-42 0.002 0.01 0.003 0.01 0.002 0.01 Acrolein 107-02-8 AP-42 0.0003 0.001 0.0005 0.002 0.0003 0.001 Benzene 71-43-2 AP-42 0.0005 0.002 0.001 0.004 0.0005 0.002 Ethyl benzene 100-41-4 AP-42 0.001 0.01 0.003 0.01 0.001 0.01 Formaldehyde 50-00-0 Mfg. 0.11 0.50 0.23 0.99 0.11 0.50 Naphthalene 91-20-3 AP-42 0.0001 0.0002 0.0001 0.0004 0.0001 0.0002 PAH AP-42 0.0001 0.0004 0.0002 0.001 0.0001 0.0004 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00002 0.0004 0.15 Acetaldehyde 75-07-0 AP-42 0.002 0.04 13.78 Acrolein 107-02-8 AP-42 0.0003 0.01 2.20 Ammonia 7664-41-7 Mfg. 1.32 31.68 11,563.20 Benzene 71-43-2 AP-42 0.0005 0.01 4.13 Formaldehyde 50-00-0 Mfg. 0.11 2.72 992.03 Toluene 108-88-3 AP-42 0.005 0.12 44.78 � 1330-20-7 AP-42 0.003 0.06 22.05 chments: (1) emissions calculations and supporting documentation: (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges. or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-74 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate B IISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-01 Taurus 70-10802S Compressor Turbine, continued CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-01 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form 81) 0Woodworking (Form 84) O Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form 82) D Coaling/finishing/printing (Form 85) 0 Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE: April 2017 !OPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Taurus 70-10B02S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM10) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source CARBON MONOXIDE (CO) Mfg C )LATILE ORGANIC COMPOUNDS (VOC) Mfg -&Ao OTHER -HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.005 0.002 0.01 0.001 0.005 Toluene 108-88-3 AP-42 0.005 0.02 0.010 0.04 0.005 0.02 Xylene 1330-20-7 AP-42 0.003 0.01 0.005 0.02 0.003 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source Attachments: (1) emissions calculations and supporting documentation; (2) indicate all requested slate and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how .se are monitored and v,;th "'11al frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-75 Attachment F. Air Quality Permit Application Review Documents FORM B2 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality· Application for Air Permit to Construct/Operate I 82 EMISSION SOURCE DESCRIPTION: Taurus 70-10802S Compressor Turbine EMISSION SOURCE ID NO: CT-01 CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-01 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): N/A ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): N/A ENGINE OUTPUT (HP): 11,882 TYPE ICE: 0 GASOLINE ENGINE D DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STATIONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 96.00 N/A •FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 set 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe Formaldehyde EMISSION FACTOR LB/UNIT 3.20 5.30 1.92 1.92 0.30 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: Attach Additional Sheets As Necessary Page F-76 Attachment F. Air Quality Permit Application Review Documents FORM CJ CONTROL DEVICE (THERMAL OR CATALYTIC) C3 (jEVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I .A AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA. CONTROL DEVICE ID NO: CT-01-SCR and CT-01-OC CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-01 EMISSION POINT (STACK) ID NO(S): EP-01 POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER:TBD MODEL NO: MANUFACTURE DATE: TBD PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: 1 PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD !CATALYST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT($) COLLECTED: BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: CONTROL DEVICE EFFICIENCY: OVERALL SYSTEM EFFICIENCY: EFFICIENCY DETERMINATION CODE: ( l;[OTAL EMISSION RATE (LB/HR): AESSURE DROP (IN. H2O): MIN INLET TEMPERATURE (°F): MIN INLET AIR FLOW RATE (ACFM): COMBUSTION CHAMBER VOLUME (FT3): % EXCESS AIR: MAX MAX (SCFM): NO, co voe % % 44 % 80 % 50 % % OUTLET TEMPERATURE (°F): MIN RESIDENCE TIME (SECONDS): COMBUSTION TEMPERATURE (°F): INLET MOISTURE CONTENT (%): CONCENTRATION (ppmv) INLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: G NO GYES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SY:; I tM: jl IACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S): Attach Additional Sheets As Necessary Formaldehyde % % 50 % MAX OUTLET UNITS: UNITS: % % % Page F-77 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-02 Centaur 50-6200LS Compressor Turbine CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 50-6200LS EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 SULFUR DIOXIDE (S02) AP-42 0.20 0.89 0.20 0.894 0.20 0.89 NITROGEN OXIDES (NOx) Mfg 1.19 5.20 2.13 9.31 1.19 5.20 BON MONOXIDE (CO) Mfg 1.87 8.19 4.57 20.04 1.87 8.19 .AATILE ORGANIC COMPOUNDS (VOC) Mfg 0.11 0.48 0.20 0.89 0.11 0.48 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.00005 0.00002 0.0001 0.00001 0.00005 Acetaldehyde 75-07-0 AP-42 0.001 0.005 0.002 0.01 0.001 0.005 Acrolein 107-02-8 AP-42 0.0002 0.001 0.0003 0.001 0.0002 0.001 Benzene 71-43-2 AP-42 0.0003 0.001 0.001 0.003 0.0003 0.001 Ethyl benzene 100-41-4 AP-42 0.0008 0.004 0.002 0.01 0.001 0.004 Formaldehyde 50-00-0 Mfg. 0.08 0.33 0.15 0.66 0.08 0.33 Naphthalene 91-20-3 AP-42 0.00003 0.0002 0.0001 0.0003 0.00003 0.0002 PAH AP-42 0.0001 0.0003 0.0001 0.001 0.0001 0.0003 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.0003 0.10 Acetaldehyde 75-07-0 AP-42 0.001 0.03 9.23 Acrolein 107-02-8 AP-42 0.0002 0.004 1.48 Ammonia 7664-41-7 Mfg. 0.82 19.63 7,165.68 Benzene 71-43-2 AP-42 0.0003 0.008 2.77 Formaldehyde 50-00-0 Mfg. 0.08 1.82 664.78 Toluene 108-88-3 AP-42 0.003 0.12 44.78 c;;? M 1330-20-7 AP-42 0.002 0.06 22 05 chments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-78 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Dlvision of Air Quality -Application for Air Permit to Construct/Operate B SSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-02 Centaur 50-6200LS Compressor Turbine CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): D Coai,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D incineration (Form B8) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 50-6200LS EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM10) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (S02) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source BON MONOXIDE (CO) Mfg ../LATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.003 0.002 0.01 0.001 0.003 Toluene 108-88-3 AP-42 0.003 0.02 0.01 0.03 0.003 0.02 Xylene 1330-20-7 AP-42 0.002 0.01 0.003 0.01 0.002 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source o�hments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-79 Attachment F. Air Quality Permit Application Review Documents FORM 82 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality· Appllcatlon for Air Permit to Construct/Operate I 82 EMISSION SOURCE DESCRIPTION: Centaur 50-6200LS Compressor Turbine EMISSION SOURCE ID NO: CT-02 CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): NIA ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): NIA ENGINE OUTPUT (HP): 6,642 TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine (complete below) - ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STATIONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUE>E STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 60.0 NIA • FUEL CHARACTERISTICS (COMPLETE ALL THAiT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe For maldehyde EMISSION FACTOR LB/UNIT 1.98 3.30 1.20 1.20 0.19 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: • Attach Additional Sheets As Necessary Page F-80 Attachment F. Air Quality Permit Application Review Documents FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC) C3 aEVISED 12/01/01 NCD ENR/Divislon of Air Quality· Application for Air Permit to Construct/Operate I )' AS REQUIRED BY 15A NCAC 2Q .0112,-THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA. CONTROL DEVICE ID NO: CT-02-SCR and CT-02-OC lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-02 EMISSION POINT (STACK) ID NO(S): EP-02 I POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER:TBD MODEL NO: MANUFACTURE DATE: TBD PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD I METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD lcATALYST VOL (FT3): TBD lvELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT(S) COLLECTED: BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: CONTROL DEVICE EFFICIENCY: OVERALL SYSTEM EFFICIENCY: EFFICIENCY DETERMINATION CODE: ci;[OTAL EMISSION RATE (LB/HR): hESSURE DROP (IN. H2O): MIN INLET TEMPERATURE (°F): MIN INLET AIR FLOW RATE (ACFM): COMBUSTION CHAMBER VOLUME (FT3): % EXCESS AIR: MAX MAX (SCFM): NO, co voe % % 44 % 80 % 50 % % OUTLET TEMPERATURE (°F): MIN RESIDENCE TIME (SECONDS): COMBUSTION TEMPERATURE (°F): INLET MOISTURE CONTENT (%): CONCENTRATION (ppmv) INLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: {j NO {;;YES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: ut:::,1.,KIBE ANY AUXILIARY MATERIALS INTRuuUCED IN I u THE CUN I KOL ::,y::, I t:M: TTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL utVICE TO ITS EMISSION SOURCE(S); Attach Additional Sheets As Necessary Formaldehyde % % 50 % MAX OUTLET UNITS: UNITS: % % % Page F-81 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Dlvlslon of Air Quality. Application for Air Permit to Construct/Operate B ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-03 Centaur 40-4700S Compressor Turbine CONTROL DEVICE ID NO(S): CT-03-SCR and CT-03-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) 0 Woodworking (Form B4) O Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) 0 Coating/finishing/printing (Form BS) D Incineration (Form BB) O Liquid storage tanks (Form B3) O Storage silos/bins (Form B6) 0 Other (Form B9) START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 201 B DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 40-4700S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 SULFUR DIOXIDE (SO2) AP-42 0.17 0.76 0.17 0.76 0.17 0.76 NITROGEN OXIDES (NOx) Mfg 1.01 4.44 5.02 22.01 1.01 4.44 �RBON MONOXIDE (CO) Mfg 1.66 7.29 6.92 30.31 1.66 7.29 ].ATILE ORGANIC COMPOUNDS (VOC) Mfg 0.09 0.41 0.17 0.76 0.09 0.41 [EAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.00004 0.00002 0.0001 0.00001 0.00004 Acetaldehyde 75-07-0 AP-42 0.001 0.004 0.002 0.01 0.001 0.004 Acrolein 107-02-8 AP-42 0.0001 0.0006 0.0003 0.001 0.0001 0.001 Benzene 71-43-2 AP-42 0.0003 0.001 0.001 0.002 0.0003 0.001 Ethyl benzene 100-41-4 AP-42 0.001 0.003 0.001 0.01 0.001 0.003 Formaldehyde 50-00-0 Mfg. 0.06 0.27 0.12 0.54 0.06 0.27 Naphthalene 91-20-3 AP-42 0.00003 0.0001 0.0001 0.0002 0.00003 0.0001 PAH AP-42 0.00005 0.0002 0.0001 0.000 0.0000 0.0002 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.0002 0.08 Acetaldehyde 75-07-0 AP-42 0.0009 0.02 7.51 Acrolein 107-02-8 AP-42 0.0001 0.003 1.20 Ammonia 7664-41-7 Mfg. 0.69 16.56 6,044.40 Benzene 71-43-2 AP-42 0.0003 0.006 2.25 Formaldehyde 50-00-0 Mfg. 0.062 1.48 541.00 Toluene 108-88-3 AP-42 0.003 0.07 24.42 �ylene 1330-20-7 AP-42 0.001 0.03 12.02 Q.chments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-82 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) ISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ,ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-03 Centaur 40-4700S Compressor Turbine CONTROL DEVICE ID NO(S): CT-03-SCR and CT-03-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) OWoodworking (Form B4) O Manufact. of chemicals/coatingsflnks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DAT April 2017 !OPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 40-4700S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) I (AFTER CONTROLS I LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source ( \RBON MONOXIDE (CO)Mfg i-,6LATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.003 0.001 0.01 0.001 0.003 Toluene 108-88-3 AP-42 0.003 0.01 0.01 0.02 0.003 0.01 Xylene 1330-20-7 AP-42 0.001 0.01 0.003 0.01 0.001 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source ochments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable pennit limits (e.g. hours of operation, emission rates) and describe w these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-83 Attachment F. Air Quality Permit Application Review Documents FORM 82 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I B2 EMISSION SOURCE DESCRIPTION: Centaur 40-4700S Compressor Turbine EMISSION SOURCE ID NO: CT-03 CONTROL DEVICE ID NO(S): CT-03-SCR and CT-03--OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): NIA ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRSNR): NIA ENGINE OUTPUT (HP): 5,023 TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STATIONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (completa below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 51.0 NIA • FUEL CHARACTERISTICS (CC:>MPLEirE ALL liHAif ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe Formaldehyde EMISSION FACTOR LB/UNIT 4.70 5.70 1.02 1.02 0.16 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: • Attach Additional Sheets As Necessary Page F-84 Attachment F. Air Quality Permit Application Review Documents FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC) C3 dEVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Pennlt to Construct/Operate I � AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA. CONTROL DEVICE ID NO: CT-03-SCR and CT-03-OC lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-03 EMISSION POINT (STACK) ID NO(S): EP-03 I POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER:TBD MODEL NO: MANUFACTURE DATE: TBD PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD !METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD lcATALYST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT(S) COLLECTED: BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: CONTROL DEVICE EFFICIENCY: OVERALL SYSTEM EFFICIENCY: EFFICIENCY DETERMINATION CODE: C .JOTAL EMISSION RATE (LB/HR) : .AESSURE DROP (IN. H2O): MIN INLET TEMPERATURE (°F): MIN INLET AIR FLOW RATE (ACFM): COMBUSTION CHAMBER VOLUME (FT3): % EXCESS AIR: MAX MAX (SCFM): NO, co voe % % 80 % 90 % 50 % % OUTLET TEMPERATURE (°F): MIN RESIDENCE TIME (SECONDS): COMBUSTION TEMPERATURE (°F): INLET MOISTURE CONTENT (%): CONCENTRATION (ppmv) INLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: G NO GYES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: DESCRltlt: ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM: Jf' 1 Ac;H A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S): Attach Additional Sheets As Necessary Formaldehyde % % 50 % MAX OUTLET UNITS: UNITS: % % % Page F-85 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) CREVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B icMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01 C C Caterpillar G3516 Emergency Generator CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form 86) D Other (Form 89) START CONSTRUCTION DAl April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Caterpillar G3516 EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ll.ZZ PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 10.76 0.54 10.76 0.54 10.76 0.54 PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42 10.76 0.54 10.76 0.54 10.76 0.54 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 10.76 0.54 10.76 0.54 10.76 0.54 SULFUR DIOXIDE (SO2) AP-42 0.14 0.01 0.14 0.01 0.14 0.01 NITROGEN OXIDES (NOx) Mfg 124.84 6.24 124.84 6.24 124.84 6.24 CARBON MONOXIDE (CO) Mfg 117.96 5.90 117.96 5.90 117.96 5.90 VOLATILE ORGANIC COMPOUNDS (VOC) Mfg 14.98 0.75 14.98 0.75 14.98 0.75 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATl@N, F@R THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1, 1,2-Trichloroethane 79-00-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1, 1-Dichloroethane 75-34-3 AP-42 0.0001 0.00001 0.0001 0.00001 0.0001 0.00001 1,2-Dichloroethane 107-06-2 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1,2-Dichloropropane 78-87-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1,3-Butadiene 106-99-0 AP-42 0.003 0.0001 0.003 0.0001 0.003 0.0001 1,3-Dichloropropene 542-75-6 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 2,2,4-Trimethylpentane 540-84-1 AP-42 0.003 0.0002 0.003 0.0002 0.003 0.0002 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 0.0002 0.01 0.02 1,2-Dichloroethane 107-06-2 AP-42 0.0001 0.00 0.02 1, 3-Butadiene 106-99-0 AP-42 0.003 0.07 0.30 Acetaldehyde 75-07-0 AP-42 0.03 0.67 2.80 Acrolein 107-02-8 AP-42 0.03 0.67 2.80 Benzene 71-43-2 AP-42 0.007 0.17 0.70 Benzo(a)pyrene 50-32-8 AP-42 0.00000002 0.0000005 0.000002 Sarbon Tetrachloride 56-23-5 AP-42 0.0002 0.01 0.02 Attachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable pennil limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-86 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ,i'-MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01 Caterpillar G3516 Emergency Generator CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):0 Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage �ilos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Caterpillar G3516 EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ll.ll. PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) I (AFTER CONTROLS I LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM10) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source (_ �RBON MONOXIDE (CO)Mfg �OLATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS I LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Acetaldehyde 75-07-0 AP-42 0.03 0.001 0.03 0.001 0.03 0.001 Acrolein 107-02-8 AP-42 0.03 0.001 0.03 0.001 0.03 0.001 Benzene 71-43-2 AP-42 0.01 0.0003 0.01 0.0003 0.01 0.0003 Biphenyl 92-52-4 AP-42 0.00001 0.000001 0.0000 0.000001 0.00001 0.000001 Carbon Tetrachloride 56-23-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 Chlorobenzene 108-90-7 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 Chloroform 67-66-3 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 Ethylbenzene 100-41-4 AP-42 0.0004 0.00002 0.00 0.00002 0.0004 0.00002 TOXIC AIR POLLUTANT. EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO.EF SOURCE lb/hr lb/day lb/yr Chlorobenzene 108-90-7 AP-42 0.0002 0.004 0.02 Chloroform 67-66-3 AP-42 0.0002 0.004 0.02 Ethylene Dibromide 106-93-4 AP-42 0.0003 0.0063 0.03 Formaldehyde 50-00-0 AP-42 0.20 4.77 19.89 Hexane (or n-Hexane) 110-54-3 AP-42 0.002 0.04 0.16 Methylene Chloride 75-09-2 AP-42 0.0005 0.01 0.05 Phenol 108-95-2 AP-42 0.0002 0.004 0.02 rtachments: (1) emissions calculations and supporting documentation; (2) indicate all requested stale and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and wilh what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-87 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) EVISED 12/01/01 NCDENR/Division of Air Quality -A pplication for Air Permit to Construct/Operate B /.:MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01 Caterpillar G3516 Emergency Generator CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Caterpillar G3516 EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZZZ PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source (_ )ARBON MONOXIDE (CO) Mfg 'lfOLATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Ethylene Dibromide 106-93-4 AP-42 0.0003 0.00001 0.0003 0.00001 0.0003 0.00001 Formaldehyde 50-00-0 AP-42 0.20 0.01 0.20 0.01 0.20 0.01 Hexane (or n-Hexane) 110-54-3 AP-42 0.002 0.0001 0.002 0.0001 0.002 0.0001 Methanol 67-56-1 AP-42 0.009 0.0004 0.01 0.0004 0.01 0.0004 Methylene Chloride 75-09-2 AP-42 0.001 0.00003 0.001 0.00003 0.001 0.00003 Naphthalene 91-20-3 AP-42 0.0003 0.00002 0.0003 0.00002 0.0003 0.00002 PAH AP-42 0.0005 0.00002 0.0005 0.00002 0.0005 0.00002 Phenol 108-95-2 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS I LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr Styrene 100-42-5 AP-42 0.0002 0.005 0.02 Toluene 108-88-3 AP-42 0.003 0.08 0.35 Vinyl Chloride 75-01-4 AP-42 0.0001 0.002 0.01 Xylene 1330-20-7 AP-42 0.001 0.02 0.10 ,llachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit Omits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-88 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES} EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B .£MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01 Caterpillar G3516 Emergency Generator CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form B8) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form BS) START CONSTRUCTION DAl April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Caterpillar G3516 EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, llll. PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE - SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM10) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this sourceC )ARBON MONOXIDE (CO) Mfg t,oLATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOUR-CE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Styrene 100-42-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 Toluene 108-88-3 AP-42 0.003 0.0002 0.003 0.0002 0.003 0.0002 Vinyl Chloride 75-01-4 AP-42 0.0001 0.000004 0.0001 0.000004 0.0001 0.000004 Xylene 1330-20-7 AP-42 0.001 0.00005 0.001 0.00005 0.001 0.00005 ---TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE - INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Pages 1-3, for TAP totals for this source .. ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable pennit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary - Page F-89 Attachment F. Air Quality Permit Application Review Documents FORM 82 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate I 82 EMISSION SOURCE DESCRIPTION: Caterpillar G3516 Emergency Generator EMISSION SOURCE ID NO: EG-01 CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION 0 PEAK SHAVER 0 OTHER (DESCRIBE): GENERATOR OUTPUT (KW): 1,000 ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): NIA ENGINE OUTPUT (HP): 1,416 TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP T0 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE r,i OTHER (DESCRIBE). natural gas fired emergency generator (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER Air/fuel ratio OR STATIONARY GP,.S TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL· 0 NATURAL GAS 0 OIL ENGINE TYPE: D 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: D COGENERATION 0 SIMPLE CONTROLS: 0 COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION SELECTIVE CATALYTIC REDUCTION CONTROLS: WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER UNCONTROLLED 0 UNCONTROLLED D LEAN-PREMIX --FUEL USAGE-(INCLUl!>E STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 12.5 NIA •FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSIC:>N FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe OTHER EMISSION FACTOR g/hp-hr 2.00 1.89 NA NA 0.24 UNIT g/hp-hr g/hp-hr g/hp-hr DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: Attach Additional Sheets As Necessary Page F-90 Attachment F. Air Quality Permit Application Review Documents FORMS SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) ISED 12/01/01 NCDENR/Division of Air Quality. Application for Air Permit to Construct/Operate B �ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: TK-1 TK-1 Accumulator Storage Tank CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): TK-1 will have a capacity of 2,500 gallons and will receive liquids from the compressor engine fluids filter. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form 82) D Coating/finishing/printing (Form 85) D Incineration (Form 88) D Liquid storage tanks (Form 83) D Storage silos/bins (Form 86) 0 Other (Form 89) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) --. ----PARTICULATE MATTER<10 MICRONS (PM,o) -------PARTICULATE MATTER<2.5 MICRONS (PM2 s) -------SULFUR DIOXIDE (SO2) -------NITROGEN OXIDES (NOx) -------C \RBON MONOXIDE (CO) -------�LATILE ORGANIC COMPOUNDS (VOC) Mass balance 0.08 0.35 0.08 0.35 0.08 0.35 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr NA TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr NA Qchments: (1) emissions calculations and supporting documentation; (2) indicate all requested stale and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-91 Attachment F. Air Quality Permit Application Review Documents FORM 83 EMISSION SOURCE (LIQUID STORAGE TANK) C REVISED 12/01/01 NCDENR/Divislon of Alr Quality -Application for Alr Permit to Construct/Operate I 83 EMISSION SOURCE DESCRIPTION: Accumulator Storage Tank EMISSION SOURCE ID NO: TK-1 CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05 EACH STORAGE TANK DESCRIBE IN DETAIL THE STORAGE TANK (ATTACH FLOW DIAGRAM): TK-1 will have a capacity of 2,500 gallons and will receive liquids from the compressor engine fluids filter. LIQUID STORED: Liquids from compressor engine fluids filter LIQUID MOLECULAR WEIGHT (LB/LB-MOLE): TBD TANK CAPACITY (GAL): 2,500 VAPOR MOLECULAR WEIGHT (LB/LB-MOLE): TBD AVERAGE LIQUID SURFACE TEMPERATURE (F): 77 VAPOR PRESSURE AT AVE. LIQUID SURFACE TEMP (PSIA): 7.70 (Reid) MIN. LIQUID SURFACE TEMP (F): 44 MAX. LIQUID SURFACE TEMP (F): 80 MAX. TRUE VAPOR PRESS. (PSIA): 7.70 (Reid) BULK LIQUID TEMPERATURE (F): BREATHER VENT SETTINGS (PSIG) VACUUM PRESSURE SHELL DIAMETER (FT): 4.6 SHELL CONDITION: X GOOD POOR IS TANK HEATED: YES X NO SHELL COLOR: Grey/Light MAXIMUM THROUGHPUT (GAL/YR): 12,500 MAXIMUM TURNOVERS PER YEAR: 5.00 WORKING VOLUME (GAL): 2,500 ACTUAL THROUGHPUT (GAL/YR): 12,500 ACTUAL TURNOVERS PER YEAR: 5.00 MAX. FILLS PER DAY: TBD MAX. FILLING RATE (GAUMIN): TBD MIN. DURATION OF FILL (HR/FILL): TBD VERTICAL FIXED ROOF TANKS SHELL HEIGHT (FT): 20 ROOF TYPE: X CONE OR DOME IROOF HEIGHT (FT): 4.61 AVERAGE LIQUID HEIGHT (FT): 10 ROOF CONDITION: X GOOD OR POOR MAXIMUM LIQUID HEIGHT (FT): 20 ROOF COLOR: Grey HORIZONTAL TANKS C SHELL LENGTH (FT): NA IS TANK UNDERGROUND?: YES X NO FLOATING ROOF TANKS DESCRIBE PERTINENT TANK DATA SUCH AS DECKS, RIM-SEALS, LIQUID DENSITY@ 60 DEG F: NA DESCRIBE ANY MONITORING OR WARNING DEVICES (SUCH AS LEAK AND FUME DETECTION INSTRUMENTATION): NA COMMENTS: C Attach Additional Sheets As Necessary Page F-92 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) OEVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B '-:MISSION SOURCE DESCRIPTION; EMISSION SOURCE ID NO: Fug-01 Fugitive Leaks -Slowdowns CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Fugitive Emissions from station blowdowns. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form 86) 0 Other (Form B9) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTUR ER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) . . -. . -. PARTICULATE MATTER<10 MICRONS (PM10) --. . -. . PARTICULATE MATTER<2.5 MICRONS (PM2.5) -. -. . . -SULFUR DIOXIDE (S02) . . . . ---NITROGEN OXIDES (NOx) ------- (_ )ARBON MONOXIDE (CO) --. ----'v'OLATILE ORGANIC COMPOUNDS (VOC) Mass balance 4.30 18.84 4.30 18.84 4.30 18.84 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS I LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Hexane 110-54-3 Mass balance 0.24 1.06 0.24 1.06 0.24 1.06 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr Hexane 110-54-3 Mass balance 0.24 5.81 2120.00 .. llachmenls: (1) emissions calculations and supporting documentation; (2) indicate all requesled state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary I Page F-93 Attachment F. Air Quality Permit Application Review Documents FORM 89 EMISSION SOURCE (OTHER) REVISED: 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate I EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-01 Fugitive Leaks -Slowdowns CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO: 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM): Fugitive Emissions from station blowdowns. MATERIALS ENTERING PROCESS -CONTINUOUS PROCESS MAX. DESIGN REQUESTED CAPACITY TYPE UNITS li\PACITY (UNIT/� LIMITATION(UNIT/HR) Natural gas NA NA NA MATERIALS ENTERING PROCESS • BATCH OPERATION MAX. DESIGN REQUESTED CAPACITY TYPE UNITS ACITY (UNIT/BA LIMITATION (UNIT/BATCH) NA MAXIMUM DESIGN (BATCHES / HOUR): NA REQUESTED LIMITATION (BATCHES / HOUR): NA (BATCHES/YR): NA FUEL USED: NA TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): NA MAX. CAPACITY HOURLY FUEL USE: NA REQUESTED CAPACITY ANNUAL FUEL USE: NA COMMENTS: Attach Additional Sheets as Necessary 89 Page F-94 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B .lMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-02 Fugitive Leaks -Piping CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Fugitive Emissions from station piping leaks. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) D Int.combustion engine/generator (Form 82) D Coating/finishing/printing (Form 85) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage silos/bins (Form 86) 0 Other (Form 89) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY CRITE�IA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE - SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) - -- -- -- PARTICULATE MATTER<10 MICRONS (PM10) - - ----- PARTICULATE MATTER<2.5 MICRONS (PM25) -- ----- SULFUR DIOXIDE (S02) --- ---- NITROGEN OXIDES (NOx) ------- (_ '\ARBON MONOXIDE (CO) ------- 'vOLATILE ORGANIC COMPOUNDS (VOC) EPA 4.57 20.03 4.57 20.03 4.57 20.03 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Hexane 110-54-3 Mass Balance 0.26 1.13 0.26 1.13 0.26 1.13 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr Hexane 110-54-3 Mass Balance 0.26 6.19 2,260.00 ... ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-95 Attachment F. Air Quality Permit Application Review Documents • • FORM 89 EMISSION SOURCE (OTHER) REVISED: 12/01/01 NCDENR/Division of Air Quality • Application for Air Permit to Construct/Operate I EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-02 Fugitive Leaks -Piping CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO: 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM): Fugitive Emissions from station piping leaks. MATERIALS ENTERING PROCESS· CONTINUOUS PROCESS MAX. DESIGN REQUESTED CAPACITY TYPE UNITS IA,PACITY (UNIT/� LIMITATION(UNIT/HR) Natural gas NA NA NA MATERIALS ENTERING PROCESS • BATCH OPERATION MAX. DESIGN REQUESTED CAPACITY TYPE UNITS �ACITY (UNIT/BA LIMITATION (UNIT/BATCH) NA MAXIMUM DESIGN (BATCHES / HOUR): NA REQUESTED LIMITATION (BATCHES / HOUR): NA (BATCHESNR): NA FUEL USED: NA TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): NA MAX. CAPACITY HOURLY FUEL USE: NA REQUESTED CAPACITY ANNUAL FUEL USE: NA COMMENTS: Attach Additional Sheets as Necessary 89 Page F-96 Attachment F. Air Quality Permit Application Review Documents FORM D1 FACILITY-WIDE EMISSIONS SUMMARY OVISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate CRITERIA AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS / (BEFORE CONTROLS / LIMITATIONS) LIMITATIONS) AIR POLLUTANT EMITTED tons/yr tons/yr PARTICULATE MATTER (PM) 18.68 18.68 PARTICULATE MATTER< 10 MICRONS (PM 10) 18.68 18.68 PARTICULATE MATTER< 2.5 MICRONS (PM2 5) 18.68 18.68 SULFUR DIOXIDE (S02) 3.09 3.09 NITROGEN OXIDES (NOx) 24.23 52.51 CARBON MONOXIDE (CO) 34.46 88.36 VOLATILE ORGANIC COMPOUNDS (VOC) 41.62 43.07 LEAD OTHER HAZARDOUS AIR P0LLUjl"ANTJj§MIS_Sl0N§l lf',IFORMATION -FACILITY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS / (BEFORE CONTROLS / LIMITATIONS) LIMITATIONS) HAZARDOUS AIR POLLUTANT EMITTED GAS NO. tons/yr tons/yr 1, 1,2,2-Tetrachloroethane 79-34-5 0.00001 0.00001 1, 1,2-Trichloroethane 79-00-5 0.00001 0.00001 1, 1-Dichloroethane 75-34-3 0.00001 0.00001 1,2-Dichloroethane 107-06-2 0.00001 0.00001 1,2-Dichloropropane 78-87-5 0.00001 0.00001 �3-Butadiene 106-99-0 0.0003 0.0005 }-Dichloropropene 542-75-6 0.00001 0.00001 2,2,4-Trimethylpentane 540-84-1 0.0002 0.0002 Acetaldehyde 106-99-0 0.02 0.03 Acrolein 75-07-0 0.004 0.006 Benzene 71-43-2 0.005 0.010 Biphenyl 92-52-4 0.000001 0.000001 Carbon Tetrachloride 56-23-5 0.00001 0.00001 TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE D1 POTENTIAL EMISSIONS (AFTER CONTROLS / LIMITATIONS) tons/yr 18.68 18.68 18.68 3.09 24.23 34.46 41.62 POTENTIAL EMISSIONS (AFTER CONTROLS / LIMITATIONS) tons/yr 0.00001 0.00001 0.00001 0.00001 0.00001 0.0003 0.00001 0.0002 0.02 0.004 0.005 0.000001 0.00001 INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15A NCAC 20 .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM 02 IF NECESSARY. Modeling Required ? Note TOXIC AIR POLLUTANT EMITTED GAS NO. lb/hr lb/day lb/year Yes No 1 1, 1,2,2-Tetrachloroethane 79-34-5 0.0002 0.01 0.02 X 1 1,2-Dichloroethane 107-06-2 0.0001 0.00 0.02 X 1 1,3-Butadiene 106-99-0 0.003 0.07 0.62 X 1 Acetaldehyde 75-07-0 0.03 0.75 33.32 X 1 Acrolein 75-07-0 0.03 0.69 7.69 X 1 Ammonia 7664-41-7 2.83 68.04 24,773.28 X 1 Benzene 71-43-2 0.01 0.19 9.86 X 1 Benzo(a)pyrene 50-32-8 0.00000002 0.0000005 0.000002 X 1 Carbon Tetrachloride 56-23-5 0.0002 0.01 0.02 X 1 Chlorobenzene 108-90-7 0.0002 0.004 0.02 X 1 Chloroform 67-66-3 0.0002 0.004 0.02 X 1 Ethylene Dibromide 106-93-4 0.0003 0.01 0.03 X 1 ( formaldehyde 50-00-0 0.45 10.79 2,217.70 X 1 )xane (or n-Hexane) 110-54-3 0.24 5.85 2,120.16 X 1 ..;OMMENTS: Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat Input value for these sources Is less than 450 MMBtu/hr, and they will be the only source of benzene at the facility. Page F-97 Attachment F. Air Quality Permit Application Review Documents FORM D1 FACILITY-WIDE EMISSIONS SUMMARY CREVISED 12/01/01 NCDENR/Dlvision of Air Quality -Application for Air Permit to Construct/Operate D1 CRITERIA AIR POLLUTANT El'/IISSIONS INFORMAljl0N -FA€11!!1TY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS/ (BEFORE CONTROLS/ (AFTER CONTROLS / LIMITATIONS) LIMITATIONS) LIMITATIONS) AIR POLLUTANT EMITTED tons/yr tons/yr tons/yr PARTICULATE MATTER (PM) PARTICULATE MATTER< 10 MICRONS (PM10) PARTICULATE MATTER< 2.5 MICRONS (PM25) SULFUR DIOXIDE (SO2) NITROGEN OXIDES (NOx) See Form D1, Page 1, for criteria pollutant totals. CARBON MONOXIDE (CO) VOLATILE ORGANIC COMPOUNDS (VOC) LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS / (BEFORE CONTROLS/ (AFTER CONTROLS / LIMITATIONS) LIMITATIONS) LIMITATIONS) HAZARDOUS AIR POLLUTANT EMITTED GAS NO. tons/yr tons/yr tons/yr Chlorob enzene 108-90-7 0.00001 0.00001 0.00001 Chloroform 67-66-3 0.00001 0.00001 0.00001 Ethylb enzene 100-41-4 0.01 0.02 0.01 Ethylene Dibromide 106-93-4 0.00001 0.00001 0.00001 Formaldehyde 75-07-0 1.11 2.21 1.11 Hexane (or n-Hexane) 110-54-3 1.06 1.06 1.06 Methanol 67-56-1 0.0004 0.0004 0.0004 Methylene Chloride 75-09-2 0.00003 0.00003 0.00003 Napthalene 91-20-3 0.001 0.001 0.001 PAH 0.001 0.002 0.001 Phenol 108-95-2 0.00001 0.00001 0.00001 Propylene oxide 75-56-9 0.01 0.02 0.01 Styrene 100-42-5 0.00001 0.00001 0.00001 Toluene 108-88-3 0.05 0.10 0.05 TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS/ LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15ANCAC 2Q .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM 02 IF NECESSARY. Modeling Required ? Note TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No 1 Methylene Chloride 75-09-2 0.0005 0.01 0.05 X 1 Phenol 108-95-2 0.0002 0.004 0.02 X 1 Styrene 100-42-5 0.0002 0.005 0.02 X 1 Toluene 108-88-3 0.01 0.36 99.55 X 1 Vinyl Chloride 75-01-4 0.0001 0.002 0.01 X 1 Xylene 1330-20-7 0.01 0.16 48.94 X 1 -( -COMMENTS: Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these sources is less than 450 MM Btu/hr, and they will be the only source of benzene at the facility. Page F-98 Attachment F. Air Quality Permit Application Review Documents FORM D1 FACILITY-WIDE EMISSIONS SUMMARY C REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I D1 CRITERIA AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS / (BEFORE CONTROLS / (AFTER CONTROLS / LIMITATIONS) LIMITATIONS) LIMITATIONS) AIR POLLUTANT EMITTED tons/yr tons/yr tons/yr PARTICULATE MATTER (PM) PARTICULATE MATTER< 10 MICRONS (PM10) PARTICULATE MATTER< 2.5 MICRONS (PM25) SULFUR DIOXIDE (SO2) NITROGEN OXIDES (NOx) See Form D1, Page 1, for criteria pollutant totals. CARBON MONOXIDE (CO) VOLATILE ORGANIC COMPOUNDS (VOC) LEAD OTHER -HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS (AFTER CONTROLS / (BEFORE CONTROLS / (AFTER CONTROLS / LIMITATIONS) LIMITATIONS) LIMITATIONS) HAZARDOUS AIR POLLUTANT EMITTED I CAS NO. tons/yr tons/yr tons/yr Vinyl Chloride 75-01-4 0.000004 0.000004 0.000004 Xylene 1330-20-7 0.024468 0.05 0.02 C TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE .1 INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15A NCAC 20 .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY. I Modeling Required ? I TOXIC AIR POLLUTANT EMITTED I CAS NO. lb/hr I lb/day lb/year I Yes No I See Form D1, Pages 2 and 3, for for TAP totals -G COMMENTS: Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC 02Q.0702(a){25), as the aggregate allowable natural gas heat Input value for these sources is less than 450 MMBtulhr, and they will be the only source of benzene at the facility. Page F-99 Attachment F. Air Quality Permit Application Review Documents FORM D2 AIR POLLUTANT NETTING WORKSHEET vised: 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate I D2 ruRPOSE OF NETTING: X AIR TOXICS PSD (100/250 tons per year) PSD SIGNIFICANT LEVELS AIR POLLUTANT: All (See Form D1) CAS NO.: EMISSION SOURCE ID NOS.: Facility-Wide SECTION A -EMISSION OFFSETTING ANALYSIS FOR MODIFIED/NEW SOURCES Summarize inthis section EMISSIONS -USE APPROPRIATE COLUMNS ONLY using the B forms LB/YEAR LB/DAY LB/HR MODIFICATION See comments below INCREASE -MINUS--MINUS--MINUS--MINUS-MODIFICATION DECREASE =EQUALS= =EQUALS= =EQUALS= =EQUALS= NET CHANGE FROM MODIFICATION SECTION 8-FACILITY-WIDE EMISSION NETTING ANALYSIS CREDITABLE See comments below INCREASE -MINUS--MINUS--MINUS--MINUS-CREDITABLE () DECREASE = EQUALS= =EQUALS= =EQUALS= =EQUALS= NET CREDITABLE CHANGE SECTION C -FACILITY-WIDE EMISSIONS TOTAL FACILITY See comments below EMISSIONS TPER LEVELS (20 .0711) CHECK HERE IF AN AIR DISPERSION MODELING ANALYSIS IS REQUIRED COMMENTS: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these sources is less than 450 MMBtu/hr, and they will be the only source of benzene at the facility. Page F-100 Attachment F. Air Quality Permit Application Review Documents FORM D4 EXEMPT AND INSIGNIFICANT ACTIVITIES SUMMARY N'ISED: 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate I D4 ACTIVITIES EXEMPTED PER 2Q .0102 OR INSIGNIFICANT ACTIVITIES PER 2Q .0503 FOR TITLE V SOURCES SIZE OR BASIS FOR EXEMPTION OR INSIGNIFICANT DESCRIPTION OF EMISSION SOURCE PRODUCTION RATE ACTIVITY 1. Natural Gas Boiler (used for building heat) 6.3 MMBtu/hr Per 15A NCAC 2Q.0102(c)(2)(B)(iv), fuel combustion equipment (except internal combustion engines and equipment burning waste oil) with a heat input rating less than 1 o million Btu per hour used solely for space heating is exempt from permitting. 2.TK-2, Hydrocarbon Waste Tank, will receive and store used oil 1,500 gallons Per 15A NCAC 02Q.0102(c)(1 )(D)(i), storage tanks used used in oil-filled operational equipment throughout the facility. solely to store used motor oil, lubricants, and cooling oils are exempt from permitting. 3. TK-3, Aqueous Ammonia Storage Tank, will be used to supply 8,000 gallons Per 15A NCAC 02Q.0102(c)(1)(D)(iii), storage tanks used aqueous ammonia to the SCRs. solely to store inorganic liquids are exempt from permitting. 4. 6. 7. 8. 9. 10. ? Page F-101 Attachment F. Air Quality Permit Application Review Documents • APPENDIXB FACILITY PLOT PLAN • ERM ACP, LLC-ACMSTATION Page F-102 Attachment F. Air Quality Permit Application Review Documents K � -.- lj J=I ,,,.,, �Jl -----"__!l]---------------------------- --,_:-HFI /,) ,,.-q JI JI TI.IIPW'l' ctlll'ill!'.X:Tllll �:..---- I -''f I ( 1: \ ;a \a,: I \t f \ I --..__ J�\\l ., ___ -s4, .... ------- y I -------_J\_ 1 //\ \1 r�eif''"�;.'""""\! !\ I I I 1 \ I 1\i I I I I I I I I I I I ! I -' ! I / I I :: : �------' I I I : (' """'"'�: (=,.=-i)!=·ll'-1--:z;-._ill.l<.tl,::;:;_i-l_�-----,, \\ �L . I\\ -·= u ��"',:;""��\,:i[�)-i_;I l-lL / I �-•1 � II �---- / j _,, .,. �-•2!! ""...!!.--. "• I '0c : "" : : r -.,---' u I.\, I I I \I i t I ---- ; I � __ ,_,.,.._!!·'"'"'"' �\ \ \ \ a I ����� 1 1 " I I I I I I I -f -·-·--·-·---·, 1 1 ��·��-f/1:..-----J---\ -:i , . . . . . . . : \ \ n / / / / \ l '� -l ':_cccccccccccccccc�''l)_,I "' ___ L I /if ,,�,..---------�-� ,1 }/1/ : �------------------------ SITE LOCATION LAT 35•32•39 48" LONG: 77°30'30 97" MILE POST 293.2� ISSUED FOR REVIEW 7/7/15 1:J.I/ I I /7;/ �------------1: --------� I 'Ii ; I I I I I ,' 1/I l I 1/i LEGEND --• - - Ttlilf'CIIIIARY�Od'TUREWCE -PEltUAHENTUAINTAINEDMEA ----roce I'', .•• I" I ·--�--·�••· -·-�---�··•I k"""="'-=-�!,L" "' OU, 12t10'1', 12'10'1' Atlantic Coast Pipeline, LLC .«SVl.llstMlllnSl Oarbbutg,'Nut\Arglnla 2f1Xt1 /PhoM:(304)523-tlOOO NORTHHAMPTON COMPRESSOR STATION PRELIMINARY SITE PLAN I I 1-'°'""""'oNjn•� ""I---_.._...----..- --··---·-�a.tllnlCSlR...,E 2085A F Page F-103 Attachment F. Air Quality Permit Application Review Documents APPENDIXC POTENTIAL TO EMIT CALCULATIONS • ERM ACP, LLC-ACP-3STATION Page F-104 Attachment F. Air Quality Permit Application Review Documents Table C-1 Permit to Construct Application Proiect Equipment List ACP Northampton Compressor Station -Northampton County, North Carolina Emission Source Manufacturer Model/Type Rated Point ID Capacitv CT-01 Compressor Turbine Solar Turbines Taurus 70-10802S 11,882 hp CT-02 Compressor Turbine Solar Turbines Centaur 50-6200LS 8,414 hp CT-03 Compressor Turbine Solar Turbines Centaur 40-4700S 5,023 hp EG-01 Emeroencv Generator Caterpillar G3516 1,416 hp WH-01 Boiler TBD TBD 6.3 MMBtu/hr FUG-01 Fugitive Leaks -Slowdowns --- FUG-02 Fuoitive Leaks -Pipino --- TK-1 Accumulator Tank --2,500 aal TK-2 Hydrocarbon (Waste Oil) Tank ----1,500 gal TK-3 Ammonia Tank ----8,000 aal Page F-105 Attachment F. Air Quality Permit Application Review Documents • Table C-2 Potential Emissions From Combustion S011rces ACP Northampton Compressor Station -Northampton Co1111hJ, North Caro/i11a Turbine Operational Pou,unelers· Emergency Generator Operational Hours: Normal Hours or Operation: 8,677 Normal Hours or O�rallon: 100 Hour.; al Low Load ( <50%) 0 Hour.; of Low TemD. (< 0 de2. F) 50 Hours or Start-un/Shut-down 33.3 Total Hour.; ofOnPrahon (hr/vr): 8,760 Pre-Control Potential IQ Emit Power Criteria Pollutants nm Combustion Sources Ralina Units Fuel Nox LL Voe 502 PMF Solar Taurus 70 Turbine 11,882 ho Natural Gas 14.9 23.8 1.36 143 2.42 Solar Centaur SOL Turbine 8,414 ho Natural Gas 9.2 14.8 0834 0894 1.51 Solar Centaur 40 Turbine 5,023 ho Natural Gas 22.0 25.6 0.70 2 0760 1.29 Caleroillar G3516 Eaen 1416 ho Natural Gas 0.312 0.295 00375 00003 00214 Boiler 6.3 MMBtu/hr Natural Gas 1.35 2.27 0.149 0.0162 0.0514 Total (tons/vd 47.7 66.B 3.08 3.10 5.3 Turbine Control Efficiencies Control Technol� NOx co voe Selective Catalytic Reduction tC,entaur 40) 80% . Selechve Calalvtic Reduction (All Others) 44% Ox1dahon Catalvst (Centaur 40) 90% 50% Oxadahon Catalvst I All Olhers) . 80% 50% Post-Control Potential to Emil Power Criteria PoUutants rrov Combustion Soun:es Ratlnn Units Fuel NOx co Solar Taurus 70 Turbine 11,882 hp Nalural Gas 8.25 4.76 Solar Centaur SOL Turbine 8,414 ho Natural Gas 5.14 2.96 Solar Centaur 40 Turbine 5,023 ho Natural Gas 4 39 256 Cateroillar G3516 Eoen 1416 ho Natural Gas 0.312 0.295 Boiler 6.3 MMBlu/hr Natural Gas 1.35 2.27 Total (tons/vd 19.4 12.8 Notes: (1) Turbine emissions are calculaled by the followinA fomMJla: ER• Run Hours / 2000 • (1 -Control Efficiency) ER = Emission Rate for oarticular equipment and pollutant (lbs/hr) 2000 = the amounl of lbs in a ton voe 0680 0.417 0.351 00375 0.149 1.63 (2) Emergency Generator emissions are calculated by the following fonrula: Power RaUng • Run Hours • EF / 2000 Power RatinA = EnQine hp ratinA (hp) EF = Emission Factor from eilher manufacturer's data or AP-42 (lb/hp-hr) 2000 = lhe amounl of lbs in a ton (3) Boller/Heater emissions calculaled by lhe following fonnula: EF • Power Rating • Run Hours / HHV / 2000 EF = AP-42 Emission Factor (lb/MMSCF) Power Ralmg = Boilern-Jeater Heat capacity (MMBtu/hr) HHV = Natural Gas High Heating Value (1020 MMBtu/MMSCF) S02 PMF 143 2.42 0894 1.51 0760 1.29 0.0003 00214 0.0162 0,0514 3.10 5,3 Boiler/Heater Operational P,Uilmelers: Normal Hours of Operation: j 8,760 PMF•10 PMF-2,5 PMC <..02 2.42 2.42 5.99 49,980 151 151 3.74 31,295 1.29 1.29 3.18 26,718 00214 0.0214 0006 77 9 00514 0.0514 0154 3246 5,3 5.3 13.07 111 317 PMF-10 PMF-2.6 PMC CO2 2.42 242 5.99 49,980 1 51 1 51 3.74 31,295 1.29 1.29 3.18 26,718 00214 00214 0006 77.9 00514 00514 0.154 3,246 5.3 5,3 13.07 111 317 (4) Turbines ara equipped with Selective CatalyUc Reduction (SCR) and oxidation catalyst for control of NOx (44%), CO (80%), and voe (50%) ( 5) Taurus Centaur 40 oxidation catalyst has a control of 90 % for CO (6) Emergency generalor engine hp laken from manufacturer dala (7) Boiler assumed lo have low-NOx burners (8) See the "HAP Em1ss1ons" worksheet for a more detailed breakdown of HAP emissions (9) See Emssions Factors table for Emissions Factors for each operating scenario. ( 10 ) Each slart-uplshut-down event assumed to last 1 O minutes I GHG Emissions rmv Ammonia rtovl HAPltovl <..H4 N20 CO2e ''"� !Otat-r 3.62 1.26 50,446 5.77 0525 2.26 0.788 31,587 3.58 0 352 1.92 0.671 26,966 3.02 0.286 0.290 0 85 1 0 00143 0.0622 00595 3266 0 00511 8.15 2.7B 112 350 12.4 1.23 GHG Emissions ,mu Ammonia ,mv, HAPltovl CH4 N20 CO2e ,m� IOUII �.- 362 1.26 50,446 5.77 0525 2.26 0788 31.587 358 0352 1.92 0.671 26.966 3.02 0.286 0.290 0 B5.1 0 00143 00622 0,0595 3,266 0 0,0511 8.15 2.78 112 350 12.4 1.229 Page F-106 Attachment F. Air Quality Permit Application Review Documents • Ta"1c C-3 Event Bastd Pottmtial Ernissio11s Fro,n Comlmstion Sor,rC].'s ACP Nortl1ampton Compressor Station -Nortlta111pto11 Co11nty, Nortlt Caro/i,ra Start:YP Ernl11k>n1 Sbu'1own Emltl.km .,_ __I,;:;: Sollr Taurus 70 Turbne ,,-2 Sols Centaur 50L Turbine 8 414 Sollr Centaur -40 Turtwie &M3 .... Units t , ... ·-I h• ho hn NaturalG• � � fuol NIIUralGas Natural Gail Nft.lralGa Toiaisusb�·� COfflPF!ISO( Bfqwdqwn Emissions �rceDesi�: � rntk.t.lm Taul Slr.•m Molen1LarW•l•hl Hm�voc C..rhi1"0loxldl- NM ...... � .... � 'voc r-� n.RuLll'll" lsoffulane n-Prnlane OOl'l'rur. � ... - TWI vex Fnctkin Tcll.alHArfr.lctk,n Dkmlllma [mm :iS.dWC l:t:ail! = 30000 -,. ........... 18 _ .... 03% ,. 1691 lb/-l �=r I 1v•-t 1 � Fracllon"' 111.,P-_,,Fmtk.-1 (wt.� , ... -1-1.01 l.(J.11:1. ,.,,,. 211.01 0.99-H, ,..,,. lfi.CM 94.llS. ....,,. ,..,,, l.9D1. -f.1.10 0.5-161. ,.,.. "-" ...... ..... "'" """" ...... 72.15 0.022' ..... "-" ..., ..u ... 71.11 1Ull2' u ... 10021 ...... ·- li1'<, u ... -----I�...'.'..� voe CO2 SoW TIUUS 70 Tlnne 100 2.218 2.293 ScMar'Centaur50L Turbine 100 2.216 2.293 SoarCentaur40TurbW'le 100 2.216 2.293 .., 6.1141 1.••o Olowdown {rpm Shm+ma emtt• I --;.:;-100 100 100 E CH4 7 75634 7 227 1::: GHQ .... --·- Soar TIUl'Ua 70 Turt>ne Solar Centaur 50L Turtwle Sol# Centa.1r 40 Turbine Toca,-n Silr:WMr lkrw+mo er,m, Sile-Wide lMowdown Voumetrt: now rale Metha,e MolecularW� _Methaoe Percent Weigh!_ Site-Wide Blowdown Rkm:down fain Sbs: m4r f!rtlia c, �P-3 100 100 100 2 000 000 10 n� M..m ( Total 8'owdown EmtHlon• (1Dn!1?1 voe 3675 3675 367 5 11.024 scffevent ocf-tbmol --,. _!b{_event 11.1 CM 380 380 380 11.41 11.5 c- 12530 12530 12 539 370 ciiioEiiinloni 300 ,, .. 143 NOx 00550 0.0200 00150 0.010 O.ffl coa. 1803 1893 1893 5171 ooa. 3139 3139 3139 11411 C02e "iioo" ... 11.!.092 co 366 346 rn � --co 467 1.n 151 7.150 11.20 83000 -,..- 1]! .,,. 2803 HAh 0.125 0.125 0.1 25 0.375 HAh 0.207 0.207 0.207 0.82 2 HAP1 0_._068 1,06 00420 0CMDO oo:mi T.ffl'" 0.0530 00200 01'1170 G.mtO oJii ,....,... .......-,. lb/-l CH< 0.16& 0.160 0.148 0.471 -- CH< 200 0212 100 00000 ••• 00600 -. o.- 117.f I o.136 • • 30.2 27.5 23 .t 34.1 120 108 .,_ m Page F-107 Attachment F. Air Quality Permit Application Review Documents Table C-4 Combustion Source Criteria Pollutant Emission Factors ACP Nort1iampto11 Compressor Station -Nortl,ampto11 Co,mhJ, Nortl, Carolina Solar Turbine Nonna! ,,.,.,ration Emission Factors llblhrl Eauloment Name Fuel Units NOx co voe SO2 PMF PMF-10 PMF-2.5 PMC CO2 CH4 N20 Solar Centaur 40 Turbine Natural Gas lb/hr 4.70 5.70 0.160 0.173 0.294 0.294 0.294 0.727 6100 0.439 0.153 Solar Centaur 50L Turbine Natural Gas lb/hr 1.98 3.30 0.190 0.204 0.345 0.345 0.345 0.855 7145 0.516 0.180 Solar Taurus 70 Turbine Natural Gas lb/hr 3.18 5.30 0.310 0.326 0.553 0.553 0.553 1.37 11411 0.826 0.288 Notes (1) Pre-Control Emission Rates for NOx, CO, VOC, PMF, PMC, and CO2 taken from Solar Turbine Data at 100% load and O degrees F (2) Emission Factors for SO2, CH4, N2O taken from AP-42 In (lbs/MMBtu) and multiplied by turbine fuel throughput by Solar Turbine at 100% load and O degree F to get Emission Rates (3) Assume PMF=PMF-10=PMF-2,5: Filterable and Condensable based on Solar Turbine Emission Factor and ratio of AP-42 Table 3.1 factors (4) NH3 emission rates based on a 10 ppm ammonia sUp from the SCR based on manufacturer information (5) CO2e emission rate calculated by mulUplying each GHG (CO2, CH4, N2O) by its Global Warming Potential (GWP) and adding them together (6) CO2 GWP = 1: CH4 GWP = 25; N2O GWP = 298 [40 CFR Part 98] Solar Turbine Alternate ,...ration Emission Factors 111/hrl < O """nHtS F Solar Turbine Low Load F Enul=•nt Name Fuel Units NOx co voe NOx co voe Solar Centaur 40 Turbine Natural Gas lb/hr 62.7 34.2" 0.320 36.6 2.280 6.40 Solar Centaur 50L Turbine Natural Gas lb/hr 26.4 19.8 0.380 15.4 1,320 7.60 Solar Taurus 70 Turbine Natural Gas lb/hr 42.4 31.8 0.620 24,7 2,120 12.4 Notes (1) Pre-Control low temperature Emission Rates for NOx, CO, voe. Conservatively assume 120 ppm NOx, 150 ppm CO, and 5 ppm VOC (10% of UHC) per Table 2 of Solar PIL 167 (2) Pre-Control low load Emission Rates for NOx, CO, voe. Conservatively assume 70 ppm NOx, 10,000 ppm CO, and 100 ppm VOC (10% of UHC) per Table 4 of Solar PIL 167 Solar Turbine Start-uo and Shutdown Emission Factors llb/eventl Start-uo EFs Shutdown EFs Eaulpmem Name Fuel Units NOx co voe CO2 CH4 C02e NOx co voe CO2 Solar Centaur 40 Turbine Natural Gas lb/event 0.700 64.4 0.740 392 2.96 466 0.300 30.2 0.340 181 Solar Centaur 50L Turbine Natural Gas lb/event 0.800 69.1 0.800 469 3.20 549 0.400 35.4 0.400 217 Solar Taurus 70 Turbine Natural Gas lb/event 0.800 73.1 0.840 519 3.36 603 1.10 93.4 1.06 575 Noles (1) Start-up and Shutdown Emissions based on Solar Turbines Incorporated Product Information Letter 170: Emission Estimates at Start-up, Shutdown, and Commissioning for SoLoNOx Combustion Products (13 June 2012). Emission Estimates do not include SO2, PM, N2O, or any HAPs. (2) voes assumed to be 20% of UHC and CH4 assumed lo be 80% of UHC. (3) CO2e emission rate calculated by multiplying each GHG (CO2, CH4) by its Global Warming Potential (GWP) and adding them together (4) CO2 GWP = 1: CH4 GWP = 25: [40 CFR Part 98] Enalne and Boller Emission Factors Eauloment Tu"" Fuel Units NOx co voe SO2 PMF PMF-10 Boiler < 100 MMBtu Natural Gas lb/MMscf 50 84 5.5 0.6 1.9 1.9 Scace & Water Heaters Natural Gas lb/MMscf 100 84 5.5 0.6 1.9 1.9 Engine 2 SLB Natural Gas lb/MMBtu 3.17 0.386 0.12 0.000588 0.0384 0.0384 1000 KW Caleroillar Eoen Natural Gas lh/hn.hf 0.004408 0.004166 0.000529 4.62E-06 0.0003018 0.00030179 Notes (1) NOx, CO, voe, and PMF-10 Emission Factors for Boilers< 100 MMBtu from ETI Combustion Analysis June 2015 (2) All other emission factors for natural gas boilers taken from AP-42 Tables 1.4-1 & 1.4-2 (3) Emission Factors for Space & Water Heaters taken from AP-42 Tables 1.4-1 & 1.4-2 (4) Emission Factors for 2 SLB engine taken from AP-42 Table 3.2-1 (5) NOx, CO, VOC, CO2, and CH4 emission factors for Caterpillar Egens taken from Caterpillar Manufacturer data PMF-2.5 1.9 1.9 0.0384 0.000302 PMC CO2 5.7 120000 5.7 120000 0.00991 110 7.79E-05 1.0998 (6) SO2, PMF, PMF-10, PMF-2.5, PMC, and N2O Emission factors for Caterpillar Egens taken from AP-42 Table 3.2-1 and converted using manufacturer fuel data (7) Assume PMF=PMF-10=PMF-2.5 (8) CO2e emission rate calculated by multiplying each GHG (CO2, CH4, N2O) by its Global Warming Potential (GWP) and adding them together (9) CO2 GWP = 1; CH4 GWP = 25: N2O GWP = 298 (40 CFR 98] CH4 2.3 2.3 1.45 0.0041 CH4 1.36 1.60 4.24 N20 2.2 2.2 0 0 CO2e NH3 6157 0.690 7212 0.818 11517 1.32 CO2e 215 257 681 CO2• NH3 120713 0.00 120713 0.00 146 0.00 1 0.00 Page F-108 Attachment F. Air Quality Permit Application Review Documents • Table C-5 Hazardo11s Air Poll11ta11t (HAP) E111issio11s From Comb11stio11 Sources ACP Nortlta111pto11 Compressor Statio11 -Nortlta111pto11 Co,mhJ, Nortl1 Caroli11a Annual HAP Emissions lib/vrl Quanmv tlJ ACP-3 1 1 1 1 Solar Centaur Solar Centaur Solar Taurus Boiler< 100 Pollutant HAP? 40 Turbine 50L Turbine 70 Turbine MMBtu 1, 1,2,2-Tetrachloroethane Yes 1, 1,2-T richloroethane Yes 1, 1-Dichloroethane Yes 1,2,3-Trimethvlbenzene No 1,2,4-Trimethvlbenzene No 1,2-Dichloroethane Yes 1,2-Dichloropropane Yes 1,3,5-Trimethvlbenzene No 1,3-Butadiene Yes 1,3-Dichloroorooene Yes 2,2, 4-Trimethvloentane Yes 2-Methvlnaohthalene No 0.001 3-Methvlchloranthrene No 0.000 7, 12-Dimethvlbenzlalanthracene No 0.001 Acenaphthene No 0.000 Acenaohthvlene No 0.000 Acetaldehvde Yes Acrolein Yes Anthracene No 0.000 Benzi a lanthracene No 0.000 Benzene Yes 0.114 Benzolalovrene No 0.000 Benzo b)fluoranthene No 0.000 Benzo elovrene No Benzo 11,h,i)pervlene No 0.000 Benzo klfluoranthene No 0.000 Biphenvl Yes Butane No 113.622 Butvr/lsobutvraldehvde No Carbon Tetrachloride Yes Chlorobenzene Yes Chloroethane Yes Chloroform Yes Chrvsene No 0.000 Cvclohexane No Cvclooentane No Dibenzo(a,hlanthracene No 0.000 Dichlorobenzene Yes 0.065 Ethane No 167.728 Ethvlbenzene Yes Ethvlene Dibromide Yes Fluoranthene No 0.000 Fluorene No 0.000 Formaldehyde Yes 541.000 664.779 992.029 4.058 Hexane !or n-Hexanel Yes 97.391 lndeno(1,2,3-c,dJpvrene No 0.000 lsobutane No Methanol Yes Methylcydohexane No Methvlene Chloride Yes n-Nonane No n-Octane No Naphthalene Yes 0.033 PAH Yes Pentane (or n-Pentanel No 140.675 Pervlene No Phenanthrene No 0.001 Phenol Yes Prooane No 86.569 Propylene Oxide Yes Pvrene No 0.000 Stvrene Yes Tetrachloroethane No Toluene Yes 0.184 Vinvl Chloride Yes XYiene Yes Arsenic Yes 0.011 Barium No 0.238 Bervllium Yes 0.001 Cadmium Yes 0.060 1 1 1 Boiler< 100 Boller< 100 1000 KW MMBtu MMBtu Caterpillar Egen 0.024 0.019 0.014 0.013 0.040 0.015 0.016 0.006 0.295 0.016 0.305 0.000 0.000 0.008 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.001 2.796 2.803 0.000 0.000 0.000 0.000 0.000 0.000 0.009 0.004 0.699 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.001 9.018 3.607 1.711 0.157 0.022 0.016 0.017 0.000 0.000 0.000 0.111 0.034 0.000 0.000 0.005 0.002 13.312 5.325 25.544 0.039 0.026 0.000 0.000 0.000 0.000 0.000 0.001 0.322 0.129 19.888 7.729 3.092 0.160 0.000 0.000 0.000 1.351 0.894 0.122 0.053 0.011 0.027 0.003 0.001 0.035 0.048 11.165 4.466 0.551 0.000 0.000 0.000 0.001 0.015 6.871 2.748 10.340 0.000 0.000 0.000 0.020 0.015 0.006 0.347 0.009 0.097 0.001 0.000 0.019 0.008 0.000 0.000 0.005 0.002 Page F-109 Attachment F. Air Quality Permit Application Review Documents • • Table C-5 Hazardous Air Pollutant (HAP) Emissions From Combustion Sources ACP Northa111pto11 Compressor Statio11 -Northa111pto11 Co1111hJ, North Caroli11a Quanmv til ACP-3 Pollutant Chromium Cobalt Copper Manaanese Mercury Molvbdenum Nickel Selenium Vanadium Zinc Lead Total HAPs Total HAP/Unit (IDIYf Total HAP/unit 11 r-r) Hazardous Air Pollutant Notes: HAP? Yes Yes No Yes Yes No Yes Yes No No Yes (1) Emissions above are on a per unit basis Annual HAP Emissions lib/vrl 1 1 1 1 Solar Centaur Solar Centaur Solar Taurus Boller< 100 40 Turbine 50L Turbine 70 Turbine MMBtu 0.076 0.005 0.046 0.021 0.014 0.060 0.114 0.001 0.124 1.569 0.027 572.934 704.019 1050.586 572.934 704.019 1060.61111 102 0.2116 0.352 0.525 0.051 1 1 Boller< 100 Boller< 100 MMBtu MMBtu 0.006 0.002 0.000 0.000 0.004 0.001 0.002 0.001 0.001 0.000 0.005 0.002 0.009 0.004 0.000 0.000 0.010 0.004 0.125 0.050 0.002 0.001 11.11 3.24 0.004 0.002 (2) Calculations for the Caterpillar emergency generator assume 100 hours of operation; all ather calculations assume 8,760 hours of operation (3) Heat rates for Solar Turbines taken from Solar Datasheets (4) Solar turbines have a 50% HAP control efficiency due to the Oxidation Catalyst 1 1000 KW Caterpillar Egan 29 0.014 Page F-110 Attachment F. Air Quality Permit Application Review Documents Table C-6 Combustion Source HAP Emission Factors ACP Northampto11 Compressor Station -Northampton Co,mhJ, North Carolina I mission Factors Solar Centaur Solar Centaur Solar Taurus Boller< 100 1000 KW Pollutant HAP? 40 Turbine SOL Turbine 70 Turbine MMBtu Caterpillar Egan lb/MMBtu lb/MMBtu lb/MMBtu lb/MMscf lb/ho-hr 1, 1,2,2-Tetrachloroethane Yes 1.7E-07 1, 1,2-T richloroethane Yes 1.3E-07 1.1-Dichloroethane Yes 9.9E-08 1,2,3-Trimethvlbenzene No 9.0E-08 1,2,4-Trimethvlbenzene No 2.BE-07 1 2-Dichloroethane Yes 1.1E-07 1,2-Dichloroorooane Yes 1.1E-07 1,3,5-Trimethvlbenzene No 4.SE-08 1,3-Butadiene Yes 2.1E-06 1 3-Dichloroorooene Yes 1.1E-07 2,2,4-Trimethvloentane Yes 2.2E-06 2-Methvlnaohthalene No 2.4E-05 5.4E-08 3-Methvlchloranthrene No 1.BE-06 7, 12-Dimethvlbenz(alanthracene No 1.SE-05 Acenaohthene No 1.BE-06 3.4E-09 Acenaohthvlene No 1.BE-06 8.1E-09 Acetaldehvde Yes 2.0E-05 Acrolein Yes 2.0E-05 Anthracene No 2.4E-06 1.BE-09 Benz(alanthracene No 1.BE-06 8.5E-10 Benzene Yes 2.1E-03 4.9E-06 Benzo alovrene No 1.2E-06 1.4E-11 Benzo blftuoranthene No 1.BE-06 2.2E-11 Benzo elovrene No 6.0E-11 Benzo a,h,iloervlene Na 1.2E-06 6.3E-11 Benza klfluoranthene No 1.BE-06 1.1E-11 Biohenvl Yes 1.0E-08 Butane No 2.1E+00 1.2E-05 • Butvr/lsobutvraldehyde No 1.1E-06 Carbon Tetrachloride Yes 1.SE-07 Chlorobenzene Yes 1.1E-07 Chloroethane Yes Chloroform Yes 1.2E-07 Chrvsene No 1.BE-06 1.7E-09 Cvdohexane No 7.BE-07 Cvciooentane No 2.4E-07 Dibenzo(a,h)anthracene No 1.2E-06 Dichlorobenzene Yes 1.2E-03 Ethane No 3.1E+00 1.BE-04 Ethvlbenzene Yes 2.7E-07 Ethylene Dibromide Yes 1.9E-07 Fluoranthene No 3.0E-06 9.2E-10 Fluorene No 2.BE-06 4.3E-09 Formaldehvde Yes 2.9E-03 2.9E-03 2.9E-03 7.SE-02 1.4E-04 Hexane (or n-Hexanel Yes 1.BE+00 1.1E-06 lndeno(1,2,3-c,d1ovrene No 1.BE-06 2.SE-11 lsobutane No 9.SE-06 Methanol Yes 6.3E-06 Methvlcvdohexane No 8.SE-07 Methvlene Chloride Yes 3.7E-07 n-Nonane No 7.BE-08 n-Octane No 1.9E-07 Naphthalene Yes 6.1E-04 2.SE-07 PAH Yes 3.4E-07 Pentane (or n-Pentanel No 2.6E+00 3.9E-06 Pervlene No 1.3E-11 Phenanthrene No 1.7E-05 9.0E-09 Phenol Yes 1.1E-07 Propane No 1.6E+00 7.3E-05 Proovlene Oxide Yes Pvrene No 5.0E-06 1.SE-09 Styrene Yes 1.4E-07 Tetrachloroethane No Toluene Yes 3.4E-03 2.SE-06 Vinvl Chloride+A32 Yes 6.3E-08 XYiene Yes 6.BE-07 • Arsenic Yes 2.0E-04 Barium No 4.4E-03 Beryllium Yes 1.2E-05 Cadmium Yes 1.1E-03 Page F-111 Attachment F. Air Quality Permit Application Review Documents • Table C-6 Co111b11stio11 Source HAP E111issio11 Factors ACP Nortlta111pto11 Compressor Statio11 -Nortltampto11 Co,mhJ, Nortlt Caroli11a Emission Factors Pollutant Chromium Cobalt Coooer Manoanese Mercurv Molvbdenum Nickel Selenium Vanadium Zinc Lead Total HAPs Hazardous Air Pollutant Notes: HAP? Yes Yes No Yes Yes No Yes Yes No No Yes Solar Centaur Solar Centaur Solar Taurus 40 Turbine &0L Turbine 70 Turbine lb/MMBtu lb/MMBtu lb/MMBtu 3.1E-03 3.1E-03 3.1E-03 (1) Emission factors for Solar and Capstone natural gas turbines from AP-42 Table 3.1-3 (2) Emission factors for natural gas boilers from AP-42 Tables 1.4-2, 1.4-3, and 1.4-4 Boller< 100 MMBtu lb/MMscf 1.4E-03 B.4E-05 8.SE-04 3.BE-04 2.SE-04 1.1E-03 2.1E-03 2.4E-05 2.3E-03 2.9E-02 5.0E-04 1000 KW Caterpillar Egan lb/hp-hr (3) Emission factors for 2 SLB natural gas engines and Caterpillar natural gas emergency generators taken from AP-42 Table 3.2-1 (4) Emission factors for Solar natural gas turbines and Caterpillar natural gas emergency generators converted using 1 KWh= 3412 Btu and 1 kw= 1.341 hp (5) Emission Factors (lb/MMBtu) for Formaldehyde and Total HAPs for Solar Turbines from Solar PIL 168 Page F-112 Attachment F. Air Quality Permit Application Review Documents • Table C-7 Pote11tial Emissio11s From F11gitive Leaks ACP Nort/rampto11 Compressor Statio11 -Nortlrampto11 Co1111ty, North Caro/i11a Fugitive Emissions (FUG) Source DcslL,nollon: flJC,()2 Qm3tioFYI P.1r.1mcln:F Annuol Houni n( Of'(?mlion (hr/ rr): "·""' Compmpor fqgltjve Eml .. jon• R.ale Equipment Stnke _H4 Emluktn P.-ctar"I Ion/comp-hr 5olur Turbine Ga, 2.67&02 1. Default mcth.ine basisonJ 1.-mi.wion fanor W-m fromToble6-6ulComp.-ndNmolGn'1.'MOU9('GIIS � �lt-9 k>rtheOil 11nJ Ga,JnJustry, APL Aur.m.l. 2llJ9. 2. SiunplrmkubUons:Hoursrl�lion {hr/yr)• EF (Ion/ romprt.'5Wf'·lv)/ Mrihanefnaction PiPdlnr Nahlr:AI CH Futltlvc Emltuil Eitv.Jpmeat Stnke E1111NloA Pactori11 ...... c ...... TNI HC r.tattlal balNlont lhllo.,l'Nllttr . ..,.,. Valves Ga, -1.50£.00 616 2.91 Compressor• c., 5.71E•01 3 in PumpS...'1)1• c., 2-I0E-0.J 0,00 Dlhl.'T'B (comr,resSOf's onJ others) Ga, 8.BOE-03 0,00 Conn«lnrs Ga, 2.00&0! 1 2.00&0! Flunr,c!I Go, 3.90£.0l 340 0.133 Opcns-0nJt"J lines Go, 2.00E-03 0.00 Tal•I 174 1. FJ'A Protorol for l::.quipn'llont L.ub Emis&ions f.slimal'-" (El'A-lSJ/R·IJ>Oln Tahkol-4:0ilond Gilli Ptoduction CJrmttiPRII Emill56on FaOora. l. Comronmt cvunl b:a.J on ft;askSyak.'ffll Engintffing &t""-!1e. "•"lYCe'cr'!t-"10: Polmtial � (lh/hr) .. Efflmion Factor (lh/hr/!iOUrtl!) 05ourreCvunl Potmli.ll Em-ona (tOM/yr) •(lb/hr),__,.• HoursofOp.'falson lhrfyr) • (1 lon/2.JXU lh) ... 12.7 751 0.00 0.00 8.76£.0.I 0.581 0,00 761 VOCWeJcbl Fractlaa 11026 11026 0.()26 0.026 0.()26 0.026 0,026 VOC!mlN11t1111 CO,Welgbl ... Pra<doa 0.334 110271 19.7 0.0271 0,00 OJIZ71 0,00 0.0271 2.30£<)5 0.0271 0.015 0.0271 0,00 0.0271 20,0 CCJi EntiMloM "'' 0.J.15 20.4 0,00 0,00 2.38E-05 0.016 noo 207 CH,Welghl M"ac:llon1� ._ ... CH,Welgbl Fraction OJ!95 OJ!95 OJ!95 0.1!95 OJ!95 0,1195 OJ!95 Fug EmJNlan Rate 250.2 CH.,EmlNien1 llAPWeipt HAPEm._._ '"" &ocdoa ... 11.-1 148&03 1.88E-02 672 1.48&03 1.11E+OO 0.00 1,48&03 0.00E+OO 0.00 1.48&03 O.OOE+OO 7,tJ4E-{U 1,48S-m 1.JOE-06 0.520 1,486-03 8.59E-{U 0,00 148&03 O.OOEtOO 61!3 113Et00 Page F-113 Attachment F. Air Quality Permit Application Review Documents Table C-8 Tank Emissions ACP Northampton Compressor Station -Northampton County, North Carolina !Source Designation:TK-1, TK-2, TK-3 Tank Parameters Source Type of Tank Contents Capacity Throughput Tank Diam. Tank Length Paint Color Paint (gal) gaJ/yr ft ft Condition TK-1 Horizontal, fixed Produced Fluids 2,500 12,500 4.61 20 Light Grey Good TK-2 Horizontal, fixed Lube Oil 1,500 7,500 4.12 10 Light Grey Good Total Emissions voe Emissions Source Plashing Losses Working Losses Breathing Losses Total Losses lcy'hr tpy lcy'hr tpy lcy'hr tpy lcy'hr tpy TK-1111 ------0.080 0.350 TK-2'21 NA NA 7.76E-07 3.40E-06 2.24E-06 9.BOE-06 3.01E-06 1.32E-05 1. Losses were calculated for TK-1 using E&P Tanks Software. See attached for output. 2. Losses were calculated for TK-2 using EPA's TANKS 4.09d software with default breather vent settings. 3. Losses (Emissions) from TK-3 8,000-gallon Ammonia tank assumed to be insignficant. Page F-114 Attachment F. Air Quality Permit Application Review Documents Table C-9 Profrct Pote11tial E111issio11s ACP Northa111pto11 Compressor Statio11 -Nortl1a111pto11 Com1hJ, North Caroli11a Criteria Pollutants nn, GHG Emissions nn Ammonla,mv HAP1,mv1 Combustion Sources ID NOx co voe SO 2 PMF PMF-10 PMF-2.5 PMC CO2 CH4 N2O CO2e l'ln-> ,.,..., MAI" Solar Taurus 70 Turbine CT-01 8.35 13.1 0.775 1.43 2.42 2.42 2.42 5.99 50035 4.00 1.26 50511 5.77 0.525 Solar Centaur SOL Turbine CT-02 5.20 8.19 0.477 0.894 1.51 1.51 1.51 3.74 31329 2.50 0.788 31627 3.58 0.352 Solar Centaur 40 Turbine CT-03 4.44 7.29 0.405 0.760 1.29 1.29 1.29 3.18 26747 2.14 0.671 27000 3.02 0.286 Caterpillar G3516 Eaen EG-01 0.312 0.295 0.0375 0.0003 0.0214 0.0214 0.0214 0.006 77.9 0.290 0.0 85.1 0 0.0143 Boller WH-01 1.35 2.27 0.149 0.0162 0.0514 0.0514 0.0514 0.154 3246 0.0622 0.0595 3266 0 0.0511 Fualtlve Leaks • Blowdowns FUG-01 . . 18.84 . . . . . 19.49 643 16,092 . 1.063 Fugitive Leaks . Plpln11 FUG-02 . . 20.0 . . . . . 20.7 683 . 17,106 . 1.13 Accumulator Tank TK-1 . . 0.350 . . . . . . . . . . . Hydrocarbon (Waste 011) Tank TK-2 . . 1.32E-05 . . . . . . . . . . . Total (tons,vr) 19.7 31.1 41.1 3.10 5.3 5.3 5.3 13.1 111,475 1,335 2.78 145,686 12.4 3.42 Page F-115 Attachment F. Air Quality Permit Application Review Documents TK-1 Produced Fluids Tank 081015.txt ****************************************************************************************** '� Project setup Information * ****************************************************************************************** Project File Pipeline\Draft Rule 13 -Flowsheet selection calculation Method control Efficiency Known Separator Stream Entering Air composition Date : M:\Projects\D\Dominion\Atlantic coastal Pipeline and Supply Header APCl\Emission calcs\TK-1 -Produced Fluids Tank.ept oil Tank with Separator AP42 100.0% Low Pressure Gas NO 2015.07.13 ****************************************************************************************** * Data Input * ****************************************************************************************** separator Pressure separator Temperature Molar GOR Ambient Pressure Ambient Temperature ClO+ SG Cl0+ MW LOW No. 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 Pressure Gas component H2S 02 CO2 N2 Cl C2 C3 i-C4n-C4i-c5n-c5C6C7+ Benzene Toluene E-BenzeneXylenesn-C6224Trimethylp 552.00[psig] 77 .00[FJ 0.0500 14. 70 [psi a]70 .00 [F]0.8990166.00 mol % 0.0000 0.0000 1.0410 0.9940 94.2060 2.9230 0.5460 0.0790 0.0840 0.0240 0.0220 0.0320 0.0490 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Page 1 •• Page F-116 Attachment F. Air Quality Permit Application Review Documents • • TK-1 Produced Fluids Tank 081015.txt C7+ Molar Ratio: c7 : 1.0000 cs : 1.0000 C9 : 1.0000 ClO+ 1.0000 --sales oil -----------------------------------------------------------------------------Production Rate 0.8[bbl/day] Days of Annual operation 365 [days/year] API Gravity 46.0 Reid Vapor Pressure 7.70[psia] Bulk Temperature 80.00[F] --Tank and shell Data Diameter Shell Height cone Roof slope Average Liquid Height vent Pressure Range solar Absorbance 5.0B[ft] 11. 90[ft]0.062.50[ft]0.06[psi]0. 54 --Meteorological Data -------------------------------------------------------------------Page 1----------------------------------------------------------------E&P TANK city Charleston, wv Ambient Pressure 14.70[psia] Ambient Temperature 70.00[F] Min Ambient Temperature 44.00[F] Max Ambient Temperature 65.50[F] Total solar Insolation 1123.00[Btu/ftA2*day] ****************************************************************************************** * calculation Results * ****************************************************************************************** --Emission Summary Item Total HAPS Total HC voes, c2+ voes, c3+ uncontrolled [ton/yr] 0.010 0.425 0.383 0.350 uncontrolled Vapor Recovery Info. HC vapor GOR 21. 230019.9800 26.05 xlE-3 xlE-3 Uncontrolled [lb/hr] 0.002 0.097 0.087 0.080 [MSCFD] [MSCFD] [SCF/bbl] Emission compos1t1on ------------------------------------------------------------------No component uncontrolled uncontrolled Page 2 Page F-117 Attachment F. Air Quality Permit Application Review Documents • • 1 H2S 2 02 3 CO2 4 N2 5 Cl 6 C2 7 C3 8 i-C49 n-C410 i-c511 n-c512 C6 13 C7 14 ca 15 C9 16 ClO+ 17 Benzene 18 Toluene 19 E-Benzene20 Xylenes 21 n-C622 224Trimethylp Total [ton/yr] 0.002 0.000 0.022 0.001 0.043 0.032 0.083 0.033 0.102 0.039 0.047 0.015 0.014 0.006 0.001 0.000 0.001 0.000 0.000 0.000 0.010 0.000 0.451 TK-1 Produced Fluids Tank 081015.txt [lb/hr] 0.000 0.000 0.005 0.000 0.010 0.007 0.019 0.008 0.023 0.009 0.011 0.003 0.003 0.001 0.000 0.000 0.000 0.000 0.000 0.000 0.002 0.000 0.103 Stream Data ---------------------------------------------------------------------------No. component MW LP oil Flash oil sale oil Flash Gas w&s Gas mol %mol %mol %mol %mol %1 H2S 34.80 0.0508 0.0349 0.0030 0.6834 0.1835 2 02 32.00 0.0000 0.0000 0.0000 0.0000 0.0000 3 CO2 44.01 0.2437 0.0907 0.0000 6.3467 0.0001 4 N2 28.01 0.0102 0.0005 0.0000 0.3990 0.0001 5 Cl 16.04 0.9543 0.1475 0.0000 33.1362 0.0001 6 C2 30.07 0.6701 0.3531 0.0000 13.3133 0.0001 7 C3 44.10 2.1827 1.7648 0.4600 18.8508 16.8782 8 i -C4 58.12 1.1269 1.0450 0.6191 4.3934 9.6293 9 n-C4 58.12 4.6091 4.4100 3.1320 12.5490 33.6645 10 i -c5 72.15 3.1066 3.0997 2.8099 3.3810 11.9899 11 n-c5 72.15 5.0558 5.0823 4.8107 4.oooo 14.9972 12 C6 86.16 4.1726 4.2520 4.3657 1.0044 4.1822 13 C7 100.20 10.3655 10.6043 11.1500 0.8388 3.6780 Page 2----------------------------------------------------------------E&P TANK14 ca 114.23 10.8426 11.1074 11.7774 0.2806 1.2761 15 C9 128.28 5.5127 5.6497 6.0063 0.0497 0.2328 16 ClO+ 166.00 45.9695 47.1217 50.1681 0.0099 0.0486 17 Benzene 78.11 0.5685 0.5808 0.6057 0.0778 0.3297 18 Toluene 92.13 0.2132 0.2183 0.2311 0.0082 0.0362 19 E-Benzene 106.17 0.0711 0.0729 0.0774 0.0009 0.0041 Page 3 Total Emissions mol % 0.5755 0.0000 4.9770 0. 312925.984910.440118.42515.523417.10615.23896.37341. 69021.4516 0.4954 0.0892 0.0182 0.1322 0.0142 0.0016 Page F-118 Attachment F. Air Quality Permit Application Review Documents • TK-1 Produced Fluids Tank 081015.txt 20 Xylenes 106.17 0.6802 0.6971 0.7408 0.0075 0.0344 0.0133 21 n-C6 86.18 3.5939 3.6672 3.7955 0.6694 2.8351 1.1368 22 224Trimethylp 114.24 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 MW 123.89 126.03 129.50 38.64 63.78 44.07 Stream Mole Ratio 1.0000 0.9755 0.9688 0.0245 0.0067 0.0312 Heating value [BTU/SCF] 2044.13 3547.91 2368.67 Gas Gravity [Gas/Air] 1.33 2.20 1. 52Bubble Pt.@ l00F [psi a] 56.28 19.66 6.19 RVP @ lO0F [psi a] 126.75 78.89 38.81 spec. Gravity@ l00F 0.800 0.803 0.810 Page 4 Page F-119 Attachment F. Air Quality Permit Application Review Documents S 4.0 Report Identification User Identification: City: State: Company: Type of Tank: Description: Tank Dimensions Shell Length (ft): Diameter (ft): Volume (gallons): Turnovers: Net Throughput(gal/yr): Is Tank Heated (y/n): Is Tank Underground (y/n): Paint Characteristics Shell Color/Shade: Shell Condition Breather Vent Settings Vacuum Settings (psig): Pressure Settings (psig) TANKS 4.0.9d Emissions Report -Detail Format Tank lndentification and Physical Characteristics TK-2 West Virginia Horizontal Tank Used Oil Aboveground Storage Tank N N Gray/Light Good 15.05 4.12 1,500.00 5.00 7,500.00 -0.03 0.03 Meterological Data used in Emissions Calculations: Charleston, West Virginia (Avg Atmospheric Pressure = 14.25 psia) file:///C:/Program%20Files/Tanks409d/summarydisplay.htm Page Lof7 8/10/2015 Page F-120 Attachment F. Air Quality Permit Application Review Documents TANKS 4.0 Report TK-2 -Horizontal Tank Daily Liquid Surf Temperature (deg F) Mixture/Component Month Avg. Min Max. used Oil All 61.57 52 .97 70.18 TANKS 4.0.9d Emissions Report - Detail Format Liquid Contents of Storage Tank Liquid Bulk Vapor Liquid Temp Vapor Pressure (psia) Mol. Mass (degF) Avg. Min. Max. Weight. Fract. 57.22 0.0001 0.0001 00001 380.0000 file:// IC :/Program%20Fi les/Tanks409d/summarydisplay .htm Vapor Mass Mol. Basis for Vapor Pressure Fract. Weight Calculations 200.00 8/10/2015 Page F-121 Attachment F. Air Quality Permit Application Review Documents TK-2 -Horizontal Tank Annual Emission Calcaulations Standing Losses (lb): Vapor Space Volume (cu ft)· Vapor Density (lb/cu ft): Vapor Space Expansion Factor: Vented Vapor Saturation Factor. Tank Vapor Space Volume: Vapor Space Volume (cu fl): Tank Diameter (fl): Effective Diameter {ft): Vapor Space Outage (ft): Tank Shell Length {ft)· Vapor Density Vapor Density (lb/cu ft): Vapor Molecular Weight {lb/lb-mole): Vapor Pressure at Daily Average Liquid Surface Temperature (psis): Daily Avg. Liquid Surface Temp. {deg. R): Daily Average Ambient Temp. {deg. F): Ideal Gas Constant R (psia cult / {lb-mol-deg R)): Liquid Bulk Temperature {deg. R): Tank Paint Solar Absorptance {Shell): Daily Total Solar Insulation Factor {Btu/sqfl day): Vapor Space Expansion Factor Vapor Space Expansion Factor. Daily Vapor Temperature Range {deg. R): Daily Vapor Pressure Range (psia): Breather Vent Press. Setting Range(psia): Vapor Pressure at Daily Average Liquid Surface Temperature (ps1a)· Vapor Pressure at Daily Minimum Liquid Surface Temperature {psia): Vapor Pressure at Daily Maximum Liquid Surface Temperature (psia)· Daily Avg Liquid Surface Temp {deg R): Daily Min. Liquid Surface Temp. {deg R): Daily Max. Liquid Surface Temp. {deg R): Daily Ambient Temp. Range {deg. R) Vented Vapor Saturation Factor Vented Vapor Saturation Factor. Vapor Pressure at Daily Average Liquid: Surface Temperature (psia): Vapor Space Outage {ft): Working Losses {lb): Vapor Molecular Weight {lb/lb-mole): Vapor Pressure at Daily Average L1qu1d Surface Temperature (psia): Annual Net Throughput {gal/yr.): Annual Turnovers: Turnover Factor: Tank Diameter {fl): 0.0196 127.7971 0.0000 0.0618 1.0000 127.7971 4.1200 8.8875 2.0600 15.0500 0.0000 380.0000 0.0001 521.2427 54.98 33 10 .731 516.8 933 0.5400 1,250.5726 00618 34 4127 0.0000 00600 0.0001 0.0001 0.0001 521.2427 512.6395 529.8458 21.5333 1 0000 0.0001 20600 0.0068 380.0000 0.0001 7,500.0000 5.0000 1.0000 4.1200 TANKS 4.0.9d Emissions Report -Detail Format Detail Calculations (AP-42) file:///C:/Program%20Files/Tanks409d/summarydisplay.htm 8/10/2015 Page F-122 Attachment F. Air Quality Permit Application Review Documents S 4.0 Report Working Loss Product Factor. 1,0000 Total Losses (lb): 0.0264 file:// IC :/Program%20Fi Ies/Tanks409d/summarydisplay .htm 8/10/2015 Page F-123 Attachment F. Air Quality Permit Application Review Documents TAaS 4.0 Report Pagec5'7 file:/ /IC :/Program%20Fi le s/Tanks409d/summaryd isplay .htm 8/10/2015 Page F-124 Attachment F. Air Quality Permit Application Review Documents Emissions Report for: Annual TK-2 -Horizontal Tank I 11 !components II lused Oil II TANKS 4.0.9d Emissions Report -Detail Format Individual Tank Emission Totals Losses(lbs) Working Los�! Breathing Lossll Total Emissions! 0.0111 0.0211 0.031 file:/ I IC :/Program%20F i les/Tanks409d/summarydisplay .htm Page 6 of 7 8/10/2015 Page F-125 Attachment F. Air Quality Permit Application Review Documents T'CSS 4.0 Report • Page(;J7 file:///C:/Program%20Files/Tanks409d/summarydisplay.htm 8/10/2015 Page F-126 Attachment F. Air Quality Permit Application Review Documents APPENDIXD VENDOR SPECIFICATIONS • ERM ACP. LlC-ACP-3STATION Page F-127 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Emissions Estimates Taurus 70-10802S Assumptions: pipeline natural gas, sea level, 4"/4" inlet/outlet losses, nominal p_erformance ...,-10 1oaa tuet flow, 1nerma1 rn,1X nuX vU vU UHi., Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 5941 63.54 23.79 9 2.3 25 3.9 25 59 5430 56.92 24.27 9 2.0 25 3.4 25 100 4341 49.58 22.28 9 1.7 25 3.0 25 fD7D 108(1 - fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff, % (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 0111:t 7ti.l:11 29.49 9 2.8 25 4.7 25 59 8145 68.47 30.27 9 2.5 25 4.2 25 100 6512 59.08 28.05 9 2.1 25 3.5 25 11111'10 1oaa fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 11882 87.27 34.64 9 3.2 25 5.3 25 59 10860 79.24 34.87 9 2.8 25 4.8 25 100 8683 68.40 32.30 9 2.4 25 4.1 25 Utll,,; YU\, YUv vU.C .-,vnuu,.fi i-nnu,,.t, 1:xnaust =naust1-1ow (lb/hr) (ppm) (lb/hr) lblhr lb/mmbtu lb/hr Temp(F) (lb/hr) 2.2 2.5 0.2 !IJ.!1 0.02 1.4 910 199,373 2.0 2.5 0.2 7407 0.02 1.3 991 170,275 1.7 2.5 0.2 6336 0.02 1.1 1045 149576 UHC voe voe CO2 PM1D/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr) 2.7 2.5 0.3 l�J 0.02 1.7 898 224,735 2.4 2.5 0.2 !IIIU5 0.02 1.5 957 194,658 2.0 2.5 0.2 7544 0.02 1.3 1019 165855 - UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr) 3.1 2.5 0.3 f1lff1 0.02 1.9 864 366,922 2.8 2.5 0.3 10301 0.02 1.7 908 334,207 2.3 2.5 0.2 8730 0.02 1.5 945 298619 Page F-128 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Emissions Estimates Centaur 50-6200LS Assumptions: J>_ipe_li_rt_l!_ natural gas, 150' elevation, 5"/8" inlet/outlet losses_._11ominal p_erformance ov,1,1011a --- fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 3321 39.27 21.54 9 1.4 25 2.4 25 59 3006 35.20 21.73 9 1.3 25 2.1 25 100 2426 30.76 20.06 9 1.1 25 1.8 25 l0'70 1080 fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 4981 47.21 26.85 9 1.7 25 2.9 25 59 4509 42.05 27.29 9 1.5 25 2.5 25 100 3639 36.70 25.23 9 1.3 25 2.2 25 "luv,a 108Q" -- fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 6642 54.55 30.98 9 2.0 25 3.3 25 59 6012 50.72 30.16 9 1.8 25 3.1 25 100 4852 44.43 27.78 9 1.6 25 2.6 25 UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) 1111hr lb/mmbtu lb/hr Temp (F) (lb/hr) 1.4 2.5 0.1 5155 0.02 0.9 837 139,384 1.2 2.5 0.1 4591 0.02 0.8 915 119,683 1.0 2.5 0.1 3938 0.02 0.7 966 103305 UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp(F) (lb/hr) 1.6 2.5 0.2 6189 0.02 1.0 849 152,889 1.5 2.5 0.2 5479 0.02 0.9 908 133,124 1.2 2.5 0.1 4695 0.02 0.8 959 115664 UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr) 1.9 2.5 0.2 7145 0.02 1.2 871 161,184 1.7 2.5 0.2 GlqJ 0.02 1.1 956 144,840 1.5 2.5 0.2 -55719 0.02 1.0 1004 127484 Page F-129 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Emissions Estimates Centaur 40-4700S Assumptions: pipeline natural gas, sea level, 4"/4" inlet/outlet losses, nominal performance ov701oaa - fue111ow, 1nermat NUX NUX 1..U c.;u UAC Temp, F HP mmbtu/hr LHV Eff, % (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 2511 32.29 19.78 25 3.2 50 3.9 25 59 2278 29.85 19.41 25 3.0 50 3.6 25 100 1735 26.09 16.92 25 2.6 50 3.1 25 ,.,-111,oa.o - fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 3767 39.31 24.39 25 3.9 50 4.8 25 59 3417 35.41 24.55 25 3.5 50 4.3 25 100 2602 30.78 21.51 25 3.0 50 3.7 25 1uv70 ioao - fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm) 0 5023 46.39 30.23 25 4.7 50 5.7 25 59 4556 42.27 29.51 25 4.2 50 5.1 25 100 3470 35.07 27.45 25 3.4 50 4.2 25 UAC vui;,; VVv """ l'MlU/.iC,ti l'MlUt.:,ti 1:xnaust 1:xnaust i-1ow (lb/hr) (ppm) (lb/hr) lblhr lb/mmbtu lb/hr Temp(F) (lb/hr) 1.1 2.5 0.1 4259 0.02 0.7 726 140,550 1.0 2.5 0.1 3911 0.02 0.7 818 122,244 0.9 2.5 0.1 3355 0.02 0.6 876 106980 - UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp(F) (lb/hr) 1.4 2.5 0.1 5177 0.02 0.9 736 156,668 1.2 2.5 0.1 4635 0.02 0.8 810 136,464 1.0 2.5 0.1 3955 0.02 0.7 873 117366 --_, UHC voe voe ' CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr) 1.6 2.5 0.2 6100 0.02 1.0 779 164,995 1.5 2.5 0.2 5526 0.02 0.9 840 148,793 1.2 2.5 0.1 4503 0.02 0.8 873 127331 Page F-130 Attachment F. Air Quality Permit Application Review Documents SolarTurbines PIL 167 A Caterpillar Company , . Product lntormat1on Letter PURPOSE SoLoNOx Products: Emissions in Non-SoLoNOx Modes Leslie Witherspoon Solar Turbines Incorporated Solar's gas turbine dry low NOx emissions combustion systems, known as SoLoNOx™, have been developed to provide the lowest emissions possible during normal operating conditions. In order to optimize the performance of the turbine, the combustion and fuel systems are designed to reduce NOx, CO and unburned hydrocarbons (UHC) without penalizing stability or transient capabilities. At very low load and cold temperature extremes, the SoLoNOx system must be controlled differently in order to assure stable operation. The required adjustments to the turbine controls at these conditions cause emissions to increase. The purpose of this Product Information Letter is to provide emissions estimates, and in some cases warrantable emissions for NOx, CO and UHC, at off-design conditions. Historically, regulatory agencies have not required a specific emissions level to be met at low load or cold ambient operating conditions, but have asked what emissions levels are expected. The expected values are necessary to appropriately estimate emissions for annual emissions inventory purposes and for New Source Review applicability determinations and permitting. COLD AMBIENT EMISSIONS ESTIMATES Solar's standard temperature range warranty for gas turbines with SoLoNOx combustion is ;:: 0 °F (-20°C). The Titan™ 250 is an exception, with a lower standard warranty at ;:: -20°F (-29°C). At ambient temperatures below 0°F, many of Solar's turbine engine models are controlled to increase pilot fuel to improve flame stability and emissions are higher. Without the increase in pilot fuel at temperatures below 0°F the engines may exhibit combustor rumble, as operation may be near the lean stability limit. If a cold ambient emissions warranty is requested, a new production turbine configured with the latest combustion hardware is required. For most models this refers to the inclusion of Cold Ambient Fuel Control Logic. Emissions warranties are not offered for ambient temperatures below -20 °F (-29 °C). In addition, cold ambient emissions warranties cannot be offered for the Centaur® 40 turbine. Table 1 provides expected and warrantable (upon Solar's documented approval) emissions levels for Solar's SoLoNOx combustion turbines. All emissions levels are in ppm at 15% 02• Refer to Product Information Letter 205 for Mercury™ 50 turbine emissions estimates. For information on the availability and approvals for cold ambient temperature emissions warranties, please contact Solar's sales representatives. PIL 167 Revision 4 1 6 June 2012 © 2012 Solar Turbines Incorporated Page F-131 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Product Information Letter 167 Table 2 summarizes "expected" emissions levels for ambient temperatures below 0°F (-20°C) for Solar's SoLoNOx turbines that do not have current production hardware or for new production hardware that is not equipped with the cold ambient fuel control logic. The emissions levels are extrapolated from San Diego factory tests and may vary at extreme temperatures and as a result of variations in other parameters, such as fuel composition, fuel quality, etc. For more conservative NOx emissions estimate for new equipment, customers can refer to the New Source Performance Standard (NSPS) 40CFR60, subpart KKKK, where the allowable NOx emissions level for ambient temperatures < 0°F (-20°F) is 150 ppm NOx at 15% 02. For pre-February 18, 2005, SoLoNOx combustion turbines subject to 40CFR60 subpart GG, a conservative estimate is the appropriate subpart GG emissions level. Subpart GG levels range from 150 to 214 ppm NOx at 15% 02 depending on the turbine model. Table 3 summarizes emissions levels for ambient temperatures below -20°F (-29 °C) for the Titan 250. Table 1. Warrantable Emissions Between 0°F and -20°F (-20° to -29°CJ for New Production Turbine Fuel System Fuel Applicable NOx, CO, Model Load ppm ppm Gas Only Gas 50 to 100% load 42 100 Centaur50 Dual Fuel Gas 50 to 100% load 72 100 Taurus™ 60 Gas Only or Dual Fuel Gas 50 to 100% load 42 100 Taurus65 Gas Only Gas 50 to 100% load 42 100 Taurus70 Gas Only or Dual Fuel Gas 50 to 100% load 42 100 Mars9 90 Gas Only Gas 50 to 100% load 42 100 Mars 100 Gas Only or Dual Fuel Gas 50 to 100% load 42 100 Titan 130 Gas Only or Dual Fuel Gas 50 to 100% load 42 100 Gas Only Gas 40 to 100% load 25 50 Titan 250 Gas Only Gas 40 to 100% load 15 25 Centaur50 Dual Fuel Liquid 65 to 100% load 120 150 Taurus 60 Dual Fuel Liquid 65 to 100% load 120 150 Taurus70 Dual Fuel Liquid 65 to 100% load 120 150 Mars 100 Dual Fuel Liquid 65 to 100% load 120 150 Titan 130 Dual Fuel Liquid 65 to 100% load 120 150 PIL 167 Revision 4 2 © 2012 Solar Turbines Incorporated UHC, ppm 50 50 50 50 50 50 50 50 25 25 75 75 75 75 75 6 June 2012 Page F-132 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Product Information Letter 167 Table 2. Expected Emissions below 0°F (-20 °C) for SoLoNOx Combustion Turbines Turbine Fuel System Fuel Applicable NOx, co, Model Load ppm ppm Centaur40 Gas Only or Dual Fuel Gas 80 to 100% load 120 150 Gas Only Gas 50 to 1 00% load 120 150 Centaur50 Dual Fuel Gas 50 to 100% load 120 150 Taurus60 Gas Only or Dual Fuel Gas 50 to 100% load 120 150 Taurus65 Gas Only Gas 50 to 100% load 120 150 Taurus 70 Gas Only or Dual Fuel Gas 50 to 100% load 120 150 Mars 90 Gas Only Gas 80 to 100% load 120 150 Mars 100 Gas Only or Dual Fuel Gas 50 to 100% load 120 150 Titan 130 Gas Only or Dual Fuel Gas 50 to 100% load 120 150 Centaur40 Dual Fuel Liquid 80 to 100% load 120 150 Centaur50 Dual Fuel Liquid 65 to 100% load 120 150 Taurus60 Dual Fuel Liquid 65 to 100% load 120 150 Taurus 70 Dual Fuel Liquid 65 to 100% load 120 150 Mars 100 Dual Fuel Liquid 65 to 100% load 120 150 Titan 130 Dual Fuel Liquid 65 to 100% load 120 150 UHC, ppm 50 50 50 50 50 50 50 50 50 75 75 75 75 75 75 Table 3. Expected Emissions below-20°F (-29 °C) for the Titan 250 SoLoNOx Combustion Turbine Turbine Fuel System Fuel Applicable NOx, co, UHC, Model Load ppm ppm ppm Titan 250 Gas Only Gas 40 to 100% load 70 150 50 COLD AMBIENT PERMITTING STRATEGY There are several permitting options to consider when permitting in cold ambient climates. Customers can use a tiered permitting approach or choose to permit a single emission rate over all temperatures. Historically, most construction and operating permits were silent on the ambient temperature boundaries for SoLoNOx operation. Some customers have used a tiered permitting strategy. For purposes of compliance and annual emissions inventories, a digital thermometer is installed to record ambient temperature. The amount of time is recorded that the ambient temperature falls below 0°F. The amount of time below 0°F is then used with the emissions estimates shown in Tables 1 and 2 to estimate "actual" emissions during sub-zero operation. A conservative alternative to using the NOx values in Tables 1, 2 and 3 is to reference 40CFR60 subpart KKKK, which allows 150 ppm NOx at 15% 02 for sub-zero operation. For customers who wish to permit at a single emission rate over all ambient temperatures, inlet air heating can be used to raise the engine inlet air temperature (T1 ) above 0°F. With inlet air heating to keep T 1 above 0 °F, standard emission warranty levels may be offered. Inlet air heating technology options include an electric resistance heater, an inlet air to exhaust heat exchanger and a glycol heat exchanger. If an emissions warranty is desired and ambient temperatures are commonly below -20°F (-29 °C}, inlet air heating can be used to raise the turbine inlet temperature (T1 ) to at least -20 °F. In such cases, the values shown in Table 1 can be warranted for new production. PIL 167 Revision 4 3 6 June 2012 © 2012 Solar Turbines Incorporated Page F-133 Attachment F. Air Quality Permit Application Review Documents • • Solar Turbines Incorporated Product Information Letter 167 EMISSIONS ESTIMATES IN NON-SOLONOX MODE (LOW LOAD) At operating loads< 50% {<40% load for the Titan 250) on natural gas fuel and < 65% {< 80% load for Centaur 40) on liquid fuels, SoLoNOx engines are controlled to increase stability and transient response capability. The control steps that are required affect emissions in two ways: 1) pilot fuel flow is increased, increasing NOx emissions, and 2) airflow through the combustor is increased, increasing CO emissions. Note that the load levels are approximate. Engine controls are triggered either by power output for single­ shaft engines or gas producer speed for two-shaft engines. A conservative method for estimating emissions of NOx at low loads is to use the applicable NSPS: 40CFR60 subpart GG or KKKK. For projects that commence construction after February 18, 2005, subpart KKKK is the applicable NSPS and contains a NOx level of 150 ppm @ 15% 02 for operating loads less than 75%. Table 4 provides estimates of NOx, CO, and UHC emissions when operating in non­ SoLoNOx mode for natural gas or liquid fuel. The estimated emissions can be assumed to vary linearly as load is decreased from just below 50% load for natural gas (or 65% load for liquid fuel) to idle. The estimates in Table 4 apply for any product for gas only or dual fuel systems using pipeline quality natural gas. Refer to Product Information Letter 205 for Mercury 50 emissions estimates. Table 4. Estimated Emissions in non-SoLoNOx Mode Ambient Fuel System Engine Load NOx, ppm CO, ppm Centaur 40150, Taurus 60/65no, Mars 90/100, Titan 130 <': -20°F (-29°C) Less than 50% 70 Natural Gas Idle 50 < -20°F (-29°C)Less than 50% 120 Natural Gas Idle 120 Titan 250 <': -20°F (-29°C) Less than 40% 50 Natural Gas Idle 50 Less than 40% 70 < -20°F (-29°C)Natural Gas Idle 70 Centaur 50, Taurus sono, Mars 100, Titan 130 <': -20°F (-29°C) < -20°F (-29°C) <': -20°F (-29°C) < -20°F (-29°C) Solar Turbines Incorporated 9330 Sky Park Court San Diego, CA 92123-5398 Liquid Liquid Liquid Liquid Caterpillar is a registered trademark of Caterpillar Inc. Less than 65% 120 Idle 120 Less than 65% 120 Idle 120 Centaur40 Less than 80% 120 Idle 120 Less than 80% 120 Idle 120 8,000 10,000 8,000 10,000 25 2,000 150 2,000 1,000 10,000 1,000 10,000 1,000 10,000 1,000 10,000 UHC, ppm 800 1,000 800 1,000 20 200 50 200 100 - 3,000 150 3,000 100 3,000 150 3,000 Solar, Titan, Mercury, Mars, Centaur and SoloNOx are trademarks of Solar Turbines Incorporated. Specifications subject to change without notice. Printed in U.S.A. PIL 167 Revision 4 4 6 June 2012 © 2012 Solar Turbines Incorporated Page F-134 Attachment F. Air Quality Permit Application Review Documents SolarTurhines PIL 168 A Caterpillar Company Pro duct Inrormation Letter Volatile Organic Compound, Sulfur Dioxide, and Formaldehyde Emission Estimates Leslie Witherspoon Solar Turbines Incorporated PURPOSE This Product Information Letter summarizes me­ thods that are available to estimate emissions of volatile organic compounds (VOe), sulfur dio­ xide (SO 2), and formaldehyde from gas turbines. Emissions estimates of these pollutants are of­ ten necessary during the air permitting process. INTRODUCTION In absence of site-specific or representative source test data, Solar refers customers to a United States Environmental Protection Agency (EPA) document titled "AP-42" or other appro­ priate EPA reference documents. AP-42 is a collection of emission factors for different emis­ sion sources. The emission factors found in AP- 42 provide a generally accepted way of estimat­ ing emissions when more representative data are not available. The most recent version of AP-42 (dated April 2000) can be found at: http://www.epa.gov/ttn/chief/ap42/ch03/index.html Solar does not typically warranty the emission rates for voe, SO 2 or formaldehyde. Volatile Organic Compounds Many permitting agencies require gas turbine users to estimate emissions of voe, a subpart of the unburned hydrocarbon (UHe) emissions, during the air permitting process. Volatile organ­ ic compounds, non-methane hydrocarbons (NMHC), and reactive organic gases (ROG) are some of the many ways of referring to the non­ methane (and non-ethane) portion of an "un­ burned hydrocarbon" emission estimate. For natural gas fuel, Solar's customers use 10- 20% of the UHC emission rate to represent voe PIL 168, Rev 4 Caterpillar: Confidential Green emissions. The estimate of 10-20% is based on a ratio of total non-methane hydrocarbons to total organic compounds. The use of 10-20% provides a conservative estimate of voe emis­ sions. The balance of the UHe is assumed to be primarily methane. For liquid fuel, it is appropriate to estimate that 100% of the UHe emission estimate is voe. Sulfur Dioxide Sulfur dioxide emissions are produced by con­ version of sulfur in the fuel to SO 2• Since Solar does not control the amount of sulfur in the fuel, we are unable to predict SO 2 emissions without a site fuel composition analysis. Customers generally estimate SO2 emissions with a mass balance calculation by assuming that any sulfur in the fuel will convert to SO2. For reference, the typical mass balance equation is shown below. Variables: wt % of sulfur in fuel Btu/lb fuel (LHV·) MMBtu/hr fuel flow (LHV) lb SO, =(wt%SulfurYib fuelx 106 Btu )(MMBtu fuel)( MW SO, ) hr JOO A Btu MMBtu hr MWSulfur As an alternative to the mass balance calcula­ tion, EPA's AP-42 document can be used. AP- 42 (Table 3.1-2a, April 2000) suggests emission factors of 0.0034 lb/MMBtu for gas fuel (HHV·) and 0.033 lb/MMBtu for liquid fuel (HHV). *LHV = Lower Heating Value; HHV = Higher Heating Value Formaldehyde In gas turbines, formaldehyde emissions are a result of incomplete combustion. Formaldehyde 14 May 2012 Page F-135 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated in the exhaust stream is unstable and very diffi­ cult to measure. In addition to turbine characte­ ristics including combustor design, size, main­ tenance history, and load profile, the formalde­ hyde emission level is also affected by: •Ambient temperature •Humidity •Atmospheric pressure •Fuel quality •Formaldehyde concentration in the ambient air •Test method measurement variability •Operational factors The emission factor data in Table 1 is an excerpt from an EPA memo: "Revised HAP Emission Product Information Letter 168 Factors for Stationary Combustion Turbines, 8/22/03." The memo presents hazardous air pol­ lutant (HAP) emission factor data in several cat­ egories including: mean, median, maximum, and minimum. The emission factors in the memo are a compilation of the HAP data EPA collected during the Maximum Achievable Con­ trol Technology (MACT) standard development process. The emission factor documentation shows there is a high degree of variability in formaldehyde emissions from gas turbines, de­ pending on the manufacturer, rating size of equipment, combustor design, and testing events. To estimate formaldehyde emissions from gas turbines, users should use the emis­ sion factor(s) that best represent the gas tur­ bines actual I planned operating profile. Refer to the memo for alternative emission factors. Table 1. EPA 's Total HAP and Formaldehyde Emission Factors for <50 MW Lean-Premix Gas Turbines burning Natural Gas {Source: Revised HAP Emission Factors for Stationary Combustion Turbines, OAR-2002-0060, IV-B-09, 8/22/03) Pollutant Engine Load Total HAP >90% Total HAP All Formaldehyde >90% Formaldehyde All Solar Turbines Incorporated 9330 Sky Park Court San Diego, CA 92123-5398 95% Upper Confidence of Mean, lb/MMBtu HHV 0.00144 0.00160 0.00127 0.00143 Caterpillar is a registered trademark of Caterpillar Inc. 95% Upper Confidence of Data, lb/MMBtu HHV 0.00258 0.00305 0.00241 0.00288 Solar is a trademark of Solar Turbines Incorporated. Specifications subject to change without notice. Printed in U.S.A. © 2008 Solar Turbines Incorporated. All rights reserved. PIL 168, Rev 4 2 Caterpillar: Confidential Green Memo Reference Table 19 Table 16 Table 19 Table 16 14 May 2012 Page F-136 Attachment F. Air Quality Permit Application Review Documents SolarTurbines PIL 170 A Caterpillar Company , . Product Inf orrnatton Letter Emission Estimates at Start-up, Shutdown, and Commissioning for SoLoNOx Combustion Products PURPOSE Leslie Witherspoon Solar Turbines Incorporated The purpose of this Product Information Letter (PIL) is to provide emission estimates for start-up and shutdown events for Solar® gas turbines with SoLoNOx ™ dry low emissions combustion systems. The commissioning process is also discussed. INTRODUCTION The information presented in this document is representative for both generator set (GS) and compressor set/mechanical drive (CS/MD) combustion turbine applications. Opera­ tion of duct burners and/or any add-on control equipment is not accounted for in the emissions estimates. Emissions related to the start-up, shutdown, and commissioning of combustion turbines will not be guaranteed or warranted. Combustion turbine start-up occurs in one of three modes: cold, warm, or hot. On large, utility size, combustion turbines, the start-up time varies by the "mode". The start-up dura­ tion for a hot, warm, or cold Solar turbine is less than 10 minutes in simple-cycle and most combined heat and power applications. Heat recovery steam generator (HRSG) steam pressure is usually 250 psig or less. At 250 psig or less, thermal stress within the HRSG is minimized and, therefore, firing ramp­ up is not limited. However, some combined heat and power plant applications will desire or dictate longer start-up times, therefore emissions assuming a 60-minute start are also estimated. A typical shutdown for a Solar turbine is <10 minutes. Emissions estimates for an elon­ gated shutdown, 30-minutes, are also included. Start-up and shutdown emissions estimates for the Mercury™ 50 engine are found in PIL 205. For start-up and shutdown emissions estimates for conventional combustion turbines, landfill gas, digester gas, or other alternative fuel applications, contact Solar's Environ­ mental Programs Department. START-UP SEQUENCE The start-up sequence, or getting to SoLoNOx combustion mode, takes three steps: 1.Purge-crank 2.Ignition and acceleration to idle 3.Loading / thermal stabilization During the "purge-crank" step, rotation of the turbine shaft is accomplished with a starter motor to remove any residual fuel gas in the engine flow path and exhaust. During "igni- PIL 170 Revision 5 1 13 June 2012 © 2012 Solar Turbines Incorporated Page F-137 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Product Information Letter 170 tion and acceleration to idle," fuel is introduced into the combustor and ignited in a diffu­ sion flame mode and the engine rotor is accelerated to idle speed. The third step consists of applying up to 50% load 1 while allowing the combustion flame to transition and stabilize. Once 50% load is achieved, the turbine transitions to SoLoNOx combustion mode and the engine control system begins to hold the combustion primary zone temperature and limit pilot fuel to achieve the targeted nitrogen oxides (NOx), car­ bon monoxide (CO), and unburned hydrocarbons (UHC) emission levels. Steps 2 and 3 are short-term transient conditions making up less than 10 minutes. SHUTDOWN PROCESS Normal, planned cool down/shutdown duration varies by engine model. The Centaur® 40, Centaur 50, Taurus ™ 60, and Taurus 65 engines take about 5 minutes. The Taurus 70, Mars® 90 and 100, Titan™ 130 and Titan 250 engines take about 10 minutes. Typically, once the shutdown process starts, the emissions will remain in SoLoNOx mode for ap­ proximately 90 seconds and move into a transitional mode for the balance of the esti­ mated shutdown time (assuming the unit was operating at full-load). START-UP AND SHUTDOWN EMISSIONS ESTIMATES Tables 1 through 5 summarize the estimated pounds of emissions per start-up and shut­ down event for each product. Emissions estimates are presented for both GS and CS/MD applications on both natural gas and liquid fuel (diesel #2). The emissions esti­ mates are calculated using empirical exhaust characteristics. COMMISSIONING EMISSIONS Commissioning generally takes place over a two-week period. Static testing, where no combustion occurs, usually requires one week and no emissions are expected. Dynamic testing, where combustion will occur, will see the engine start and shutdown a number of times and a variety of loads will be placed on the system. It is impossible to predict how long the turbine will run and in what combustion / emissions mode it will be running. The dynamic testing period is generally followed by one to two days of "tune-up" during which the turbine is running at various loads, most likely within low emissions mode (warranted emissions range). Solar Turbines Incorporated 9330 Sky Park Court San Diego, CA 92123-5398 Caterpillar is a registered trademark of Caterpillar Inc. Solar, Titan, Mars, Taurus, Mercury, Centaur, Saturn, SoLoNOx, and Turbotronic are trademarks of Solar Turbines Incorporated. All other trademarks are the intellectual property of their respective companies. Specifications are subject to change without notice. 1 40% load for the Titan 250 engine on natural gas. 65% load for all engines on liqui d fuel (except 80% load for the Centaur 40). PIL 170 Revision 5 2 13 June 2012 © 2012 Solar Turbines Incorporated Page F-138 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Table 1. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set Applications 10 Minute Start-up and 10 Minute Shutdown Natural Gas Fuel Data will NOT be warranted under any circumstances Centaur 40 4701 S Centaur 50 6201 S Taurus 60 7901S Taurus 65 8401 S NOx co UHC CO2 NOx co UHC llbsl llbsl llbsl llbsl llbsl llbsl llbsl I Total Emissions oar Start llbsl 0.6 58.1 3.3 35!1 0.8 75.0 4.3 CO2 NOx llbsl llbsl 454 0.8 co llbsl 78.5 UHC I CO2 llbsl llbsl 4.5 4ltl NOx co UHC llbsl llbsl llbsl 0.9 85.8 4.9 Product Information Letter 170 CO2 llbsl 523 Total Emissions per Shutdown flbsll o.JI 25.51 1.51 1&0! ul 31.11 1.81 194! ul 34.71 2.ol 211! ul 38.2! 2.21 ml Taurus 70 10801S Men 90 13002S GSC Mars 100 16002S GSC Titan 130 20501 S Titan 250 30002S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 llbsl llbsl llbsl llbsl llbsl llbsl l lbsl llbsl !lbs) llbsl llbsl l lb sl ll bs l llbsl llbsl llbsl llbsl llbsl llbsl llb sl Total Emissions per Start (lbsl 1.1 103.9 5.9 634 u 129.0 7.4 868 1.6 151.2 8.6 952 2.1 195.6 11.2 1,194 2.5 22.7 1.5 1,925 Total Emissions per Shutdown fibs)! 1.31 11o.1I 6.31 G?I 1.11 147.91 ul 91zj 1.91 166.81 9.51 1,0� 2.41 210.ol 12.ol 1,30� 3.ol 19.91 1.51 1,99� Assumes ISO conditions: 59F, 60% RH, sea level, no losses Assumes unit is operating at full load prior to shutdown. Assumes natural gas fuel; ES 9-98 compliant. PIL 170 Revision 5 © 2012 Solar Turbines Incorporated 3 13 June 2012 Page F-139 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Table 2.Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set Applications 60 Minute Start-up and 30 Minute Shutdown Natural Gas Fuel Data will NOT be warranted under any circumstances Centaur 40 4701 S Centaur 50 6201 S Taurus 60 7901S Taurus 65 8401 S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC (lbs) (lbs) {lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) Total Emissions Der Start libs 4.1 219.4 13.0 3,4711 5.0 m.4 16.1 4,219 5.7 299.8 17.8 4,780 6.1 326.5 19.3 Pr oduct Information Letter 170 CO2 !lbs) 5,074 Total Emissions per Shutdown (lbs' 1.81 121.1 7.11 1,44: 2.31 163.3 9.51 1, 2.51 163.5 9.61 1,994 2.61 177.21 10.41 2, 11 Taurus 70 10801S Mars 90 13002S NOx co UHC CO2 NOx (lbs) {lbsl llbsl libs) {lbs) I Total Emissions Der Start llbsl 7.6 410.3 24.2 6, 16A I Total Emissions Der Shutdown llbs 3.3 223.0 13.0 2.� Assumes ISO conditions: 59F, 60% RH, sea level, no losses. Assumes unit is operating at full load prior to shutdown. Assumes natural gas fuel; ES 9-98 compliant. PIL 170 Revision 5 © 2012 Solar Turbines Incorporated 10.5 4.3 co UHC {lbs) llbsl 570.8 33.7 277.0 16.2 CO2 llbsl 8,641 3,&M! 4 Mars 100 16002S Titan 130 20501 S Titan 250 30002S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 llbsl {lbs) {lbsl llbsl llbsl llbsl llbsl !lbs) llbsl llbsl llbsl llbsl 11.3 583.5 34.6 9,691 13.8 740.4 43.8 11,'95 14.6 75.5 7.3 16,253 4.8 308.1 18.0 4,056 6.0 405.3 23.7 4,826 6.2 52.6 4.1 7,222 13 June 2012 Page F-140 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Incorporated Table 3. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx CS/MD Applications 10 Minute Start-up and 10 Minute Shutdown Natural Gas Fuel Data will NOT be warranted under any circumstances Centaur 40 4702S Centaur 50 6102S Taurus 60 7802S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 llb&I llbsl llb&I llbsl llbal llbsl llbsl llbsl llbsl llbsl llbal llbsl I T DIDI Emissions per Start llbsl 0.7 64.4 3.7 391 0.8 69.1 4.0 .t6!I 0.7 64.3 3.7 41E Total Emissions per Shutdown (lbs)! 0.3� 1.11 m} 0.4� 2.0� 0.4� 1.91 ii Taurus 70 10302S Mars 90 13002S CSMD Mars 100 16002S CSMD Titan 130 20502S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC llbsl llbsl llbsl llbsl llbsl libs! llbsl """' llbsl llbal llbsl llbsl llbsl llbsl llbsl T DIDI Emissions oor Start fibs' 0.8 73.1 4.2 519 1.2 109.3 6.2 11111'1 1.4 123.5 7.1 a,11 1.9 176.9 10.1 Product Information Letter 170 Titan 250 30002S CO2 NOx co UHC CO2 llbsl llbsl llbsl llbsl llbsl 1,161 2.6 26.2 1.7 1,7<U Total Emissions per Shutdown (lbs)! 1.1� 5.31 57� 1.5� 7.61 a1il 1.7� 8.5� 2.41 201.&I 11.91 1.2nl 2.9� 1.4� Assumes ISO conditions: 59F, 60% RH, sea level, no losses. Assumes unit is operating at full load prior to shutdown. Assumes natural gas fuel; ES 9-98 compliant. PIL 170 Revision 5 © 2012 Solar Turbines Incorporated 5 13 June 2012 Page F-141 Attachment F. Air Quality Permit Application Review Documents Solar Turbines Inc orporated Table 4. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set 10 Minute Start-up and 10 Minute Shutdown Liquid Fuel (Diesel #2) Data will NOT be warranted under any circumstances Centaur 40 4701 S Centaur 50 6201S NOx co UHC CO2 NOx co UHC (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs) I Total Emissions per Start (lbsl 1.3 44.5 7.4 473 1.7 59.0 9.8 CO2 (lbs) 601 Total Emissions per Shutdown (lb 0.6 17.3 2.8 211 0.71 21.2 3.41 256 Taurus 70 10801S NOx co (lbs\ libs\ I Total Emissions per Start (lbs' 2.3 78.5 Total Emissions per Shutdown (lb 2.5 73.6 Assumes ISO conditions: 59F, 60% RH, sea level, no losses. Assumes unit is operating at full load prior to shutdown. Assumes #2 Diesel fuel; ES 9-98 compliant. PIL 170 Revision 5 © 2012 Solar Turbines Incorporated UHC libs\ 13.0 12.0 Mars 100 16002S GSC CO2 NOx co UHC CO2 libs\ libs\ libs\ libs\ (lbs\ 823 3.4 114.1 18.8 1,239 889 3.81 111.4 18.11 1 !331 6 Product Information Letter 170 Taurus 60 7901S NOx co UHC CO2 (lbs) (lbsl (lbsl (lbsl 1.7 59.8 9.9 636 0.81 23.5 3.81 286 Trtan 130 20501 S NOx co UHC CO2 (lbs) (lbs) (lbs) (lbs) 4.3 147.5 24.4 1,547 4.71 139.1 22.61 1 !6TT 13 June 2012 Page F-142 Attachment F. Air Quality Permit Application Review Documents • Solar Turbines Incorporated Table 5.Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set 60 Minute Start-up and 30 Minute Shutdown Liquid Fuel (Diesel #2) Data will NOT be warranted under any circumstances Centaur 40 4701S NOx co UHC CO2 (lbsl (lbsl (lbsl flbsl I Total Emissions ner Start fibs! 11.7 194.7 30.9 4,255 Total Emissions 1>er Shutdown (lbs 4.41 84.7 13.61 1,816 Taurus 70 10801S NOx co flbsl flbsl Total Emissions per Start (lbs) 18.4 360.3 Total Emissions per Shutdown (lbs 8.01 207.8 Assumes ISO conditions: 59F, 60% RH, sea level, no losses. Assumes unit is operating at full load prior to shutdown. Assumes #2 Diesel fuel; ES 9-98 compliant. PIL 170 Revision 5 © 2012 Solar Turbines Incorporated UHC CO2 fibs) flbsl 57.4 7,375 34.11 3,156 Centaur 50 6201 S NOx co UHC CO2 flbsl (lbsl fibs) flbsl 15.2 271.9 43.3 5,302 6.71 164.3 27.0I 2,334 Mars 100 16002S NOx co UHC CO2 flbsl flbsl flbsl flbsl 29.1 552.0 87.7 11,685 12.31 302.6 49.41 4,970 7 Product Information Letter 170 Taurus 60 7901S NOx co UHC CO2 (lbsl flbsl (lbsl (lbsl 14.7 282.6 45.0 5,962 6.31 159.0 26.0I 2,515 Titan 130 20501 S NOx co UHC CO2 flbsl flbsl flbsl (lbsl 34.4 6TT.0 108.0 13,731 15.0I 388.5 63.71 5,876 13 June 2012 Page F-143 Attachment F. Air Quality Permit Application Review Documents SCR CATALYST DESIGN DATASHEET -dSCR, °"""ea., CUstcrnetOesig\C&Se -- Fu,ICae a = 0 ·--- EXHAUST GAS EIIISSIOHS DATA (BEFORE COOUNG) Exhaust Gas Mass Aarnte, Wet "" &:lllust Gu Vchmdric Fbwate, Wet ACFM ExhsustGasT� _, l;Dl,§!Si9Corrmasiia, """"""'"' MW 02 31.999 "'"'""I H20 1!1.015 "'"'""I N2 29013 """IWOIJ CO2 44.010 """IWOIJ "' ""' """IWOIJ l;;!!!!!!!i!!!k5!!!1he�a @'1102 15 Rrinllca�*71"fflodiltrlmg,Nm3(dryj Na<aN02 -Na<aN02 "" co -co "" S02 -S02 "" S03 ..... S03 "" COOUNG AIR DATA. Cocmg A'I Mass Flc:wete, Wet "" CoailOArVob.lneiicFbN&e.\Yet ACFM ArnbienA'IT�in _, Relawel-kmility - EXHAUST GAS EIIISSIONS DATA WTEft 000LIHG) Exhaust Gm Mass FlcMrate, Wet "" ExhalstGmVdlmetricFkwnta,Wet ACFM -GaT ......... (""'"""'11 -F El!t!!!i!!! !i!J Ccmmn:n "'"-MW 02 31.999 "'"'""I H20 111.015 "'"'""I N2 28013 "'"'(Ml) CO2 44 010 """IWOIJ " "·"' """IWOIJ El!!!ll!lmm!lb� @'1102 ,. Rmenca�b"ppmKl•rrlmg.t,lmJ(dryJ NmasN02 -Na<aN02 "" co -co "" S02 -S02 "" S03 ""'""' S03 "" """"""" ,.,, Tta:eElements m,jNmJ(cty) voe - Amou"lt d Nm BS N02 ·--,.._ - OikllionAi'�Rd "" °"""""-SCFM A�Amrmria � "" -Ammon,-- T<Ul--bySCR "" Exhaust Ga Mass Ao.tnle, Wet et SCR catmysl: "" Exhsusl:GasValFbv.nlte,WdatSCR� ACFM �!!i!l!�!§ @'1102 15 Reh.retaappfcableb'ppmW•rrlmg,NmJ(dryJ Na<aN02 -NCllasN02 "" NH3Sip - NH3Sip "" AFCUSela:tD:! S021o503Ccnversion ...... Pressl.re�acrouthe-ri!20 0VTA•VM1ata� n.,,,;,,,AmbieriT� 100 ,� Ani:it.nl Ptes:sl.n ,., ""'° SleElevtuln 1500 ft 1r.-..... Ductf'ress1nt 2000 ""'° RdsNeHtmdty 60 - r-1 2 C-3 r ..... .,., ..... 5Dl ·-1""' "'"' NC NG NG , ..... 127C03 161184 .,,,. """ 117'! mo ano 171.0 1'78 1020 ,.., "' 1.15 055 JU3 "" '"' 241 2.27 a 0.91 , .. 0.1 un.oo 10000 too 2500 2500 ,oo '" 14' U5 50.00 5000 2500 .., 4.19 131 000 000 0.00 000 0.00 000 000 0.00 000 0.00 0.00 000 71111 2 278001 29270' 1311 6'311 5653 000 100.00 0.00 60.00 1>100 1>100 172175 155203 190455 ..... 60838 ..... 750.00 T5000 75000 1099 16.15 1013 ... 7.30 ,n 7UJ 1111 T921 231 111 2'3 0.91 ... 0.91 10000 !OOCCI 10000 2500 2508 9.00 ... , .. 195 5000 Sl.13 2500 . ., '19 131 0.00 000 000 0.00 0.00 000 000 000 000 000 000 000 000 000 000 000 0.00 000 000 0.00 000 50 50 50 8000 0)00 ..... 327 327 327 " .. .. 11 •8 10'8 m ... l3I 335 333 1725111 1555312 190717 1 l9013 81113 91558 .. .. .. 083 ... 1.09 10.IXJ 1003 1000 069 051 DID ACIEL15 AOEl.15 AOEtlS VTA VTA VTA VTA VTA VTA AFCU UESIGtl c.., Cae! 5Dl TatrUS60 """ 1""' NG NG ,,, ... , ..... ... ,, 107807 10040 ..... .... 1450 1.21 .., no, ,.,, . ., 3.00 011 Q.91 10000 100.00 900 9.00 "' 231 2500 2500 263 "' 000 0.00 0.00 ODO 000 0.00 000 ODO 514'0 311705.3 1Dl3 "" 10000 0.00 6000 60.00 114929 225515 96292 116559 T50.00 T50.00 15.95 1059 7.55 , ... 1315 T91' '" 250 ... 091 10000 10000 904 9.00 155 230 2511 2500 213 402 000 000 000 000 000 000 000 000 0.00 0.00 000 000 000 000 50 50 .... .... 327 321 .. " 5 1 '52 ,., 332 33' 1152606 2259195 "'85 116732 .. 50 ... 1.32 10.04 10.00 .... ... AOEL15 AOEl.15 VTA VTA VTA VTA 11001 %'NW """'' C-1 T ., T " 1""' '""' NG "' 151704 2•7255 ll6052 1,..,, ..... esao 1183 "" 9.3' . ., 12.96 "" 290 305 '·" '" 100.00 10000 9.00 9.00 "' 320 2500 2500 120 542 0.00 000 0.00 0.00 0.00 000 0.00 0.00 67013.0 4007 12 15511 mo 10000 000 60.00 IDOO 218717 217332 113920 1"553 T50.00 T5000 1062 ,.,. 7."7 rn 7161 1905 203 293 ... 091 100.00 10000 904 9.00 "' 320 2511 2500 120 542 000 ODO 0.00 000 0.00 000 0.00 0.00 0.00 0.00 0.00 000 000 000 50 50 ..... .... 327 327 .. .. ' 10 551 832 333 337 219049.7 287668 .9 114083 14!n7 !iO 50 UIS 111 10.04 1000 0.19 1.32 AQEL15 AOEltS VTA VTA VTA VTA r-• ea,, C...10 C..,11 C...12 TaLn.Gm Mn100 Mn100 Ti,n,:!) Tf.an1'.'li ,.,.. "'"' 100% 100% 100% .., NG NG NG NG 11182' 367228 289445 '31156 3'1228 112303 207183 1173&1 """ 215260 980.0 850.0 95l0 ""·' 0830 "" 14.73 1'-2:J 1440 1160 '·" 561 908 ... 9.55 �� T58! 1106 1015 n.8' 283 290 216 104 3.01 Q.A7 0.91 0.17 0.111 0.87 100.00 10000 100.00 HX:UXI 100.00 900 ,oo 9.00 900 9.00 226 '51 14' ... "' 2500 2500 2500 2500 2500 u, 1.62 511 , ... ,.., 000 0.00 000 000 ODO 000 0.00 000 0.00 0.00 000 0.00 000 000 0.00 000 0.00 000 0.00 0.00 133113 6001'6 104237.S 985939 147099.4 16091 11601 241:Jil 1 .... 3'064 100.0D 000 100.00 000 100.00 1>100 6000 1>1.00 60.00 1>100 253191 '27.113 3'l663 536550 '81325 131945 220785 205195 2mc ,..... 15000 T5000 T50.00 T5000 T5000 100I 1559 15.78 1059 1062 719 ... 1.10 '" 1.14 1155 76.15 ll!III 76.16 "" 210 250 204 24' 212 ... 0.91 ... 0.91 ... 100.00 100.00 10000 100.00 10000 904 900 903 900 9.04 226 '51 14' ... ,., 2510 2500 2509 2500 25.11 113 1.62 511 9.51 1.4' 000 000 000 000 ODO 0.00 0.00 000 0.00 000 0.00 0.00 000 000 000 000 0.00 000 000 000 000 0.00 0.00 000 0.00 000 000 0.00 0.00 0.00 000 ODO 0.00 0.00 000 50 50 50 50 50 ..... .... .... .... .... 327 327 321 327 327 .. .. .. .. .. 1 " 10 11 13 659 1311 1000 18'8 1289 l3' 3'1 337 "' 340 253531 1 427643.2 3040200 536894.1 ....... 132119 220962 205311 277421 2548'2 !iO !iO 5.0 .. 50 126 250 191 115 "' 10.04 10.00 10.04 10.IXI 1004 0.83 185 1'1 233 U2 AQEL15 AOEl.15 AOEL15 AOEL15 AOELIS VTA VTA VTA VTA VTA VTA VTA VTA VTA VTA Page F-144 Attachment F. Air Quality Permit Application Review Documents C G3516 GAS ENGINE TECHNICAL DATA ENGINE SPEED (rpm): OMPRESSION RATIO: FTERCOOLER TYPE: :-\FTERCOOLER WATER INLET ('F): JACKET WATER OUTLET ('F): ASPIRATION: COOLING SYSTEM: CONTROL SYSTEM: EXHAUST MANIFOLD: COMBUSTION: NOx EMISSION LEVEL (g/bhp-hr NOx): GENSET POWER GENSET POWER ENGINE POWER GENERATOR EFFICIENCY RATING GENSET EFFICIENCY(@ 1.0 Power Factor) THERMAL EFFICIENCY TOTAL EFFICIENCY (@ 1.0 Power Factor) 1800 11:1 SCAC 130 210 TA JW+OC,AC EIS ASWC Low Emission 2.0 ENGINE DATA GENSET FUEL CONSUMPTION GENSET FUEL CONSUMPTION ENGINE FUEL CONSUMPTION AIR FLOW (77'F, 14.7 psia) AIR FLOW FUEL FLOW (60°F, 14.7 psia) COMPRESSOR OUT PRESSURE COMPRESSOR OUT TEMPERATURE AFTERCOOLER AIR OUT TEMPERATURE INLET MAN. PRESSURE INLET MAN. TEMPERATURE TIMING EXHAUST TEMPERATURE -ENGINE OUTLET EXHAUST GAS FLOW (@engine outlet temp, 14.5 psia) EXHAUST GAS MASS FLOW EMISSIONS DATA -ENGINE OUT NOx (as NO2) co THC (mol. wt. of 15.84) NMHC (mol. wt. of 15.84) NMNEHC (VOCs) (mol. wt. of 15.84) HCHO (Formaldehyde) CO2 EXHAUST OXYGEN LAMBDA ENERGY BALANCE DATA LHV INPUT HEAT REJECTION TO JACKET WATER (JW) HEAT REJECTION TO ATMOSPHERE HEAT REJECTION TO LUBE OIL (OC) HEAT REJECTION TO EXHAUST (LHV TO 77'F) HEAT REJECTION TO EXHAUST (LHV TO 248'F) HEAT REJECTION TO AFTERCOOLER (AC) PUMP POWER CONDITIONS AND DEFINITIONS RATING STRATEGY: APPLICATION: RATING LEVEL: FUEL: FUEL SYSTEM: FUEL PRESSURE RANGE(psig): FUEL METHANE NUMBER: FUEL LHV (Btu/sci): ALTITUDE CAPABILITY AT 77'F INLET AIR TEMP. (fl): POWER FACTOR: VOLTAGE(V): NOTES LOAD 100% (WITHOUT FAN (1)(2) ekW 1000 (1)(2) kVA 1250 (WITHOUT FAN (2) bhp 1416 (1) % 94.7 (ISO 3046/1 (3) % 31.7 (4) % 52.4 (5) % 84.1 (ISO 3046/1 (6) Btu/ekW-hr 10917 (NOMINAL (6) Btu/ekW-hr 11128 (NOMINAL (6) Btu/bhp-hr 7859 (WET (7) (8) fl3/min 2988 (WET (7) (8) lb/hr 13248 scfm 205 in Hg(abs) 70.1 'F 309 'F 134 (9) in Hg(abs) 62.6 (MEASURED IN PLENUM (10) 'F 138 (11) 'BTDC 18 (12) 'F 876 (WET (13) (8) fl3/min 8086 (WET (13) (8) lb/hr 13810 (14)(15) g/bhp-hr 2.00 (14)(16) g/bhp-hr 1.89 (14)(16) g/bhp-hr 2.36 (14)(16) g/bhp-hr 0.35 (14)(16)(17) g/bhp-hr 0.24 (14)(16) g/bhp-hr 0.28 (14)(16) g/bhp-hr 499 (14)(18) %DRY 7.5 (14)(18) 1.49 (19) Btu/min 185475 (20)(27) Btu/min 49148 (21) Btu/min 6831 (22)(27) Btu/min 8040 (23)(24) Btu/min 51104 (23) Btu/min 39125 (25)(28) Btu/min 9329 (26) Btu/min 971 CATERPILLAR. STANDARD Gensel STANDBY Nat Gas LPG IMPCO WITH AIR FUEL RATIO CONTROL 1.5-5.0 85 905 3501 0.8 240-480 75% 50% 750 500 937 625 1059 707 95.0 94.8 30.5 28.1 54.7 58.6 85.2 86.7 11314 12254 11533 12492 8170 8831 2240 1522 9934 6747 159 115 60.4 47.0 269 201 131 131 48.5 34.9 135 134 18 18 873 879 6062 4155 10371 7063 2.00 2.00 1.90 1.95 2.47 2.82 0.37 0.42 0.25 0.28 0.28 0.28 507 525 7.2 6.9 1.43 1.35 144166 104103 41900 34467 5682 4553 6854 5638 38351 26562 29274 20234 5510 1919 971 971 Engine rating obtained and presented in accordance with ISO 3046/1. (Standard reference conditions of 77'F, 29.60 in Hg barometric pressure.) No overload permitted at rating shown. Consult the altitude deration factor chart for applications that exceed the rated attitude or temperature. Emission levels are at engine exhaust flange prior to any after treatment. Values are based on engine operating at steady state conditions, adjusted to the specified NOx level at 100% load. Tolerances specified are dependent upon fuel quallty. Fuel methane number cannot vary more than ± 3. For notes information consult page three. Data generated by Data Maintenance Utillty Version 3.02.34 Ref. Data Set EM0749-00-001, Printed 13Nov2013 Page 1 of 4 Page F-145 Attachment F. Air Quality Permit Application Review Documents G3516 GAS ENGINE TECHNICAL DATA C FUEL USAGE GUIDE I CAT METHANE NUMBER 30 35 40 SET POINT TIMING --- DERATION FACTOR 0 0 0 ALTITUDE DERATION FACTORS AT RATED SPEED I 130 1 1 0.99 0.96 120 1 1 1 0.97 INLET 110 1 1 1 0.99 AIR 100 1 1 1 1 TEMP 90 1 1 1 1 "F 80 1 1 1 1 70 1 1 1 1 60 1 1 1 1 50 1 1 1 1 0 1000 2000 3000 AFTERCOOLER HEAT REJECTION FACTORS (ACHRFI 130 1.40 1.46 1.54 120 1.32 1.38 1.45 INLET 110 1.23 1.30 1.37 AIR 100 1.15 1.22 1.29 TEMP 90 1.07 1.14 1.20 "F 80 1 1.06 1.12 70 1 1 1.04 60 1 1 1 I 50 1 1 1 0 1000 2000 Data generated by Data Maintenance Utility Version 3.02.34 Ref. Data Set EM0749-00-001, Printed 13Nov2013 1.61 1.52 1.44 1.35 1.27 1.19 1.10 1.02 1 3000 I 45 50 55 60 65 ----- 0 0 0 0 0 0.92 0.89 0.85 0.82 0.79 0.94 0.90 0.87 0.83 0.80 0.95 0.92 0.88 0.85 0.81 0.97 0.93 0.90 0.86 0.83 0.99 0.95 0.91 0.88 0.84 1 0.97 0.93 0.89 0.86 1 0.99 0.95 0.91 0.88 1 1 0.97 0.93 0.89 1 1 0.99 0.95 0.91 4000 5000 6000 7000 8000 ALTITUDE (FEET ABOVE SEA LEVEL) 1.68 1.70 1.70 1.70 1.70 1.59 1.62 1.62 1.62 1.62 1.51 1.53 1.53 1.53 1.53 1.42 1.44 1.44 1.44 1.44 1.34 1.36 1.36 1.36 1.36 1.25 1.27 1.27 1.27 1.27 1.17 1.19 1.19 1.19 1.19 1.08 1.10 1.10 1.10 1.10 1 1.02 1.02 1.02 1.02 4000 5000 6000 7000 8000 ALTITUDE (FEET ABOVE SEA LEVEL) CATERPILLAR. 70 75 80 85 15 16 17 18 1 1 1 1 0.76 0.73 0.70 0.67 0.77 0.74 0.71 0.68 0.78 0.75 0.72 0.69 0.80 0.76 0.73 0.70 0.81 0.78 0.75 0.72 0.83 0.79 0.76 0.73 0.84 0.81 0.78 0.74 0.86 0.82 0.79 0.76 0.87 0.84 0.81 0.77 9000 10000 11000 12000 1.70 1.70 1.70 1.70 1.62 1.62 1.62 1.62 1.53 1.53 1.53 1.53 1.44 1.44 1.44 1.44 1.36 1.36 1.36 1.36 1.27 1.27 1.27 1.27 1.19 1.19 1.19 1.19 1.10 1.10 1.10 1.10 1.02 1.02 1.02 1.02 9000 10000 11000 12000 Page 2 of 4 Page F-146 Attachment F. Air Quality Permit Application Review Documents G3516 GAS ENGINE TECHNICAL DATA CATERPILLAR• is table shows the derate factor and full load set point timing required for a given fuel. Note that deration and set point timing reduction may be required as the methane number ecreases. Methane number is a scale to measure detonation characteristics of various fuels. The methane number of a fuel is determined by using the Caterpillar methane number calculation program. ALTITUDE DERA TION FACTORS: This table shows the deration required for various air inlet temperatures and altltudes. Use this information along with the fuel usage guide chart to help determine actual engine power for your site. ACTUAL ENGINE RATING: To determine the actual rating of the engine at site conditions, one must consider separately, !imitations due to fuel characteristics and air system limitations. The Fuel Usage Guide deration establishes fuel limitations. The Altltude/Temperature deration factors and RPC (reference the Caterpillar Methane Program) establish air system �mitations. RPC comes into play when the Altitude/Temperature deration is less than 1.0 (100%). Under this condition, add the two factors together. When the site conditions do not require an Altltude/ Temperature derate (factor is 1.0), ii is assumed the turbocharger has sufficient capabiHty to overcome the low fuel relative power, and RPC is ignored. To determine the actual power available, take the lowest rating between 1) and 2). 1) Fuel Usage Guide Deratlon 2) 1-((1-Altltude/Temperature Deration) + (1-RPC)) AFTERCOOLER HEAT REJECTION FACTORS(ACHRF): To maintain a constant air inlet manifold temperature, as the inlet air temperature goes up, so must the heat rejection. As altitude increases, the turbocharger must work harder to overcome the lower atmospheric pressure. This increases the amount of heat that must be removed from the inlet air by the aftercooler. Use the aftercooler heat rejection factor (ACHRF) to adjust for Inlet air temp and altitude conditions. See note 28 for application of this factor in calculating the heat exchanger sizing criteria. Failure to properly account for these factors could result in detonation and cause the engine to shutdown or fail. NOTES: �or efficiencies, power factor, and voltage are based on standard generator. [Gensel Power (ekW) is calculated as: Engine Power (bkW) x Generator Efficiency), [Gensel Power (kVA) is calculated as: Engine Power (bkW) x Generator Efficiency / Power Factor) 2. Rating is with two engine driven water pumps. Tolerance is (+)3, (-)0% of full load. 3. ISO 3046/1 Gensel efficiency tolerance is (+)0, (-)5% of full load % efficiency value based on a 1.0 power factor. 4. Thermal Efficiency is calculated based on energy recovery from the jacket water, lube oil, and exhaust to 248°F with engine operation at ISO 3046/1 Gensel Efficiency, and assumes unburned fuel Is converted in an oxidation catalyst. 5. Total efficiency is calculated as: Gensel Efficiency + Thermal Efficiency. Tolerance is ±10% of full load data, 6. ISO 3046/1 Gensel fuel consumption tolerance Is (+)5, (-)0% of full load data. Nominal genset and engine fuel consumption tolerance is :I: 3.0% of full load data. 7. Air flow value is on a 'wet' basis. Flow is a nominal vaue with a tolerance of :1: 5 %. 8. Inlet and Exhaust Restrictions must not exceed A&l limlts based on full load flow rates from the standard technical data sheet. 9. Inlet manifold pressure is a nominal value with a tolerance of :1: 5 %. 10. Inlet manifold temperature is a nominal value with a tolerance of :I: 9"F. 11. Timing Indicated is for use with the minimum fuel methane number specified. Consult the appropriate fuel usage guide for timing at other methane numbers. 12. Exhaust temperature is a nominal value with a tolerance of (+)63"F, (-)54"F. 13. Exhaust flow value is on a 'wet' basis. Flow Is a nominal value with a tolerance of :1: 6 %. 14. Emissions data Is at engine exhaust flange prior to any after treatment. 15. NOx tolerances are :1: 18% of specified value. 16. CO, CO2, THC, NMHC, NMNEHC, and HCHO values are "Not to Exceed" levels. THC, NMHC, and NMNEHC do not include aldehydes. An oxidation catalyst may be required to eel Federal, State or local CO or HC requirements. 7. voes -Volatile organic compounds as defined in US EPA 40 CFR 60, subpart JJJJ 18.Exhaust Oxygen tolerance is :1: 0.5; Lambda tolerance is :1: 0.05. Lambda and Exhaust Oxygen level are the result of adjusting the engine to operate at the specified NOx level. 19. LHV rate tolerance is :1: 3.0%. 20. Heat rejection to jacket water value displayed includes heat to jacket water alone. Value is based on treated water. Tolerance is :I: 10% of full load data. 21. Heat rejection to atmosphere based on treated water. Tolerance is :I: 50% of full load data. 22. Lube all heat rate based on treated water. Tolerance is :I: 20% of full load data. 23. Exhaust heat rate based on treated water. Tolerance is :I: 10% of full load data. 24. Heat rejection to exhaust (LHV to 77"F) value shown includes unburned fuel and Is not Intended to be used for sizing or recovery calculations. 25. Heat rejection to aftercooler based on treated water. Tolerance is :1:5% of ful load data. 26. Pump power includes engine driven jacket water and aftercooler water pumps. Engine brake power includes effects of pump power. 27. Total Jacket Water Circuit heat rejection Is calculated as: (JW x 1.1) + (OC x 1.2). Heat exchanger sizing criterion is maximum circuit heat rejection at site conditions, with applied tolerances. A cooling system safety factor may be multiplied by the total circuit heat rejection to provide addltional margin. 28. Total Aftercooler Circuit heat rejection is calculated as: AC x ACHRF x 1.05. Heat exchanger sizing criterion is maximum circuit heat rejection at site conditions, with applied tolerances. A cooling system safety factor may be multiplied by the total circuit heat rejection to provide additional margin . • Data generated by Data Maintenance Utility Version 3.02.34 Ref. Data Set EM07 49-00-001, Printed 13Nov2013 Page 3 of 4 Page F-147 Attachment F. Air Quality Permit Application Review Documents G3516 ENGINE POWER (bhp): NGINE SPEED (rpm): HAUST MANIFOLD: 1416 1800 ASWC GAS ENGINE TECHNICAL DATA COOLING SYSTEM: AFTERCOOLER WATER INLET (°F): JA CKET WATER OUTLET (°F): Free Field Mechanical and Exhaust Noise SOUND PRESSURE LEVEL (dB) Octave Band Center Frequency (OBCF) 100% Load Data dB(A) 63 Hz 125 Hz 250 Hz 500 Hz 1 kHz 2 kHz 4 kHz Mechanical Distance from 3.3 100 95 96.6 92.8 94 96.1 93.3 90.1 Sound the Engine (ft) 23.0 90.4 85.4 87 83.2 84.4 86.5 83.7 80.5 49.2 85.1 80.1 81.7 77.9 79.1 81.2 78.4 75.2 Exhaust Sound Distance from 4.9 115.4 104.7 105.7 112.4 110.6 108.3 108.2 108 the Engine (ft) 23.0 102 92.4 95.4 100.2 96.7 95.4 94.7 94.6 49.2 95.4 85.8 88.8 93.6 90 88.8 88.1 87.9 SOUND PARAMETER DEFINITION: Data Variability Statement: 8 kHz 84.4 74.8 69.5 106.1 91.8 85.2 CATERPILLAR. JW+OC,AC 130 210 Sound data presented by Caterpillar has been measured in accordance with ISO 6798 in a Grade 3 test environment. Measurements made inaccordance with ISO 6798 will result in some amount of uncertainty. The uncertainties depend not only on the accuracies with which sound pressurelevels and measurement surface areas are determined, but also on the 'near-field error' which increases for smaller measurement distances and lowerfrequencies. The uncertainty for a Grade 3 test environment, that has a source that produces sounds that are uniformly distributed in frequency over thefrequency range of interest, is equal to 4 dB (A-weighted). This uncertainty is expressed as the largest value of the standard deviation. Data generated by Data Maintenance Utilijy Version 3.02.34 Ref. Data Set EM0749-00-001, Printed 13Nov2013 Page 4 of 4 Page F-148 Attachment F. Air Quality Permit Application Review Documents APPENDIXE SECRET ARY OF STATE REGISTRATION • ERM ACP. LLC -NORTHAMPTON COMPRESSOR STATION Page F-149 Attachment F. Air Quality Permit Application Review Documents NORTH CAROLINA Department of the Secretary of State To all whom these presents shall come, Greetings: I, Elaine F. Marshall, Secretary of State of the State of North Carolina, do hereby certify the following and hereto attached to be a true copy of CERTIFICATE OF AUTHORITY OF ATLANTIC COAST PIPELINE, LLC the original of which was filed in this office on the 3rd day of November, 2014. •-� . . . . . I!] . . Scan to verify online. Certification# 97485708-1 Reference# 12733297-Page: 1 of7 Verify this certificate online at www.secretary.state.nc. us/verification IN WITNESS WHEREOF, I have hereunto set my hand and affixed my official seal at the City of Raleigh, this 9th day of September, 2015 . Secretary of State Page F-150 Attachment F. Air Quality Permit Application Review Documents State of Nortlt Carolina Department of tl,e Secretary of State SOSID: 1410169 Date Filed: 11/3/2014 10:30:00 AM Elaine F. Marshall North Carolina Secretary of State C2014 304 02235 APPLICATION FOR CERTIFICATE OF AUTHORITY FOR LIMITED LIABILITY COMPANY Pursuant to §57D-7-03 of the General Statutes of North Carolina, the undersigned limited liability company hereby applies for a Certificate of Authority to transact business in the State of North Carolina, and for that purpose submits the following: 1.The name of the limited liability company is Atlantic Coast Pipeline, LLC and if the limited liability company name is unavailable for use in the State ofNorth Carolina, the name the limited liability company wishes to use is _________________________ _ 2.The state or country under whose laws the limited liability company was fonncd is Delaware 3.Principal office information: (Select eilher a orb.) a.181 The limited liability company has a principal office. The principal office telephone number: _8_04-_8_19_-2_0_0_0 ________________ _ The street address and county of the principal office of the limited liability company is: Number and Street: 12 0 Tredegar Street City: Richmond State: VA Zip Code:._23_2 _1_9 ___ County: _______ _ The mailing address, If dljfere,rtfrom tl,e street address, of the principal office of the corporation is: Number and Street: __________________________ _ City: __________ State: __ Zip Code:. _____ County: ______ _ b.0 The limited liability company does not have a principal office. 4.The name of the registered agent in the State ofNorth Carolina is: _C_T_C _orpo�ra_t_io_n_S_y _ste_m ________ _ 5.The street address and county of the registered agent's office in the State of North Carolina is: Number nnd Street: 150 Fayetteville Street, Box IO 11 City: Raleigh State: NC Zip Code:_2 _7_60_1 ___ County: _W_ak_e ______ _ 6.The North Carolina mailing address, If diflere1,tfro11, tire slreet address, of the registered agent's office in the State of NorthCarolina is: Number and Street:. _____________________________ _ City:. _________ State: NC CORPORATIONS DMSION (Revised Jo11uo,,, 2014) IIC0S1 • ll/ll/101) Wol"1S Kl\lwtT011ll,.. Certification# 97485708-1 Reference# 12733297-Page: 2 of 7 Zip Code: _____ County: ________ _ P.O. BOX 29622 RALEIGH, NC 27626-0622 (Fon11L-09) Page F-151 Attachment F. Air Quality Permit Application Review Documents Directors/Officers Report Officers Mlchele L. Cardiff Vice President (Chief Accounting Officer) Primary Address 701 East Cary Street Richmond, Virginia 23219 G.Scott Hetzer Vice President and Treasurer Primary Add ress 100 Tredegar Street Richmond, Virginia 23219 Henry P Linginfelter Vice President Primary Address 120 Tredegar Street Richmond, Virginia 23219 Carter M. Reid Vice President and Secretary prima ry Address 100 Tredegar Street Richmond, Virginia 23219 D1ri,crc,f'S/Officnr:; Fl&po:1 BOE - v : GeMratad 11/0J/2014 Ii 30 t4AM Certification# 97485708-1 Reference# 12733297-Page: 3 of 7 As of November 03, 2014 Paqe 1 o/3 Page F-152 Attachment F. Air Quality Permit Application Review Documents Directors/Officers Report Karen W. Doggett Assistant Secretary Prim ary Address 100 Tredegar Street Richmond, Virginia 23219 John L. Newman Assistant Treasurer Primary Address 100 Tredegar Street Richmond, Virginia 23219 Managers Anne E. Bomar Manager & Vice President Primary Address 120 Tredegar Street Richmond, Virginia 23219 Phllllp C Grigsby Manager & Vice President Primary Address 120 Tredegar Street Richmond, Virginia 23219 D11e1t11(.,,'0flic1'rs ReCX!'I BOE, 1• I Gt,11,m)/i,d 11,iJ:112014 B·JO 15AM Ce1-tiflcation# 97485708-1 Reference# 12733297-Page: 4 of 7 As of November 03, 2014 PB(l(l2of3 Page F-153 Attachment F. Air Quality Permit Application Review Documents Directors/Officers Report Karl W Newlin Manager & Vice President Primary Address 120 Tredegar Street Richmond, Virginia 23219 n,r,�Jo,s:'Off,cr,,, Rep1>1t BOE "1 Ger>eraft'd t liO.J/2014 a·:10 75AM Certification# 97485708-1 Refe1·ence# 12733297-Page: 5 of7 As of November 03, 2014 Pari113af3 Page F-154 Attachment F. Air Quality Permit Application Review Documents APPLlCATION FOR CERTIFICATE OF AUTHORITY Pagel 7.The names, titles, and usual business addresses of the current company officials of the limited liability company are: (use allachme11t if necessary) Name and Title Business Address Anne E. Bomar, Manager & Vice President 120 Tredegar Street, Richmond, VA 232 l 9 Phillip C. Grigsby, Manager & Vice President 120 Tredegar Street, Richmond, VA 23219 Karl W. Newlin, Manager & Vice President 120 Tredegar Street, Richmond, VA 23219 Henry P. Linginfelter, Vice President 120 Tredegar Street, Richmond, VA 23219 See Attachment. K.Attached is a certificate of existence (or docwnent of similar import), duly authentic11ied by the secretary of state or other officialhaving custody oflimited liability company records in the stale or country of formation. The Certlflcate of E1lstcnce must be less than six months old. A photocopy of the certlOcatlon cannot be accepted. 9.lfthe limited liability company is required to use a fictitious name in order to transact business in this State, a copy of the resolutionof its managers adopting the fictitiou.,; name is attached. JO. (Optional): Please provide a business e-mail address:�IP_r.,:.iv;.:a;,;;c;.i;v..:R�e:;:d;;;a;;;c;,;ti�o,;.;n ______ __,1 __________ _ The Secretary of State's Office will e-mail the business automatically at the address provided above at no cost when a document is filed. The e-mail provided will not be viewable on the website. For more information on why this service is offered, please see the instructions for this document. I J. This application will be effective upon filing, unless a delayed date and/or time is specified: ___________ ....:.. This the _3_day of November Notes: 2014 ' - Atlantic Coast Pipeline, LLC Karen W. Doggett, Assistant Secretory Type or Print Name and Tille I.flllng fee Is 5250. This document must be filed with the Secretary of State. CORPORA TfONS DIVISION (Re.vised January 2014) N!'llll • l?llli?DI) Wollen KluwerOnfio, Certificntion# 97485708-1 Reference# 12733297-Pnge: 6 of 7 P.O. BOX 29622 RALEIGH, NC 27626-0622 (Form L-09) Page F-155 Attachment F. Air Quality Permit Application Review Documents 'lJefaware PAGE 1 'JJie, !first State I, JEFFREY W. BULLOCIC, SECRE!l'ARY OF S!Z'A!Z'E OF !Z'HE S!Z'A!l'E OF DELAW'ARB, DO HEREBY CER!Z'IFY "A!Z'LMnIC COAS7.' PIPELINE, LLC" IS DULY FORMED UNDER !Z'BE LA11S OF !Z'BE S!Z'A!Z'E OF DELAWARE AND IS IN GOOD S!'ANDING AND HAS A LEGAL EXISTENCE SO FAR AS !!'BE RECORDS OF !Z'BIS OFFICE SHOW, AS OF 7.'BE 'l'WENff-NIN!Z'H DAY OF OCTOBER, A.D. 2014. AND I DO HEREBY FURTHER CERTIFY TBA'l' TBE ANNUAL !l'AXES HAVE NOT BEEN ASSESSED !l'O DA!ZW. 5593371 8300 141346545 ��� DA!Z'E: 10-29-14 rou may verUy this cert:i�ic:a�e online .t: coq.delawue, gov/authver. shtml Certification# 97485708-1 Reference# 12733297-Page: 7 of7 Page F-156 Attachment F. Air Quality Permit Application Review Documents Page F-157Attachment F. Air Quality Permit Application Review Documents Dominion Energy Services, Inc. 5000 Dominion Boulevard Glen Allen, VA 23060 DominionEnergy.com July 20, 2017 BY: OVERNIGHT MAIL Mr. Charles McEachem � DominionP' Energy· � - '--0 .... ..., � C t:T1 Raleigh Regional Office NCDEQ Division of Air Quality Suite 101 ' .-., �-"'I o.:. 3800 Barrett Drive Raleigh, NC �!509 0 $:I) 'c5 RE: Atlantic Coast Pipeline, L.L.C. Northampton Compressor Station Air Permit Application Update Dear Mr. McEachem: -=::i0 s ('l Atlantic Coast Pipeline, LLC (ACP) is submitting updates to the Northampton Compressor Station permit application, dated September 16, 2015. The changes are to ancillary equipment including emergency generators and storage tanks. No changes are requested for the main natural gas compressors. The changes do not materially affect the applicable regulatory requirements. ACP is proposing the following updates: •Replace the Caterpillar G3516 emergency generator rated at 1,416 hp (EG-01) with a Caterpillar G3516B emergency generator rated at 1,818 hp; •Add a new Generac SG 100 emergency generator rated at 148.9 hp (EG-02) for the regional operations center; ('1) ::l � 0 c:: � •Replace the boiler rated at 6.3 MMBtu/hr (WH-01) with a Hurst LPW-G-125-60W boiler rated at 5.25 MMBtu/hr; •Decrease the volume of the proposed pipeline fluids tank (TK-2) from 1,500 gallons to 1,000 gallons; •Increase the volume of the proposed Ammonia Tank (TK-3) from 8,000 gallons to 13,400 gallons; and •Correct a calculation error that overestimated fugitive emissions. The updated application forms are contained in Attachment 1 including the equipment changes. A revised site plan is contained in Attachment 2. Revised emission calculations are provided in Attachment 3 based on the same operating assumptions used in the original application. Vendor specifications are provided in Attachment 4 for the updated emergency generators (EG-01, EG- Page F-158 Attachment F. Air Quality Permit Application Review Documents Mr. Charles McEachern July 20, 2017 Page 2 02)and the boiler (WH-01). The changes in annual emissions are summarized in the following table; creating a decrease in NOx, CO, VOC, and CO2e values. Annual Emissions (TonsN ear) NOx co voe PM SO2 CO2e Original 19.7 31.1 41.1 18.4 3.1 145,686 Application Proposed 19.2 31.0 21.2 18.4 3.1 129,133 Update If you have questions about this submittal, please do not hesitate to contact Mr. Laurence Labrie at (804) 273-3075 or at laurence.a.labrie@dominionenergy.com. Richard B. Gangle, Manager Environmental Atlantic Coast Pipeline Page F-159 Attachment F. Air Quality Permit Application Review Documents • Dominion Energy Services, Inc. 5000 Dominion Boulevard Glen Allen, VA 23060 DominionEnergy.com July 20, 2017 BY: OVERNIGHT MAIL Mr. Charles McEachem Raleigh Regional Office NCDEQ Division of Air Quality Suite 101 3800 Barrett Drive Raleigh, NC 27609 RE: Atlantic Coast Pipeline, L.L.C. Northampton Compressor Station Air Permit Application Update Dear Mr. McEachem: � p) --· :-0 (IO -·0 � -0 s (D P, Dominion ;:;:iiiiii" Energy· ti - c,_.. C: r-::I r-,.) ::;· -::I r,.;, 9 C) ::I -e. e. � Atlantic Coast Pipeline, LLC (ACP) is submitting updates to the Northampton Compressor Station permit application, dated September 16, 2015. The changes are to ancillary equipment including emergency generators and storage tanks. No changes are requested for the main natural gas compressors. The changes do not materially affect the applicable regulatory requirements. ACP is proposing the following updates: •Replace the Caterpillar G3516 emergency generator rated at 1,416 hp (EG-01) with a Caterpillar G3516B emergency generator rated at 1,818 hp; •Add a new Generac SG lO0 emergency generator rated at 148.9 hp (EG-02) for the regional operations center; •Replace the boiler rated at 6.3 MMBtu/hr (WH-01) with a Hurst LPW-G-125-60W boiler rated at 5 .25 MMBtu/hr; •Decrease the volume of the proposed pipeline fluids tank (TK-2) from 1,500 gallons to 1,000 gallons; •Increase the volume of the proposed Ammonia Tank (TK-3) from 8,000 gallons to 13,400 gallons; and •Correct a calculation error that overestimated fugitive emissions. The updated application forms are contained in Attachment 1 including the equipment changes. A revised site plan is contained in Attachment 2. Revised emission calculations are provided in Attachment 3 based on the same operating assumptions used in the original application. Vendor specifications are provided in Attachment 4 for the updated emergency generators (EG-01, EG- Page F-160 Attachment F. Air Quality Permit Application Review Documents Mr. Charles McEachem July 20, 2017 Page 2 02)and the boiler (WH-01). The changes in annual emissions are summarized in the following table; creating a decrease in NOx, CO, VOC, and CO2e values. Annual Emissions (Tons/Year) NOx co voe PM SO2 CO2e Original 19.7 31.1 41.1 18.4 3.1 145,686 Application Proposed 19.2 31.0 21.2 18.4 3.1 129,133 Update If you have questions about this submittal, please do not hesitate to contact Mr. Laurence Labrie at (804) 273-3075 or at laurence.a.labrie@dominionenergy.com. Richard B. Gangle, Manager Environmental Atlantic Coast Pipeline Page F-161 Attachment F. Air Quality Permit Application Review Documents ATTACHMENTS • ERM DOMINION -ACP-3 ST A TION Page F-162 Attachment F. Air Quality Permit Application Review Documents • A1TACHMENT A NC DENR PERMIT APPLICATION FORMS • ERM DOMINION - ACP-.3 Sf A TION Page F-163 Attachment F. Air Quality Permit Application Review Documents FORM A1 FACILITY (General Information) NCDENR/Dlvlslon of Air Quality· Application for Air Pennlt to Construct/Operate ()�ISED 05/25/12 NOTE-APPLICATION WILL NOT BE PROCESSED WITHOUT THE FOLLOWING: 0 Local Zoning Consistency Determination (if required) D Facility Reduction & Recycling Survey Form (Form A4) 0.pplication Fee 0 Responsible Official/Authorized Contact Signature 0 Appropriate Number of Copies of Application O.E. Seal (if required) GENERAL INFORMATION Legal Corporate/Owner Name: Atiantic Coast Pipeline, LLC Site Name: Nomampton Compressor Station Site Address (911 Address) Line 1: 718 Forest Rd Site Address Line 2: City: Pleasant Hill State: North Carolina Zip Code: 27866 County: Northampton CONTACT INFORMATION Permlttrechnlcal Contact: Fac/1/tyRnspection Contact: Name/Title: Laurence A Labrie Name/Title: Mailing Address Line 1: 5000 Dominion Boulevard Mailing Address Line 1: Mailing Address Line 2: 2 NE Mailing Address Line 2: City: Glen Allen State: VA Zip Code: 23060 City: State: Zip Code: Phone No. (area code) 804-273-3075 !Fax No. (area code) Phone No. ( area code ) I Fax No. ( area code) Email Address: lilUC!lD!;l! i1,li1bli11@!1Q!DIDiQDIIDllllll! ,Q!D Email Address: Responsible OfflclaVAuthorized Contact: Invoice Contact: Name/Title: Leslie Hartz Namemue: Richard B Gangle Mailing Address Line 1: 707 E. Main Street Mailing Address Line 1: 5000 Dominion Boulevard Mailing Address Line 2: Mailing Address Line 2: 2 NE City: Richmond State: VA Zip Code: 23219 City: Glen Allen State: VA Zip Code: Phone No. (area code) 804-771-4468 !Fax No. ( area code ) Phone No. (area code) 804-273-2814 I Fax No. (area code) 1ail Address: llllilill bil�@!IQIDIDIQDIIDllllll!,,Q!D Email Address: ... � .... "··- _,/ APPLICATION IS BEING MADE FOR 0 New Non-permitted Facility/Greenfield D Modification of Facility (permitted) D Renewal with Modification 0 Renewal (TV Only) FACILITY CLASSIFICATION AFTER APPLICATION (Check Only One) D General 0 Small D Prohibitory Small D Synthetic Minor O Title V FACILITY (Plant Site) INFORMATION Describe nature of (plant site) operation(s): Facility ID No. TBD Proposed new (greenfield) natural gas pipeline compressor station. I Primary SIC/NAICS Code: 4922/48621 o Current/Previous Air Permit No. N/A Expiration Date: Facility Coordinates: Latitude: 36.543874 Longitude: -77.505712 Does this application contain confidential YES D NO 0 •••1fyes, please contact the DAQ Regional Office prior to submitting this application ... • data? (See Instructions) PERSON OR FIRM THAT PREPARED APPLICATION Person Name: Robert Sawyer Firm'Name: Environmental Resources Management Mailing Address Line 1: 180 Admiral Cochrane Dr Mailing Address Line 2: Suite 400 City: Annapolis !state: MD Zip Code: 21401 lcounty: Anne Arundel Phone No. ( area code ) 410-266-0006 !Fax No. ( area code ) Email Address: CQbll!l,lii!Wll!:@ll!ID,,QaJ SIGNATURE OF RESPONSIBLE OFFICIAL/AUTHORIZED CONTACT Name (typed): Leslie Ha.ctz.._ Title: VP Pipeline Construction X Signature(Blue Ink): rXhV� Date: 7f3f? �ch Additional Sheets As Necessary A1 23060 Page F-164 Attachment F. Air Quality Permit Application Review Documents . EVISED 04/10/07 FORMs A2, A3 EMISSION SOURCE LISTING FOR THIS APPLICATION -A2 112r APPLICABILITY INFORMATION -A3 NCOENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate EMISSION SOURCE LISTING: New, Modified, Previously Unpermitted, Replaced, Deleted EMISSION SOURCE I EMISSION SOURCE I CONTROL DEVICE I CONTROL DEVICE ID NO. DE SCRIPTION ID NO. DESCRIPTION Equipment To Be ADDED By This Aoolication (New, Previously Unoermitted, or Replacement) CT-01 Taurus 70-10802S Compressor Turbine CT-01-SCR Selective Catalyst Reduction CT-01-0C Oxidation Catalyst CT-02 Centaur 50-62DOLS Compressor Turbine CT-02-SCR Selective Catalyst Reduction CT-02-0C Oxidation Catalyst CT-03 Centaur 40-4700S Compressor Turbine CT-03-SCR Selective Catalyst Reduction CT-03-0C Oxidation Catalvst EG-01 Caterpillar G35168 Emergency Generator N/A EG-02 Generac SG 1 OD Emeroency Generator N/A WH-01 Hurst LPW-G-125-60W Hot Water Boiler N/A TK-1 Pipeline Liquids Storage Tank N/A TK-2 Hydrocarbon Waste Tank N/A TK-3 Ammonia Tank N/A TK-4 Odorant Tank N/A Fug-01 Fugitive Leaks -Slowdowns N/A Fuo-02 Fugitive Leaks -Piping N/A Existing Permitted Equipment To Be MODIFIED B ,, This Aoollcation N/A C1 Eaulpment To Be DELETED By This AP11>llcation N/A 112(r) APPLICABILITY INFORMATION Is your facility subject to 40 CFR Part 68 "Prevention of Accidental Releases" -Section 112(r) of the Federal Clean Air Act? No If No, please specify in detail how your facility avoided applicability: No chemicals subject to regulation under this Subpart will be present onsite. The aqueous ammonia stored in TK-3 (exempt from permitting) will have an ammonia concentration of less than 20%. If your facility is Subject to 112(r), please complete the following: A. Have you already submitted a Risk Management Plan (RMP) to EPA Pursuant to 40 CFR Part 68.1 O or Part 68.150? Yes No Specify required RMP submittal date: If submitted, RMP submittal date: B. Are you using administrative controls to subject your facility to a lesser 112(r) program standard? Yes No If yes, please specify: Attach Additional Sheets As Necessary I A2 I A3 Page F-165 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ,ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-01 Taurus 70-10802S Compressor Turbine CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-01 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7} 0 Int.combustion engine/generator (Form B2} D Coating/finishing/printing (Form BS) D Incineration (Form BB) D Liquid storage tanks (Form B3} D Storage silos/bins (Form B6} D Other (Form B9} START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Taurus 70-10802S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?}: No PERCENTAGE ANNUAL THROUGHPUT (%}: DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLU...T�NT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 PARTICULATE MATTER<2.5 MICRONS (PM20) Mfg/AP-42 1.92 8.41 1.92 8.41 1.92 8.41 SULFUR DIOXIDE (SO2} AP-42 0.33 1.43 0.33 1.43 0.33 1.43 NITROGEN OXIDES (NOx} Mfg 1.91 8.35 3.41 14.95 1.91 8.35 �BON MONOXIDE (CO} Mfg 2.99 13.08 7.33 32.11 2.99 13.08 J.ATILE ORGANIC COMPOUNDS (VOC) Mfg 0.18 0.78 0.33 1.46 0.18 0.78 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE - SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS I LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00002 0.0001 0.00003 0.0001 0.00002 0.0001 Acetaldehyde 75-07-0 AP-42 0.002 0.01 0.003 0.01 0.002 0.01 Acrolein 107-02-8 AP-42 0.0003 0.001 0.0005 0.002 0.0003 0.001 Benzene 71-43-2 AP-42 0.0005 0.002 0.001 0.004 0.0005 0.002 Ethyl benzene 100-41-4 AP-42 0.001 0.01 0.003 0.01 0.001 0.01 Formaldehyde 50-00-0 Mfg. 0.11 0.50 0.23 0.99 0.11 0.50 Naphthalene 91-20-3 AP-42 0.0001 0.0002 0.0001 0.0004 0.0001 0.0002 PAH AP-42 0.0001 0.0004 0.0002 0.001 0.0001 0.0004 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00002 0.0004 0.15 Acetaldehyde 75-07-0 AP-42 0.002 0.04 13.78 Acrolein 107-02-8 AP-42 0.0003 0.01 2.20 Ammonia 7664-41-7 Mfg. 1.32 31.68 11,563.20 Benzene 71-43-2 AP-42 0.0005 0.01 4.13 Formaldehyde 50-00-0 Mfg. 0.11 2.72 992.03 Toluene 108-88-3 AP-42 0.005 0.12 44.78 Sd'"' 1330-2�7 AP-42 0.003 0.06 22.05 chments: (1) emissions calculations and supporting documentation; (2) indicate all requested slate and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-166 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Dlvision of Air Quality -Application for Air Permit to Construct/Operate B ,ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-01 Taurus 70-10802S Compressor Turbine, continued CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-01 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form 82) O Coating/finishing/printing (Form 85) D Incineration (Form 88) D Liquid storage tanks (Form 83) O Storage silos/bins (Form 86) D Other (Form 89) START CONSTRUCTION DATE: April 2017 !OPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Taurus 70-10802S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS / LIMITS) I (AFTER CONTROLS / LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source CARBON MONOXIDE (CO) Mfg ( )LATILE ORGANIC COMPOUNDS (VOC) Mfg �D OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS / LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.005 0.002 0.01 0.001 0.005 Toluene 108-88-3 AP-42 0.005 0.02 0.010 0.04 0.005 0.02 Xylene 1330-20-7 AP-42 0.003 0.01 0.005 0.02 0.003 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE - INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source Attachments: (1) emissions calculations and supporting documentaUon: (2) indicate aN requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and descrtbe how ·1se are monitored and with what frequency; and (3) descrtbe any monitortng devices. gauges. or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-167 Attachment F. Air Quality Permit Application Review Documents FORM B2 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate I B2 EMISSION SOURCE DESCRIPTION: Taurus 70--10B02S Compressor Turbine EMISSION SOURCE 10 NO: CT-01 CONTROL DEVICE ID NO(S): CT-01-SCR and CT-01-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) 10 NO(S): EP-01 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): N/A ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): N/A ENGINE OUTPUT (HP): 11,107 horsepower output ISO TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STATIONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 96.00 N/A • FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLlE) POLLUTANT NOX co PM PM10 voe Formaldehyde EMISSION FACTOR LB/UNIT 3.20 5.30 1.92 1.92 0.30 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: Attach Additional Sheets As Necessary Page F-168 Attachment F. Air Quality Permit Application Review Documents FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC) C3 OEVISED 12/01/01 NCDENR/Dlvislon of Air Quality -Application for Air Permit to Construct/Operate I / AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA. CONTROL DEVICE ID NO: CT-01-SCR and CT-01-0C lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-01 EMISSION POINT (STACK) ID NO(S): EP-01 I POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER: MODEL NO: MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD !METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD lcATALYST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT(S) COLLECTED: NO, co voe Formaldehyde BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: % % % % CONTROL DEVICE EFFICIENCY: 44 % 80 % 50 % 50 % OVERALL SYSTEM EFFICIENCY: % % % % EFFICIENCY DETERMINATION CODE: ,;rOTAL EMISSION RATE (LB/HR): )RESSURE DROP (IN. H20): MIN MAX OUTLET TEMPERATURE (°F): MIN MAX INLET TEMPERATURE {°F): MIN MAX RESIDENCE TIME (SECONDS): INLET AIR FLOW RATE (ACFM): (SCFM): COMBUSTION TEMPERATURE (°F): COMBUSTION CHAMBER VOLUME (FT'): INLET MOISTURE CONTENT (%): % EXCESS AIR: CONCENTRATION (ppmv) INLET OUTLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: UNITS: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: l3 NO l3YES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: Dt:SCRIBE ANY AUXILIARY MATERIALS INTRODULot:u INTO THE CON I KOL SYSTEM: f(TT ACH A DIAGRAM OF THE RELATIONSHIP OF THE i.;uNTROL DEVICE TO ITS EMISSION SOURCE(S): Attach Additional Sheets As Necessary Page F-169 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION {REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B �ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-02 Centaur 50-6200LS Compressor Turbine CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatingsflnks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incin eration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE: April 2011IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 50-6200LS EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 1.20 5.26 1.20 5.26 1.20 5.26 SULFUR DIOXIDE (S02) AP-42 0.20 0.89 0.20 0.894 0.20 0.89 NITROGEN OXIDES (NOx) Mfg 1.19 5.20 2.13 9.31 1.19 5.20 """\RBON MONOXIDE (CO) Mfg 1.87 8.19 4.57 20.04 1.87 8.19 JLATILE ORGANIC COMPOUNDS (VOC) Mfg 0.11 0.48 0.20 0.89 0.11 0.48 LEAD OTHER HAZARD0US JAIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.00005 0.00002 0.0001 0.00001 0.00005 Acetaldehyde 75-07-0 AP-42 0.001 0.005 0.002 O.Q1 0.001 0.005 Acrolein 107-02-8 AP-42 0.0002 0.001 0.0003 0.001 0.0002 0.001 Benzene 71-43-2 AP-42 0.0003 0.001 0.001 0.003 0.0003 0.001 Ethyl benzene 100-41-4 AP-42 0.0008 0.004 0.002 0.01 0.001 0.004 Formaldehyde 50-00-0 Mfg. 0.08 0.33 0.15 0.66 0.08 0.33 Naphthalene 91-20-3 AP-42 0.00003 0.0002 0.0001 0.0003 0.00003 0.0002 PAH AP-42 0.0001 0.0003 0.0001 0.001 0.0001 0.0003 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.0003 0.10 Acetaldehyde 75-07-0 AP-42 0.001 0.03 9.23 Acrolein 107-02-8 AP-42 0.0002 0.004 1.48 Ammonia 7664-41-7 Mfg. 0.82 19.63 7,165.68 Benzene 71-43-2 AP-42 0.0003 0.008 2.77 Formaldehyde 50-00-0 Mfg. 0.08 1.82 664.78 Toluene 108-88-3 AP-42 0.003 0.12 44.78 9'"' 1330-20-7 AP-42 0.002 0.06 22.05 achments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limlts (e.g. hours of operation, emission rates) and describe how se are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-170 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B .,JISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-02 Centaur 50-6200LS Compressor Turbine CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) 0Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 50-6200LS EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS I LIMITS) I (AFTER CONTROLS I LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM10) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (S02) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source BON MONOXIDE (CO) Mfg ,...JLATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS I LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.003 0.002 0.01 0.001 0.003 Toluene 108-88-3 AP-42 0.003 0.02 0.01 0.03 0.003 0.02 Xylene 1330-20-7 AP-42 0.002 0.01 0.003 0.01 0.002 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source ochments: (1) emissions calculations and supporting documentation; (2) indicate all requested stale and federal enforceable pennit limits (e.g. hours of operation, emission rates) and describe howe are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-171 Attachment F. Air Quality Permit Application Review Documents FORM 82 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate I 82 EMISSION SOURCE DESCRIPTION: Centaur 50-6200LS Compressor Turbine EMISSION SOURCE ID NO: CT-02 CONTROL DEVICE ID NO(S): CT-02-SCR and CT-02-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-02 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): NIA ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): N/A ENGINE OUTPUT (HP): 6,276 horsepower output ISO TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STA"'(IONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 60.0 NIA FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe Formaldehyde EMISSION FACTOR LB/UNIT 1.98 3.30 1.20 1.20 0.19 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: Attach Additional Sheets As Necessary Page F-172 Attachment F. Air Quality Permit Application Review Documents FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC) C3 (jEVISED 12/01/01 NCDENR/Dlvision of Air Quality· Application for Air Permit to Construct/Operate I AS REQUIRED B_Y 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CABOLINA. CONTROL DEVICE ID NO: CT-02-SCR and CT-02-OC CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-02 EMISSION POINT (STACK) ID NO(S): EP-02 POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER: MODEL NO: MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD jCATALYST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT($) COLLECTED: BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: CONTROL DEVICE EFFICIENCY: OVERALL SYSTEM EFFICIENCY: EFFICIENCY DETERMINATION CODE: ( JOT AL EMISSION RATE (LB/HR) : hESSURE DROP (IN. H2O): MIN INLET TEMPERATURE (°F): MIN INLET AIR FLOW RATE (ACFM): COMBUSTION CHAMBER VOLUME (FT\ % EXCESS AIR: MAX MAX (SCFM): NOx co voe % % 44 % 80 % 50 % % OUTLET TEMPERATURE (°F): MIN RESIDENCE TIME (SECONDS): COMBUSTION TEMPERATURE (°F): INLET MOISTURE CONTENT (%): CONCENTRATION (ppmv) INLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: l;; NO l;;YES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM: .TI ACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S): Attach Additional Sheets As Necessary Formaldehyde % % 50 % MAX OUTLET UNITS: UNITS: % % % Page F-173 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) VISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate 8 ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-03 Centaur 40-4700S Compressor Turbine CONTROL DEVICE ID NO(S): CT -03-SCR and CT -03-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPR OPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) 0 Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form 82) D Coating/finishing/printing (Form 85) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage silos/bins (Form B6) D Other (Form 89) START CONSTRUCTION DATE: April 2011IOPERATION DATE: November 201 B DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 40-4700S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACIT Y CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 PARTICULATE MATTER<2.5 MICRONS (PM20) Mfg/AP-42 1.02 4.47 1.02 4.47 1.02 4.47 SULFUR DIOXIDE (S02) AP-42 0.17 0.76 0.17 0.76 0.17 0.76 NITROGEN OXIDES (NOx) Mfg 1.01 4.44 5.02 22.01 1.01 4.44 �RBON MONOXIDE (CO) Mfg 1.66 7.29 6.92 30.31 1.66 7.29 )...ATILE ORGANIC COMPOUNDS (VOC) Mfg 0.09 0.41 0.17 0.76 0.09 0.41 LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.00004 0.00002 0.0001 0.00001 0.00004 Acetaldehyde 75-07-0 AP-42 0.001 0.004 0.002 0.01 0.001 0.004 Acrolein 107-02-8 AP-42 0.0001 0.0006 0.0003 0.001 0.0001 0.001 Benzene 71-43-2 AP-42 0.0003 0.001 0.001 0.002 0.0003 0.001 Ethylbenzene 100-41-4 AP-42 0.001 0.003 0.001 0.01 0.001 0.003 Formaldehyde 50-00-0 Mfg. 0.06 0.27 0.12 0.54 0.06 0.27 Naphthalene 91-20-3 AP-42 0.00003 0.0001 0.0001 0.0002 0.00003 0.0001 PAH AP-42 0.00005 0.0002 0.0001 0.000 0.0000 0.0002 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT ANO CAS NO. EF SOURCE lb/hr lb/day lb/yr 1,3-Butadiene 106-99-0 AP-42 0.00001 0.0002 0.08 Acetaldehyde 75-07-0 AP-42 0.0009 0.02 7.51 Acrolein 107-02-8 AP-42 0.0001 0.003 1.20 Ammonia 7664-41-7 Mfg. 0.69 16.56 6,044.40 Benzene 71-43-2 AP-42 0.0003 0.006 2.25 Formaldehyde 50-00-0 Mfg. 0.062 1.48 541.00 Toluene 108-88-3 AP-42 0.003 0.07 24.42 �lene 1330-20-7 AP-42 0.001 0.03 12.02 Q.chments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how e are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or lest ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-174 Attachment F. Air Quality Permit Application Review Documents FORMB SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) . ISED 12/01/01 NCDENR/Division of Air Quality. Application for Air Permit to Construct/Operate B ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: CT-03 Centaur 40-4700S Compressor Turbine CONTROL DEVICE ID NO(S): CT-03-SCR and CT-03-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired compressor turbine used to boost the pressure of natural gas in a transmission pipeline. TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form 81) 0 WoodworKing (Form 84) D Manufact. of chemicalslcoatingsflnks (Form 87) 0 Int.combustion engine/generator (Form B2) O Coating/finishing/printing (Form B5) 0 Incineration (Form BB) O Liquid storage tanks (Form B3) 0 Storage silos/bins (Form BB) 0 Other (Form 89) START CONSTRUCTION DAl April 2017 !OPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Solar Turbines Centaur 40-4700S EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, KKKK NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FDR THIS SOURCE - SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg SULFUR DIOXIDE (SO2) AP-42 NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source ( 'RBON MONOXIDE (CO) Mfg "1'6LATILE ORGANIC COMPOUNDS (VOC) Mfg LEAD OTHER HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Propylene oxide 75-56-9 AP-42 0.001 0.003 0.001 0.01 0.001 0.003 Toluene 108-88-3 AP-42 0.003 0.01 0.01 0.02 0.003 0.01 Xylene 1330-20-7 AP-42 0.001 0.01 0.003 0.01 0.001 0.01 TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr See Form B, Page 1, for TAP totals for this source Qchments: (1) emissions calculaUons and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe w these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source. COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE Attach Additional Sheets As Necessary Page F-175 Attachment F. Air Quality Permit Application Review Documents FORM B2 EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS) REVISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate I 82 EMISSION SOURCE DESCRIPTION: Centaur 40-4700S Compressor Turbine EMISSION SOURCE ID NO: CT-03 CONTROL DEVICE ID NO(S): CT-03-SCR and CT-03-OC OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-03 CHECK ALL THAT APPLY 0 EMERGENCY 0 SPACE HEAT 0 ELECTRICAL GENERATION D PEAK SHAVER 0 OTHER (DESCRIBE): Natural Gas Compressor Turbine GENERATOR OUTPUT (KW): N/A ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): NIA ENGINE OUTPUT (HP): 4,427 horsepower output ISO TYPE ICE: 0 GASOLINE ENGINE 0 DIESEL ENGINE UP TO 600 HP 0 DIESEL ENGINE GREATER THAN 600 HP 0 DUAL FUEL ENGINE 0 OTHER (DESCRIBE): Natural Gas Comprassor Turbine (complete below) ENGINE TYPE 0 RICH BURN 0 LEAN BURN EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER OR STATIONARY GAS TURBINE (comple1e below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below) FUEL 0 NATURAL GAS DOIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN 0 TURBINE 0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE): CYCLE: 0 COGENERATION 0 SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): 0 REGENERATIVE 0 COMBINED NONSELECTIVE CATALYTIC REDUCTION D SELECTIVE CATALYTIC REDUCTION 0 CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER D UNCONTROLLED 0 0 UNCONTROLLED 0 LEAN-PREMIX and oxidation catalyst FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL) MAXIMUM DESIGN REQUESTED CAPACITY FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR) Natural Gas MMBtu 51.0 NIA FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT) Natural Gas 1,020 scf 0.0005 MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE) POLLUTANT NOX co PM PM10 voe Formaldehyde EMISSION FACTOR LB/UNIT 4.70 5.70 1.02 1.02 0.16 0.00288 UNIT hour hour hour hour hour MMBtu DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS: COMMENTS: • Attach Additional Sheets As Necessary Page F-176 Attachment F. Air Quality Permit Application Review Documents FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC) C3 OEVISED 12/01/01 NCDENR/Dlvislon of Air Quality -Application for Air Permit to Construct/Operate I / AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENG/NNER (P.E.) LICENSED IN NORTH CAROl,INA. CONTROL DEVICE ID NO: CT-03-SCR and CT-03-0C lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-03 EMISSION POINT (STACK) ID NO(S): EP-03 I POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1 MANUFACTURER: MODEL NO: MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018 OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017 1 of 1 TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD !METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL TBD SULFUR COMPOUND OTHER NONE TYPE OF CATALYST: TBD lcATALYST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD SCFM THROUGH CATALYST: DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM: Selective Catalyst Reduction and Oxidation Catalyst POLLUTANT(S) COLLECTED: BEFORE CONTROL EMISSION RATE (LB/HR): CAPTURE EFFICIENCY: CONTROL DEVICE EFFICIENCY: OVERALL SYSTEM EFFICIENCY: EFFICIENCY DETERMINATION CODE: ( .;roTAL EMIssI0N RATE (LB/HRJ : )RESSURE DROP (IN. H20): MIN INLET TEMPERATURE (°F): MIN INLET AIR FLOW RATE (ACFM): COMBUSTION CHAMBER VOLUME (FT3): % EXCESS AIR: MAX MAX (SCFM): NO, co voe % % 80 % 90 % 50 % % OUTLET TEMPERATURE (°F): MIN RESIDENCE TIME (SECONDS): COMBUSTION TEMPERATURE (°FJ: INLET MOISTURE CONTENT (%): CONCENTRATION (ppmv) INLET AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: DESCRIBE METHOD USED TO INCREASE MIXING: DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE: DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES: STACK TESTING PORTS: (j NO (jYES (INLET AND OUTLET) DESCRIBE MAINTENANCE PROCEDURES: DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM: ATTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S): Attach Additional Sheets As Necessary Formaldehyde % % 50 % MAX OUTLET UNITS: UNITS: % % % Page F-177 Attachment F. Air Quality Permit Application Review Documents