appalachia midstream services, llc park place corporate center 2 2018 applications... · 2018. 5....
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Appalachia Midstream Services, LLC Park Place Corporate Center 2 2000 Commerce Drive Pittsburgh, PA 15275-1026
May 18, 2018 (Via Federal Express)
Beverly D. McKeone New Source Review Program Manager Division of Air Quality West Virginia Department of Environmental Protection 601 57th Street SE Charleston, WV 25304-2345
Subject: Application for G35-D General Permit Registration Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Brooke County, West Virginia
Dear Ms. McKeone:
Appalachia Midstream Services, LLC (AMS) is submitting one (1) original paper copy and two (2) CD-ROMs of an Application for G35-D General Permit Registration for the proposed grassroots Threedubs Compressor Station (3WCS), located at the end of Grizzel Ln, approximately 0.3 mi East of Apple Pie Ridge Rd, Wellsburg, in Brooke County, West Virginia.
This application for G35-D General Permit Registration has been prepared and submitted to provide for the construction and operation of the following equipment at the subject facility:
• Four (4) 5,000 bhp CAT G3616LE A4 Compressor Engines CE-01 thru CE-04 • Compressor Rod Packing CRP • Startup/Shutdown/Maintenance (including Blowdown) SSM • One (1) SSM Zeeco MJ-16 Flare FLR • One (1) 1,742 bhp FlexEnergy GT1300S Microturbine Generator GT • One (1) 200 MMscfd Dehydrator - Flash Tank DFT • One (1) 200 MMscfd Dehydrator - Still Vent DSV • One (1) 2.0 MMBtu/hr Reboiler RBV • One (1) Thermal Oxidizer (Dehydrator Emissions Control) TOx • Six (6) Stabilized Condensate Storage Tanks (2,400 bbl Total) TK-01 thru TK-06 • Two (2) Produced Water Storage Tanks (800 bbl Total) TK-07 thru TK-08 • Stabilized Condensate and Produced Water Truck Load-Out TLO • Piping and Equipment Fugitives (Gas and Light Oil) FUG-G and FUG-L • Engine Crankcase Emissions ECC
The facility qualifies as a Minor Source under Non-Attainment New Source Review (NNSR), Prevention of Significant Deterioration (PSD), and Title V Operating Permits. The facility is also an Area Source for Hazardous Air Pollutants (HAP) under the National Emission Standards for Hazardous Air Pollutants (NESHAP) regulations.
Application for
G35-D General Permit Registration
For the:
Appalachia Midstream Services, LLC (AMS)
Threedubs Compressor Station (3WCS) Plant ID No. TBD
Brooke County, West Virginia
Submitted to:
West Virginia
Department of Environmental Protection
Division of Air Quality
Submitted by:
Appalachia Midstream Services, LLC (AMS)
Park Place Corporate Center 2 2000 Commerce Drive
Pittsburgh, PA 15275-1026
Prepared by:
EcoLogic Environmental Consultants, LLC
864 Windsor Court Santa Barbara, CA 93111-1037
May 2018
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Application for
G35-D General Permit Registration
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS)
Plant ID No. TBD Brooke County, West Virginia
Table of Contents
Supplement to Application
Application for G35-D General Permit Registration
Attachments to Application
• Attachment A Single Source Determination Form • Attachment B Siting Criteria Waiver (If Applicable) • Attachment C Current Business Certificate • Attachment D Process Flow Diagram(s) (PFD) • Attachment E Process Description • Attachment F Plot Plan • Attachment G Area Map • Attachment H G35-D Section Applicability Form • Attachment I Emission Units/ERD Table • Attachment J Fugitive Emissions Summary Sheet(s) • Attachment K Storage Vessel(s)Data Sheet • Attachment L Natural Gas Fired Fuel Burning Unit(s) Data Sheet • Attachment M Internal Combustion Engine Data Sheet(s) • Attachment N Tanker Truck Loading Data Sheet (If Applicable) • Attachment O Glycol Dehydration Unit Data Sheet(s) • Attachment P Pneumatic Controllers Data Sheet(s) • Attachment Q Centrifugal Compressor Data Sheet(s) • Attachment R Reciprocating Compressor Data Sheet(s) • Attachment S Blowdown and Pigging Operations Data Sheet(s) • Attachment T Air Pollution Control Device/Emission Reduction Device(s) Sheet(s) • Attachment U Emission Calculations • Attachment V Facility-wide Emission Summary Sheet(s) • Attachment W Class I Legal Advertisement
Appendices to Application
• Appendix S1 Lab Analysis (Wet Gas, Stabilized Condensate) • Appendix S2 AP-42 / EPA Emission Factors • Appendix S3 Btu Load (Flare and Thermal Oxidizer) • Appendix S4 Vendor Data (Engines, Flare, Microturbine, Thermal Oxidizer) • Appendix S5 Emission Programs (GRIGLYCalc, EPA TANKS)
Application Fee Determination
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Supplement
to Application for G35-D General Permit Registration
A. Introduction
B. Potential to Emit (PTE)
C. Applicability of New Source Review (NSR) Regulations 1. Prevention of Significant Deterioration (PSD) 2. Nonattainment New Source Review (NSR) 3. Major Source of Hazardous Air Pollutants (HAPs) 4. Title V Operating Permit (TVOP)
D. Applicability of Federal Regulations 1. NSPS A, General Provisions 2. NSPS A, Control Devices – Flares 3. NSPS Dc – Steam Generating Units 4. NSPS Kb – Volatile Organic Liquid Storage Vessels 5. NSPS GG – Stationary Gas Turbines 6. NSPS KKK – Leaks from Natural Gas Processing Plants 7. NSPS LLL – Onshore Natural Gas Processing: SO2 Emissions 8. NSPS IIII – Compression Ignition Reciprocating Internal Combustion Engines (RICE) 9. NSPS JJJJ – Stationary Spark Ignition (SI) Internal Combustion Engines (ICE) 10. NSPS KKKK – Stationary Combustion Turbines 11. NSPS OOOO – Oil and Natural Gas Production, Transmission and Distribution 12. NSPS OOOOa – Oil and Natural Gas Production, Transmission and Distribution 13. NESHAP Part 61 - Designated Source Standards 14. NESHAP Part 63 (aka MACT) – General Provisions 15. NESHAP HH – Oil and Natural Gas Production Facilities 16. NESHAP HHH – Natural Gas Transmission and Storage Facilities 17. NESHAP YYYY – Stationary Combustion Turbines 18. NESHAP ZZZZ – Stationary Reciprocating Internal Combustion Engines (RICE) 19. NESHAP DDDDD – Boilers and Process Heaters – Major Sources 20. NESHAP JJJJJJ – Boilers – Area Sources 21. CAM – Compliance Assurance Monitoring 22. Chemical Accident Prevention Provisions (Risk Management Plan (RMP)) 23. GHG – Mandatory Greenhouse Gases (GHG) Reporting
E. Applicability of Source Aggregation
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Supplement
to Application for G35-D General Permit Registration
--- Continued ---
F. Applicability of State Regulations
1. Particulate Air Pollution from Combustion of Fuel in Indirect Heat Exchangers 2. Prevent and Control the Discharge of Air Pollutants into the Open Air Which Causes
or Contributes to an Objectionable Odor or Odors 3. Control of Air Pollution from Combustion of Refuse 4. Prevent and Control Air Pollution from the Emission of Sulfur Oxides 5. Permits for Construction, Modification, Relocation and Operation of Stationary
Sources of Air Pollutants, Notification Requirements, Administrative Updates, Temporary Permits, General Permits, and Procedures for Evaluation
6. Permits for Construction and Major Modification of Major Stationary Sources of Air Pollutants
7. Standards of Performance for New Stationary Sources Pursuant to 40 CFR Part 60 8. Permits for Construction and Major Modification of Major Stationary Sources of Air
Pollution Which Cause or Contribute to Nonattainment 9. Regulation of Volatile Organic Compounds (VOC) 10. Air Quality Management Fees Program 11. Prevent and Control Emissions of Toxic Air Pollutants (Best Available Control
Technology (BAT)) 12. Air Pollution Emissions Banking and Trading 13. Emission Statements for VOC and NOx 14. Requirements for Operating Permits 15. Emission Standards for Hazardous Air Pollutants (HAP)
Supplement – Page 1 of 11
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
SUPPLEMENT
(Regulatory Discussion)
A. Introduction Appalachia Midstream Services, LLC (AMS) proposes to construct and operate the grassroots Threedubs Compressor Station (3WCS) to be located at the end of Grizzel Ln, approximately 0.3 miles East of Apple Pie Ridge Rd, Wellsburg, in Brooke County, West Virginia. (See Attachment G – Area Map). The facility receives natural gas from local production wells then compresses and dehydrates the gas for delivery to a gathering pipeline. Additionally, raw field condensate is received at the site, stabilized and then sent offsite via tanker trucks.
This application provides for the following equipment and operations at the subject facility:
• Four (4) 5,000 bhp CAT G3616LE Compressor Engines CE-01 thru CE-04 • Compressor Rod Packing CRP • Startup/Shutdown/Maintenance (including Blowdown) SSM
- Compressor Rod Packing (CRP) “ - Emergency Shutdown (ESD) Testing “ - Pigging Operations (PIG) “
• One (1) Process Flare (Control for SSM) FLR • One (1) 1,742 bhp FlexEnergy Microturbine Generator GT • One (1) 200 MMscfd TEG Dehydrator - Flash Tank DFT • One (1) 200 MMscfd TEG Dehydrator - Still Vent DSV • One (1) 2.0 MMBtu/hr Reboiler RBV • One (1) Thermal Oxidizer (Control for Dehydrator) TOx • Six (6) Stabilized Condensate Storage Tanks (2,400 bbl Total) TK-01 thru TK-06 • Two (2) Produced Water Storage Tanks (800 bbl Total) TK-07 and TK-08 • Stabilized Condensate/Produced Water Truck Load-Out TLO • Piping and Equipment Fugitives (Gas and Light Liquid) FUG-G and FUG-L • Engine Crankcase Emissions ECC
B. Potential to Emit (PTE) The facility qualifies as a synthetic minor source for criteria pollutants and as an area source of HAPs, as summarized on the following page.
Supplement – Page 2 of 11
CE-01 Compressor Engine 01 - CAT G3616LE A4 19.31 11.32 9.05 1.22 1.72 23,656CE-02 Compressor Engine 02 - CAT G3616LE A4 19.31 11.32 9.05 1.22 1.72 23,656CE-03 Compressor Engine 03 - CAT G3616LE A4 19.31 11.32 9.05 1.22 1.72 23,656CE-04 Compressor Engine 04 - CAT G3616LE A4 19.31 11.32 9.05 1.22 1.72 23,656CRP Compressor Rod Packing --- --- 30.15 --- 0.72 1,537
Compressor Blowdown (CBD) --- --- 4.06 --- 0.10 207Emergency Shutdown (ESD) Testing --- --- 0.17 --- 4E-03 8.78Pigging Operations (PIG) --- --- 0.15 --- 3E-03 7.42
FLR SSM Flare - Zeeco MJ-16 (Comb. Only) 1.50 4.74 1E-03 1E-03 1E-03 1,789GT Microturbine Generator - FlexEnergy GT1300S 4.55 12.51 1.23 0.09 0.14 14,414DFT Dehydrator - Flash Tank --- --- 4.89 --- 0.11 93.41DSV Dehydrator - Still Vent --- --- 6.46 --- 2.61 9.59RBV Dehydrator - Reboiler Vent 0.86 0.72 0.05 6E-04 0.02 1,026TOx Thermal Oxidizer - Zeeco Z-HTO (Comb. Only) 2.67 8.43 2E-03 2E-03 2E-03 3,184
TK-01 Storage Tank 01 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-02 Storage Tank 02 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-03 Storage Tank 03 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-04 Storage Tank 04 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-05 Storage Tank 05 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-06 Storage Tank 06 - Stabilized Condensate --- --- 0.06 --- 0.01 ---TK-07 Storage Tank 07 - Produced Water --- --- 1E-03 --- 0.01 ---TK-08 Storage Tank 08 - Produced Water --- --- 1E-03 --- 0.01 ---
Truck Load-Out - Stabilized Condensate --- --- 7.51 --- 1.08 ---Truck Load-Out - Produced Water --- --- 0.14 --- 0.02 ---
86.82 71.67 91.38 2.41 11.77 116,901
100 100 100 na na na
FUG-G Process Piping Fugitives - Gas --- --- 4.23 --- 0.10 216FUG-L Process Piping Fugitives - Light Liquid --- --- 7.15 --- 1.03 ---ECC Engine Crankcase 0.21 1.51 0.59 0.07 0.11 252
0.21 1.51 11.98 0.07 1.23 468
87.03 73.18 103 5.03 13.00 117,369
na na na 10 25 na
1 - Emissions based on 100% of rated load for 8,760 hr/yr, except SSM, FLR, and TLO which are infrequent.2 - VOC is volatile organic compounds, as defined by EPA, includes HCHO (formaldehyde).3 - HCHO is formaldehyde and is the individual HAP with the highest PTE.
Total Facility-Wide PTE
Unit
Description
Unit
ID
4 - Total HAP includes, but not limited to, HCHO (Formaldehyde), n-hexane, BTEX (benzene, toluene, ethylbenzene, xylenes, 2,2,4-TMP (i-Octane), acetaldehyde, acrolein, and MeOH.
5 - CO2e is aggregated Greenhouse Gas (GHG), comprised of carbon dioxide (CO2), methane (CH4(, and nitrous oxide (N2O), as adjusted for Global Warming Potential (GWP).
Fugitive Sources
Facility-Wide Potential-to-Emit (PTE)
Facility-Wide Potential-to-Emit (PTE) [Tons per Year]
Total Fugitive Sources:
Important Notes:
* Criteria pollutant fugitive emissions are not included in major source determinations because the facility is not a listed source category. * Hazardous air pollutant (HAP) fugitive emissions are included in major source determinations regardless of whether the facility is a listed source category. * Greenhouse gases (GHG) are not treated as air pollutants for major source determinations.
VOCTotal
HAP
TLO
SSM
Total Point Sources:
HCHO
Title V Operating Permit Threshold:
Title V Operating Permit Threshold:
NOX COGHG
(CO2e)
Point Sources
Supplement – Page 3 of 11
C. Applicability of New Source Review (NSR) Regulations
The following New Source Review (NSR) regulations are potentially applicable to natural gas compressor stations. Applicability to the subject facility has been determined as follows:
1. Prevention of Significant Deterioration (PSD) [Not Applicable]
This rule does not apply because the facility is a “PSD Minor Source” for each regulated pollutant, as follows:
• NOx: PSD Natural Minor Source with Pre-Controlled PTE less than 250 tpy • CO: PSD Synthetic Source with Controlled PTE less than 250 tpy • VOC: PSD Synthetic Minor Source with Controlled PTE less than 250 tpy • PM10/2.5: PSD Natural Minor Source with Pre-Controlled PTE less than 250 tpy • SO2: PSD Natural Minor Source with Pre-Controlled PTE less than 250 tpy • CO2e: Not Applicable - Facility is NOT PSD Major for any other pollutant
2. Non-Attainment New Source Review (NNSR) [Not Applicable]
This rule does not apply. The facility is in Brooke County, WV, which is currently classified as Attainment, Unclassified, or Maintenance for all national ambient air quality standards (NAAQS) (http://www3.epa.gov/airquality/greenbook/ancl.html).
3. Major Source of Hazardous Air Pollutants (HAPs) [Not Applicable]
This rule does not apply. The entire facility qualifies as a “HAP Area Source” as follows:
• Each HAP: HAP Area Source with Controlled Individual HAP PTE less than 10 tpy • Total HAPs: HAP Area Source with Controlled Total of All HAPs PTE less than 25 tpy
4. Title V Operating Permit (TVOP) [Not Applicable]
This rule does not apply. With the requested Federally Enforceable Limits (FEL), the facility qualifies as a “Title V Minor Source” as follows:
• NOx: Title V Natural Minor Source with Pre-Controlled PTE less than 100 tpy • CO: Title V Synthetic Minor Source with Controlled PTE less than 100 tpy • VOC: Title V Synthetic Minor Source with Controlled PTE less than 100 tpy • PM10/2.5 Title V Natural Minor Source with Pre-Controlled PTE less than 100 tpy • SO2: Title V Natural Minor Source with Pre-Controlled PTE less than 100 tpy • Each HAP: Title V Synthetic Minor (Area) Source with Controlled PTE less than 10 tpy • Total HAPs: Title V Synthetic Minor (Area) Source with Controlled PTE less than 25 tpy
Important Notes:
* Criteria pollutant fugitive emissions are not included in major source determinations because the facility is not a listed source category.
* Hazardous air pollutant (HAP) fugitive emissions are included in major source determinations regardless of whether the facility is a listed source category.
* Greenhouse gases (GHG) are not treated as air pollutants for major source determinations.
Supplement – Page 4 of 11
D. Applicability of Federal Regulations
The following federal regulations are potentially applicable to natural gas compressor stations. Applicability to the subject facility has been determined as follows:
1. NSPS A, General Provisions
40CFR§60.1-§60.19 [Applicable]
This rule does apply to all sources subject to an NSPS (unless a specific provision is excluded within the source NSPS). Requirements include notification (§60.7); recordkeeping and reporting (§60.7); source testing (§60.8, §60.11); and control device requirements (§60.18).
2. NSPS A, Control Devices - Flares
40CFR§60.18(b) [Not Applicable]
This rule does not apply to the SSM Flare (FLR) nor to the Thermal Oxidizer (TOx) because neither is subject to any New Source Performance Standard (NSPS).
3. NSPS D (also Da, Db, and Dc), Steam Generating Units
40CFR§60.40-§60.48 [Not Applicable]
These rules do not apply because there are no steam generating units (including line heaters) at the facility with a maximum design heat input capacity equal to or greater than 10 MMBtu/hr (§60.40c(a)).
4. NSPS K (also Ka and Kb), Volatile Organic Liquid Storage Vessels
40CFR§60.40-§60.48 [Not Applicable]
This rule does not apply because there is no Storage Vessel/Tank with capacity equal to or greater than 75 m3 (471.7 bbl or 19,813 gal) that is used to store volatile organic liquids (VOL) at the facility (§60.110(a)).
5. NSPS GG, Stationary Gas Turbines
40CFR§60.330-§60.335 [Not Applicable]
This rule does not apply because the FlexEnergy GT1300S Microturbine Generator (GT) is comprised of four (4) individual microturbines and each microturbine has a heat input at peak load less than 10.7 gigajoules (10 million Btu) per hour, based on the lower heating value of the fuel fired (§60.330).
6. NSPS KKK, Leaks from Natural Gas Processing Plants
40CFR§60.630-§60.636 [Not Applicable]
This rule does not apply because the facility is not a natural gas processing plant (§60.630(a)).
7. NSPS LLL, Onshore Natural Gas Processing: SO2 Emissions
40CFR§60.640-§60.648 [Not Applicable]
This rule does not apply because there is no gas sweetening operation at the facility (§60.640(a)).
Supplement – Page 5 of 11
8. NSPS IIII, Compression Ignition Reciprocating Internal Combustion Engines
40CFR§60.4200-§60.4219 [Not Applicable]
This rule does not apply because there is no compression ignition stationary reciprocating internal combustion engine (RICE) at the facility that was manufactured on or after April 1, 2006 (§60.4200(a)).
9. NSPS JJJJ, Stationary Spark Ignition (SI) Internal Combustion Engines (ICE)
40CFR§60.4230-§60.4248 [Applicable]
This rule does apply to the four (4) 5,000 bhp CAT G3616LE A4 lean burn compressor engines (CE-01 thru CE-04) because the maximum engine power of each engine is greater than 1,340 bhp and each engine was manufactured or reconstructed on or after 07/01/07 (§60.4230(a)(4)(i)).
Requirements include NOx, CO and VOC emission limits (§60.4233(e-f)); operating limits (§60.4243); performance testing (§60.4244); and notification and recordkeeping (§60.4245).
10. NSPS KKKK, Stationary Combustion Turbines
40CFR§60.4300-§60.4420 [Not Applicable]
This rule does not apply because the FlexEnergy GT1300S Microturbine Generator (GT) is comprised of four (4) individual microturbines and each microturbine has a heat input at peak load less than 10.7 gigajoules (10 million Btu) per hour, based on the lower heating value of the fuel fired (§60.4305(a)).
11. NSPS OOOO, Crude Oil and Natural Gas Production
40CFR§60.5360-§60.5430 [Not Applicable]
This rule does not apply because the facility was constructed after September 18, 2015 (§60.5360).
12. NSPS OOOOa, Crude Oil and Natural Gas Production
40CFR§60.5360a-§60.5430a [Applicable]
This rule does apply to the reciprocating compressors driven by the CAT G3616LE A4 Engines (CE-01 thru CE-04) because the facility is identified within the natural gas production segment and each compressor commenced construction after 08/23/11 (§60.5360 and §60.5365(c)).
Requirements include replacing rod packing systems on a specified schedule (§60.5385(a)) and notification, monitoring, recordkeeping and reporting (§60.5410(c), §60.5415(c), §60.5420(b)(1) and §60.5420(b)(4)).
Supplement – Page 6 of 11
This rule does apply to the fugitive emission components at a compressor station.
Requirements include reducing GHG (in the form of a limitation on emissions of methane) and VOC emissions by developing a fugitive emission monitoring plan, monitoring all fugitive emission components, repairing all sources of fugitive emissions, and recordkeeping and reporting. For the purposes of this section, fugitive emissions are defined as: Any visible emission from a fugitive emissions component observed using optical gas imaging or an instrument reading of 500 ppm or greater using Method 21.
This rule does not apply to the stabilized condensate storage tanks (TK-01 thru TK-06) nor to the produced water storage tanks (TK-07 and TK-08) (nor any other tank) at the facility because each tank does not have the potential to emit more than 6 tpy of VOCs. Note, however, there is a requirement to document that the VOC PTE is less than 6 tpy per tank (§60.5420).
This rule does not apply to the pneumatic controllers because they are compressed air driven, else they have a bleed rate ≤ 6 scfh, are located between the wellhead and point of custody transfer, and they are not located at a natural gas processing plant (§60.5365(d)(1)).
Other requirements of this rule do not apply because the facility is a) not a well, b) does not have a centrifugal compressor using wet seals, and c) does not have a process unit associated with the processing of natural gas.
13. NESHAP Part 61 - Designated Source Standards
40CFR§61.01-§61.359 [Not Applicable]
This rule does not apply because the facility is not a NESHAP Designated Facility (or Source).
Specifically, NESHAP J - Equipment Leaks (Fugitive Emission Sources) of Benzene and NESHAP V - Equipment Leaks (Fugitive Emission Sources) do not apply because all the fluids (liquid or gas) at the facility are less than 10 wt% volatile hazardous air pollutant (VHAP) ((§61.111 and §61.241).
14. NESHAP Part 63 (aka: MACT) - General Provisions
40CFR§63.1-§63.16 [Applicable/Exempt]
This rule does apply because the dehydrator (DFT and DSV) is subject to NESHAP HH–Oil and Natural Gas Production Facilities. However, because the dehydrator has actual annual average benzene emissions less than 0.9 megagrams per year, it is exempt from all requirements except to maintain records of actual annual average benzene emissions to demonstrate continuing exemption status (§63.764(e)(1)).
This rule does not apply to storage vessels (tanks), compressors, or ancillary equipment because the facility is an area source of HAP emissions (§63.760(b)(2)). In no case does this rule apply to engines or turbines.
Supplement – Page 7 of 11
15. NESHAP HH, Oil and Natural Gas Production Facilities
40CFR§63.760-§63.779 [Applicable/Exempt]
This rule does apply to the dehydrator (DFT and DSV). However, because the facility is an area source of HAP emissions, and the actual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere is less than 0.90 megagram per year (1.0 tpy), the dehydration unit is exempt. The only requirement is to maintain records of the actual average benzene emissions per year (§63.774(d)(1)(i)).
This rule does not apply to storage vessels (tanks), compressors, or ancillary equipment because the facility is an area source of HAP emissions (§63.760(b)(2)). In no case does this rule apply to engines or turbines.
16. NESHAP HHH, Natural Gas Transmission and Storage Facilities
40CFR§63.1270-§63.1289 [Not Applicable]
This rule does not apply because the facility is not a natural gas transmission or storage facility transporting or storing natural gas prior to local distribution (§63.1270(a)).
17. NESHAP YYYY, Stationary Combustion Turbines
40CFR§63.6080-§63.6175 [Not Applicable]
This rule does not apply because the facility is not a major source of HAP emissions (§63.6080).
18. NESHAP ZZZZ, Stationary Reciprocating Internal Combustion Engines (RICE)
40CFR§63.6580-§63.6675 [Applicable/Exempt]
This rule does apply to the 5,000 bhp CAT G3616LE A4 (CE-01 thru CE-04) compressor engines. However, because each engine is “new” (i.e., commenced construction or reconstruction on or after 06/12/06) (§63.6590(a)(2)(iii)); the only requirement is compliance with §60.4230-§60.4248 (NSPS JJJJ) for Spark Ignition Internal Combustion Engines.
19. NESHAP DDDDD, Industrial, Commercial, and Institutional Boilers and Process
Heaters – Major Sources
40CFR§63.7480 – §63.7575 [Not Applicable]
This rule does not apply because the facility is not a major source of HAP emissions (§63.7485).
20. NESHAP JJJJJJ, Industrial, Commercial, and Institutional Boilers and Process
Heaters – Area Sources
40CFR§63.11193 – §63.11237 [Not Applicable]
This rule does not apply because the gas-fired reboiler (RBV) does not meet the definition of “boiler” in §63.11237. Specifically, “boiler” is defined as an enclosed device using controlled flame combustion in which water is heated to recover thermal energy in the form of steam and/or hot water. Furthermore, waste heat boilers, process heaters, and autoclaves are excluded from the definition of “boiler”.
Supplement – Page 8 of 11
21. Compliance Assurance Monitoring (CAM)
40CFR§64.1-§64.10 [Not Applicable]
This rule does not apply because the facility is not a major source required to obtain a Title V Operating Permit (§64.2(a)).
22. Chemical Accident Prevention Provisions (Risk Management Plan (RMP))
40CFR§68.1-§68.220 [Not Applicable]
This rule does not apply because the facility does not store more than a threshold quantity of a regulated substance in a process. Specifically, “Prior to entry into a natural gas processing plant or a petroleum refining process unit, regulated substances in naturally occurring hydrocarbon mixtures need not be considered when determining whether more than a threshold quantity is present at a stationary source” (§68.115(b)(2)(iii)).
23. Mandatory Greenhouse Gases (GHG) Reporting
40CFR§98.1-§98.9 [Applicable]
This rule does apply because the CO2e emissions from all stationary sources combined within the hydrocarbon basin as defined in 40 CFR Part 98 is ≥ 25,000 metric ton/yr (§98.2(a)(3)).
Requirements include monitoring, recordkeeping, and annual reporting of GHG from stationary fuel combustion sources (§98.2(a)(3)).
E. Applicability of Source Aggregation
The operations of the facility have not been aggregated with any other gas production, midstream service facilities, or transportation operations because there are no other oil and gas facilities or operations that are both a) “contiguous and adjacent” and b) “under common control” to the facility.
F. Applicability of State Regulations
The following state regulations are potentially applicable to natural gas compressor stations. Applicability to the facility has been determined as follows:
1. Particulate Air Pollution from Combustion of Fuel in Indirect Heat Exchangers
§45CSR2 [Applicable]
This rule does apply; however, because the reboiler (RBV) has a maximum design heat input (MDHI) rating less than 10 MMBtu/hr, the only requirement is to limit visible emissions to less than 10% opacity during normal operations (§45-02-3.1). The reboiler combusts only natural gas which inherently conforms to the visible emission standards.
Supplement – Page 9 of 11
2. Prevent and Control the Discharge of Air Pollutants into the Open Air Which
Causes or Contributes to an Objectionable Odor or Odors
§45CSR4 [Applicable]
This rule does apply and states that an objectionable odor is an odor that is deemed objectionable when in the opinion of a duly authorized representative of the Air Pollution Control Commission (Division of Air Quality), based upon their investigations and complaints, such odor is objectionable.
3. Control of Air Pollution from Combustion of Refuse
§45CSR6 [Applicable]
This rule does apply to the SSM Flare (FLR) and to the Thermal Oxidizer (TOx); however, these units combust waste from natural gas operations which inherently conforms to the particulate emission and opacity standards.
4. Prevent and Control Air Pollution from the Emission of Sulfur Oxides
§45CSR10 [Not Applicable]
This rule does not apply to the Compressor Engines (CE-01 thru CE-04), SSM Flare (FLR), Microturbine Generator (GT), Reboiler (RBV), Thermal Oxidizer (TOx), or any other fuel burning units, manufacturing process sources, or combustion sources because each combust only natural gas (§45-10A-3.1.b).
5. Permits for Construction, Modification, Relocation and Operation of Stationary
Sources of Air Pollutants, Notification Requirements, Administrative Updates,
Temporary Permits, General Permits, and Procedures for Evaluation
§45CSR13 [Applicable]
The rule does apply. Appalachia Midstream Services, LLC (AMS) is applying for G35-D General Permit Registration, has published the required Class I legal advertisement notifying the public of the application to construct and operate the facility, and paid the applicable fees to the WVDEP – Division of Air Quality.
6. Permits for Construction and Major Modification of Major Stationary Sources of
Air Pollutants for Prevention of Significant Deterioration
45CSR14 [Not Applicable]
The rule does not apply because the facility is neither a new PSD major source of pollutants nor is the proposed facility a modification to an existing PSD major source.
7. Standards of Performance for New Stationary Sources Pursuant to 40 CFR Part 60
45CSR16 [Applicable]
The rule does apply to this source by reference to §40CFR60 Subparts JJJJ and OOOOa. The facility is subject to the notification, testing, monitoring, recordkeeping and reporting requirements of these Subparts.
Supplement – Page 10 of 11
8. Permits for Construction and Major Modification of Major Stationary Sources of
Air Pollution Which Cause or Contribute to Nonattainment
45CSR19 [Not Applicable]
This rule does not apply because the facility is a minor (or “deferred”) source of all regulated pollutants.
9. Regulation of Volatile Organic Compounds (VOC)
45CSR21 [Not Applicable]
This rule does not apply because the facility is not located in Putnam, Kanawha, Cabell, Wayne, Wood, or Greenbrier Counties (§45-29-1).
10. Air Quality Management Fees Program
45CSR22 [Applicable]
This rule does apply. It establishes a program to collect fees for certificates to operate and for permits to construct, modify or relocate sources of air pollution.
11. Prevent and Control Emissions of Toxic Air Pollutants (Best Available Control Technology (BAT)) 45CSR27 [Not Applicable]
This rule does not apply because the equipment used in the production and distribution of petroleum products is exempt, provided the product contains no more than 5% benzene by weight (§45-27-2.4).
12. Air Pollution Emissions Banking and Trading
45CSR28 [Not Applicable]
This rule does not apply because the facility does not choose to participate in the voluntarily statewide air pollutant emissions trading program.
13. Emission Statements for VOC and NOX 45CSR29 [Not Applicable]
This rule does not apply because the facility is not located in Putnam, Kanawha, Cabell, Wayne, Wood, or Greenbrier Counties (§45-29-1).
14. Requirements for Operating Permits
45CSR30 [Not Applicable/Deferred]
This rule does not apply because the facility qualifies as a “Title V Synthetic Minor Source”.
Pursuant to the authority granted in West Virginia 45CSR§30-3.2 and 45CSR§30A-3.1, the DAQ is extending the deferral, which was set to expire December 15, 2000, of non-major sources to West Virginia 45CSR30 (Title V Program) from the obligation to submit an operating permit application.
Supplement – Page 11 of 11
15. Emission Standards for Hazardous Air Pollutants (HAP)
45CSR34 [Not Applicable]
This rule does not apply because the facility is an area source of HAP emissions. Note: The provisions under Subparts HH and ZZZZ of 40 CFR Part 63 which apply to non-major area sources of hazardous air pollutants are excluded.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Application for G35-D General Permit Registration
G35-D General Permit Registration Application
Section I General
Section II Certification of Information
Section III Operating Site Information
Section IV Attachments and Supporting Documents
OPERATING SITE INFORMATION
Briefly describe the proposed new operation and/or any change(s) to the facility: The Threedubs Compressor Station (3WCS) will be constructed and operated to compress and dehydrate natural gas. Directions to the facility: From Charles St in Wellsburg: 1) Head South on WV-2/Commerce St ~3.5 mi; 2) Turn Left onto 3rd St (Beech Bottom) ~0.2 mi; 3) Continue onto 49 Hill Rd ~0.8 mi; 4) Turn Right onto Apple Pie Ridge Rd ~2.7 mi; 5) Turn Left onto Grizzel Ln ~0.3 mi; 6) Destination is on the Right.
ATTACHMENTS AND SUPPORTING DOCUMENTS
I have enclosed the following required documents: Check payable to WVDEP – Division of Air Quality with the appropriate application fee (per 45CSR13 and 45CSR22). ☒ Check attached to front of application. ☐ I wish to pay by electronic transfer. Contact for payment (incl. name and email address):
☐ I wish to pay by credit card. Contact for payment (incl. name and email address):
☒$500 (Construction, Modification, and Relocation) ☐$300 (Class II Administrative Update) ☒$1,000 NSPS fee for 40 CFR60, Subpart IIII, JJJJ and/or OOOO and/or OOOOa1 ☒$2,500 NESHAP fee for 40 CFR63, Subpart ZZZZ and/or HH2
1 Only one NSPS fee will apply. 2 Only one NESHAP fee will apply. The Subpart ZZZZ NESHAP fee will be waived for new engines that satisfy
requirements by complying with NSPS, Subparts IIII and/or JJJJ. NSPS and NESHAP fees apply to new construction or if the source is being modified.
☒ Responsible Official or Authorized Representative Signature (if applicable)
☒ Single Source Determination Form (must be completed in its entirety) – Attachment A
☒ Siting Criteria Waiver (if applicable) – Attachment B ☒ Current Business Certificate – Attachment C
☒ Process Flow Diagram – Attachment D ☒ Process Description – Attachment E
☒ Plot Plan – Attachment F ☒ Area Map – Attachment G
☒ G35-D Section Applicability Form – Attachment H ☒ Emission Units/ERD Table – Attachment I
☒ Fugitive Emissions Summary Sheet – Attachment J
☒ Storage Vessel(s) Data Sheet (include gas sample data, USEPA Tanks, simulation software (e.g. ProMax, E&P Tanks, HYSYS, etc.), etc. where applicable) – Attachment K
☒ Natural Gas Fired Fuel Burning Unit(s) Data Sheet (GPUs, Heater Treaters, In-Line Heaters if applicable) – Attachment L
☒ Internal Combustion Engine Data Sheet(s) (include manufacturer performance data sheet(s) if applicable) – Attachment M
☒ Tanker Truck Loading Data Sheet (if applicable) – Attachment N
☒ Glycol Dehydration Unit Data Sheet(s) (include wet gas analysis, GRI- GLYCalcTM input and output reports and information on reboiler if applicable) – Attachment O
☒ Pneumatic Controllers Data Sheet – Attachment P
☒ Centrifugal Compressor Data Sheet – Attachment Q
☒ Reciprocating Compressor Data Sheet – Attachment R
☒ Blowdown and Pigging Operations Data Sheet – Attachment S
☒ Air Pollution Control Device/Emission Reduction Device(s) Sheet(s) (include manufacturer performance data sheet(s) if applicable) – Attachment T
☒ Emission Calculations (please be specific and include all calculation methodologies used) – Attachment U
☒ Facility-wide Emission Summary Sheet(s) – Attachment V
☒ Class I Legal Advertisement – Attachment W
☒ One (1) paper copy and two (2) copies of CD or DVD with pdf copy of application and attachments All attachments must be identified by name, divided into sections, and submitted in order.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachments
to Application for G35-D General Permit Registration
• Attachment A Single Source Determination Form
• Attachment B Siting Criteria Waiver (If Applicable)
• Attachment C Current Business Certificate
• Attachment D Process Flow Diagram(s) (PFD)
• Attachment E Process Description
• Attachment F Plot Plan
• Attachment G Area Map
• Attachment H G35-D Section Applicability Form
• Attachment I Emission Units/ERD Table
• Attachment J Fugitive Emissions Summary Sheet(s)
• Attachment K Storage Vessel(s)Data Sheet
• Attachment L Natural Gas Fired Fuel Burning Unit(s) Data Sheet
• Attachment M Internal Combustion Engine Data Sheet(s)
• Attachment N Tanker Truck Loading Data Sheet (If Applicable)
• Attachment O Glycol Dehydration Unit Data Sheet(s)
• Attachment P Pneumatic Controllers Data Sheet(s)
• Attachment Q Centrifugal Compressor Data Sheet(s)
• Attachment R Reciprocating Compressor Data Sheet(s)
• Attachment S Blowdown and Pigging Operations Data Sheet(s)
• Attachment T Air Pollution Control Device/Emission Reduction Device(s)
• Attachment U Emission Calculations
• Attachment V Facility-wide Emission Summary Sheet(s)
• Attachment W Class I Legal Advertisement
Attachment A
Single Source Determination Form
ATTACHMENT A - SINGLE SOURCE DETERMINATION FORM Classifying multiple facilities as one “stationary source” under 45CSR13, 45CSR14, and 45CSR19 is based on the definition of Building, structure, facility, or installation as given in §45-14-2.13 and §45-19-2.12. The definition states:“Building, Structure, Facility, or Installation” means all of the pollutant-emitting activities which belong to the same industrial grouping, and are located on one or more contiguous or adjacent properties, and are under the control of the same person (or persons under common control). Pollutant-emitting activities are a part of the same industrial grouping if they belong to the same “Major Group” (i.e., which have the same two (2)-digit code) as described in the Standard Industrial Classification Manual, 1987 (United States Government Printing Office stock number GPO 1987 0-185-718:QL 3). The Source Determination Rule for the oil and gas industry was published in the Federal Register on June 3, 2016 and will become effective on August 2, 2016. EPA defined the term “adjacent” and stated that equipment and activities in the oil and gas sector that are under common control will be considered part of the same source if they are located on the same site or on sites that share equipment and are within ¼ mile of each other.
Is there equipment and activities in the same industrial grouping (defined by SIC code)? Yes ☒ No ☐
(The upstream well(s) and the subject facility all share the same two-digit major SIC code of 13.)
Is there equipment and activities under the control of the same person/people? Yes ☐ No ☒
(The subject facility receives raw natural gas from wells owned and/or operated (i.e.,“controlled”) by other companies.)
Is there equipment and activities located on the same site or on sites that share equipment and are within ¼ mile of each other? Yes ☐ No ☒
(The nearest facility under “common control” is the Pioneer Compressor Station located approx. 3.7 mi to the S-SE.)
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment B
Siting Criteria Waiver (If Applicable)
ATTACHMENT B - SITING CRITERIA WAIVER – NOT APPLICABLE
If applicable, please complete this form and it must be notarized.
G35-D General Permit
Siting Criteria Waiver
WV Division of Air Quality 300’ Waiver
I ________________________________________________ hereby Print Name
acknowledge and agree that _______________________________________ will General Permit Applicant’s Name
construct an emission unit(s) at a natural gas compressor and/or dehydration facility
that will be located within 300’ of my dwelling and/or business.
I hereby offer this waiver of siting criteria to the West Virginia Department of Environmental Protection
Division of Air Quality as permission to construct, install and operate in such location.
Signed:
______________________________________________________________ Signature Date
______________________________________________________________
Signature Date
Taken, subscribed and sworn before me this _____ day of _________________, 20_____.
My commission expires: ________________________
SEAL__________________________________________________ Notary Public
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment C
Current Business Certificate
ATTACHMENT C – CURRENT BUSINESS CERTIFICATE
If the applicant is a resident of West Virginia, the applicant should provide a copy of the
current Business Registration Certificate issued to them from the West Virginia Secretary of
State’s Office. If the applicant is not a resident of the State of West Virginia, the registrant
should provide a copy of the Certificate of Authority/Authority of LLC/Registration. This
information is required for all sources to operate a business in West Virginia regardless of
whether it is a construction, modification, or administrative update.
If you are a new business to West Virginia and have applied to the West Virginia Secretary of
State’s Office for a business license, please include a copy of your application.
Please note: Under the West Virginia Bureau of Employment Programs, 96CSR1, the DAQ
may not grant, issue, or renew approval of any permit, general permit registration, or
Certificate to Operate to any employing unit whose account is in default with the Bureau of
Employment Programs Unemployment Compensation Division.
Business Registration Certificate
To: Appalachia Midstream Services, LLC
Date: June 30, 2010
Attachment D
Process Flow Diagram(s) (PFD)
ATTACHMENT D – PROCESS FLOW DIAGRAM Provide a diagram or schematic that supplements the process description of the operation. The process flow diagram must show all sources, components or facets of the operation in an understandable line sequence of operation. The process flow diagram should include the emission unit ID numbers, the pollution control device ID numbers, and the emission point ID numbers consistent with references in other attachments of the application. For a proposed modification, clearly identify the process areas, emission units, emission points, and/or control devices that will be modified, and specify the nature and extent of the modification.
Use the following guidelines to ensure a complete process flow diagram:
The process flow diagram shall logically follow the entire process from beginning toend.
Identify each emission source and air pollution control device with proper andconsistent emission unit identification numbers, emission point identification numbers,and control device identification numbers.
The process flow lines may appear different for clarity. For example, dotted lines maybe used for vapor flow and solid lines used for liquid flow and arrows for direction offlow.
The process flow lines may be color coded. For example: new or modified equipmentmay be red; old or existing equipment may be blue; different stages of preparation suchas raw material may be green; and, finished product or refuse, another color.
~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Air Defender
Carbon Filtration
Oxy
gen
Microtubine
Generator
(CT-01 (8E))
Hydrocarbon Liquids
Emission Stream:
Other Flows:
Product Flow:
Gas Flow:
SSM Flare
(FLR (7E))
Thermal
Oxidizer
(TOx (12E))
Vapor Recovery
Unit (VRU)
(Electric)
Stabilized Condensate
Truck Load-Out
(TLO (21E))
Condensate
Stabilizer
(Electric Heat )
Stabilized Condensate Storage
Tanks
(TK-01 (13E) thru TK-06 (18E))
COMPRESSED AND
DEHYDRATED GAS
TO PIPELINEInlet Gas
Process and Piping Emissions
(FUG-G (1F) and FUG-L (2F))
Produced Water
Truck Load-Out
(TLO (21E))
Three Phase Separator
(Totally Enclosed)
ProducedWater
Attachment D - Process Flow Diagram (PFD)
Appalachia Midstream Services, LLC (AMS)
Threedubs Compressor Station (3WCS)
Attachment D - Process Flow Diagram (PFD)
Produced Water Storage Tanks
(TK-07 (19E) and TK-08 (20E))
Deh
ydra
tor F
lash
Tan
k a
nd S
till V
ent S
tream
s
Produced Water/Hydrocarbon Liquids
Blow
dow
ns(C
BD, E
SD, P
IG)
Application for G35-D General Permit Registration
Engine Crankcase Leaks
(ECC (3F))
Inlet Separator
Compressors and Engines
(CE-01 (1E) thru CE-04 (4E),
CRP (5E), and SSM (6E))
Dehydrator and Reboiler
(DFT (9E), DSV (10E),
and RBV (11E))
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment E
Process Description
ATTACHMENT E – PROCESS DESCRIPTION
Provide a detailed written description of the operation for which the applicant is seeking a
permit. The process description is used in conjunction with the process flow diagram to
provide the reviewing engineer a complete understanding of the activity at the operation.
Describe in detail and order the complete process operation.
Use the following guidelines to ensure a complete Process Description:
▪ The process flow diagram should be prepared first and used as a guide when preparing
the process description. The written description shall follow the logical order of the
process flow diagram.
▪ All emission sources, emission points, and air pollution control devices must be
included in the process description.
▪ When modifications are proposed, describe the modifications and the effect the
changes will have on the emission sources, emission points, control devices and the
potential emissions.
▪ Proper emission source ID numbers must be used consistently in the process
description, the process flow diagram, the emissions calculations, and the emissions
summary information provided.
▪ Include any additional information that may facilitate the reviewers understanding of
the process operation.
The process description is required for all sources regardless of whether it is a construction,
modification, or administrative update.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Attachment E
Process Description
A. Project Overview
Appalachia Midstream Services, LLC (AMS) proposes to construct and operate the grassroots Threedubs Compressor Station (3WCS) to be located at the end of Grizzel Ln, approximately 0.3 miles East of Apple Pie Ridge Rd, Wellsburg, in Brooke County, West Virginia. (See Attachment G – Area Map). The facility receives natural gas from local production wells then compresses and dehydrates the gas for delivery to a gathering pipeline.
Additionally, raw field condensate is received at the site, stabilized and then sent offsite via tanker trucks.
B. Compressor Engines (CE-01 thru CE-04)
Four (4) natural gas-fueled reciprocating engines are utilized at the facility. These engines drive a natural gas compressor to increase the pressure of the natural gas. Emissions result from the combustion of natural gas fuel.
C. Compressor Rod Packing Leaks (CRP)
The reciprocating compressor operations result in emissions from the wear of mechanical seals around the piston rods over time.
D. Startup/Shutdown/Maintenance (SSM)
As part of facility operation, the compressor engines will undergo periods of startup and shutdown. When an engine is shutdown, the natural gas contained within the compressor and associated piping must be evacuated (compressor blowdown, CBD) and the blowdown gas will be routed to the flare for destruction. Additionally, there will be other infrequent emissions from various maintenance activities at the facility that are not associated with compressor blowdowns such as emergency shutdown (ESD) testing and pigging operations (PIG).
E. SSM Flare (FLR)
One (1) process flare with 98% VOC/HAPs destruction efficiency is used to control emissions from startup/shutdown/maintenance (SSM) activities (including compressor blowdown (CBD), emergency shutdown (ESD) testing, and pigging operations (PIG).
F. Microturbine Generator (GT)
One (1) natural gas-fueled microturbine generator will be utilized to provide electrical power to the facility.
G. Tri-Ethylene Glycol (TEG) Dehydrator (DHY - DFT and DSV)
One (1) Triethylene Glycol (TEG) Dehydrator will be utilized at the facility. The dehydrator is comprised of a Contactor/Absorber Tower (no vented emissions), a Flash Tank (DFT), and a Regenerator/Still Vent (DSV).
The TEG Dehydrator is used to remove water vapor from the inlet wet gas stream to meet pipeline specifications. In the dehydration process, the wet inlet gas stream flows through a contactor tower where the gas is contacted with lean glycol. The lean glycol absorbs the water in the gas stream and becomes rich glycol laden with water and trace amounts of hydrocarbons.
The rich glycol is then routed to a flash tank where the glycol pressure is reduced to liberate the lighter end hydrocarbons (especially methane). The lighter end hydrocarbons are routed from the flash tank to the reboiler for use as fuel with the excess hydrocarbons vented to a thermal oxidizer.
The rich glycol is then sent from the flash tank to the regenerator/still where the TEG is heated to drive off the water vapor and any remaining hydrocarbons. The off-gases from the regenerator/still are vented to a thermal oxidizer.
After regeneration, the glycol is returned to a lean state and used again in the process.
H. Reboiler (RBV)
One (1) gas-fueled reboiler will be utilized to supply heat to the Regenerator/Still.
I. Thermal Oxidizer (TOx)
One (1) thermal oxidizer with 98% VOC/HAPs destruction efficiency is used to control the dehydrator’s flash gas and still vent vapor streams.
J. Condensate Stabilizer
An electrically heated 3-phase separator will separate gas vapor, water, and condensate. Water will go to the produced water tanks. Raw condensate from the 3-phase separator will be sent to a stabilizer tower skid to stabilize the condensate to an RVP 12 product. An electric immersion heater will be used to provide the heat necessary to stabilize the condensate.
K. Storage Tanks (TK-01 thru TK-08, Misc. Tanks)
Six (6) 400 bbl storage tanks will be used to hold the stabilized condensate from the condensate stabilizer and two (2) 400 bbl storage tanks will be used to hold the produced water from the inlet separator and the dehydrator. Gas vapor from these tanks will be routed to an electric motor driven vapor recovery unit (VRU). The VRU will discharge into the compressor facility suction line.
There are also tanks at the facility used to store various materials, including fresh and used lube oil, fresh and spent TEG, etc. Each of these misc. storage tanks generate de-minimis (insignificant) emissions.
Attachment E – Process Description – Page 03 of 03
L. Truck Load-Out (TLO)
Loading of stabilized condensate and produced water into tanker trucks will occur at the facility. In condensate truck-loading facilities, the introduction of oxygen into the vapor space can create a dangerous explosive environment. An Air Defender system eliminates the problem by using carbon-bed based technology to treat the vapor produced during truck-loading operations and puts oxygen free hydrocarbon vapors back into the system. The Air Defender along with use of a Vapor Recovery Unit (VRU) will help to minimize VOC and HAP emissions from truck loading activities.
M. Piping and Equipment Fugitive Emissions
Piping and process equipment will generate from leaks from different component types (connectors, valves, pumps, etc.) in gas-vapor service and light-liquid (condensate) service.
N. Engine Crankcase Emissions (ECC)
Internal combustion results in a small but continual amount of blow-by, which occurs when some of the gases from combustion leak past the piston rings (that is, blow-by them) to end up inside the crankcase, causing pressure to build up in the crank case. These blow-by gases are vented to the atmosphere.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment F
Plot Plan
ATTACHMENT F – PLOT PLAN
Provide an accurately scaled and detailed Plot Plan showing the locations of all emission units,
emission points, and air pollution control devices. Show all emission units, affected facilities,
enclosures, buildings and plant entrances and exits from the nearest public road(s) as
appropriate. Note height, width and length of proposed or existing buildings and structures.
A scale between 1"=10' and 1"=200' should be used with the determining factor being the
level of detail necessary to show operation or plant areas, affected facilities, emission unit
sources, transfer points, etc. An overall small-scale plot plan (e.g., 1"=300') should be
submitted in addition to larger scale plot plans for process or activity areas (e.g., 1"=50') if the
plant is too large to allow adequate detail on a single plot plan. Process or activity areas may
be grouped for the enlargements as long as sufficient detail is shown.
Use the following guidelines to ensure a complete Plot Plan:
▪ Facility name
▪ Company name
▪ Company facility ID number (for existing facilities)
▪ Plot scale, north arrow, date drawn, and submittal date.
▪ Facility boundary lines
▪ Base elevation
▪ Lat/Long reference coordinates from the area map and corresponding reference point
elevation
▪ Location of all point sources labeled with proper and consistent source identification
numbers
This information is required for all sources regardless of whether it is a construction,
modification, or administrative update.
Threedubs Compressor Station (3WCS) Attachment F - Plot Plan Application for G35-D General Permit Registration
Appalachia Midstream Services, LLC (AMS)
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Attachment F - Plot Plan
Attachment G
Area Map
ATTACHMENT G – AREA MAP Provide an Area Map showing the current or proposed location of the operation. On this map, identify plant or operation property lines, access roads and any adjacent dwelling, business, public building, school, church, cemetery, community or institutional building or public park within a 300’ boundary circle of the collective emission units.
Please provide a 300’ boundary circle on the map surrounding the proposed emission units collectively.
This information is required for all sources regardless of whether it is a construction, modification, or administrative update.
Attachment G - Location Map Application for G35-D General Permit RegistrationThreedubs Compressor Station (3WCS)
Appalachia Midstream Services, LLC (AMS)
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Attachment G - Location Map
From Charles St in Wellsburg: 1) Head South on WV-2/Commerce St ~3.5 mi;2) Turn Left onto 3rd St (Beech Bottom) ~0.2 mi;3) Continue onto 49 Hill Rd ~0.8 mi;4) Turn Right onto Apple Pie Ridge Rd ~2.7 mi;5) Turn Left onto Grizzel Ln ~0.3 mi;6) Destination is on the Right.
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
End of Grizzel Ln (~0.3 mi East of Apple Pie Ridge Rd)Wellsburg, in Brooke County, WV 26070Lat: 40°11'34.0"N x Lon: -80°37'07.0"W
Lat: 40.19278°N x -80.61861°WUTM: 532.46 km E x 4,449.22 km N x 17T
2016 USGS US Topo 7.5 - minute map for TILTONSVILLE, OH-WV2016 USGS US Topo 7.5 - minute map for BETHANY, WV-PA
Threedubs Compressor Station (3WCS) Attachment G - Area Map Application for G35-D General Permit Registration
Appalachia Midstream Services, LLC (AMS)
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Attachment G - Area Map
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
End of Grizzel Ln (~0.3 mi East of Apple Pie Ridge Rd)Wellsburg, in Brooke County, WV 26070Lat: 40°11'34.0"N x Lon: -80°37'07.0"W
Lat: 40.19278°N x -80.61861°WUTM: 532.46 km E x 4,449.22 km N x 17T
2016 USGS US Topo 7.5 - minute map for TILTONSVILLE, OH-WV2016 USGS US Topo 7.5 - minute map for BETHANY, WV-PA
Elevation: ~1,185'
Fenceline
300' Boundary
All of the existing "dwellings and/or businesses"w/in the 300' Boundary are owned by the applicant
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment H
Applicability Form
ATTACHMENT H – G35-D SECTION APPLICABILITY FORM
General Permit G35-D was developed to allow qualified applicants to seek registration for a
variety of sources. These sources include storage vessels, gas production units, in-line heaters,
heater treaters, glycol dehydration units and associated reboilers, pneumatic controllers,
centrifugal compressors, reciprocating compressors, reciprocating internal combustion engines
(RICEs), tank truck loading, fugitive emissions, completion combustion devices, flares, enclosed
combustion devices, and vapor recovery systems. All registered facilities will be subject to
Sections 1.0, 2.0, 3.0, and 4.0.
General Permit G35-D allows the registrant to choose which sections of the permit they are
seeking registration under. Therefore, please mark which additional sections that you are
applying for registration under. If the applicant is seeking registration under multiple sections,
please select all that apply. Please keep in mind, that if this registration is approved, the issued
registration will state which sections will apply to your affected facility.
GENERAL PERMIT G35-D APPLICABLE SECTIONS
☒Section 5.0 Storage Vessels Containing Condensate and/or Produced Water1 (Att K)
☐Section 6.0 Storage Vessel Affected Facility (NSPS, Subpart OOOO/OOOOa) (Att K)
☒Section 7.0 Control Devices and Emission Reduction Devices not subject to NSPS Subpart
OOOO/OOOOa and/or NESHAP Subpart HH (Att T)
☒Section 8.0 Small Heaters and Reboilers not subject to 40CFR60 Subpart Dc (Att L)
☐Section 9.0 Pneumatic Controllers Affected Facility (NSPS, Subpart OOOO/OOOOa) (Att P)
☐Section 10.0 Centrifugal Compressor Affected Facility (NSPS, Subpart OOOO/OOOOa)2 (Att Q)
☒Section 11.0 Reciprocating Compressor Affected Facility (NSPS, Subpart OOOO/OOOOa)2 (Att R)
☒Section 12.0 Reciprocating Internal Combustion Engines, Generator Engines, and Microturbine
Generators (Att M)
☒Section 13.0 Tanker Truck Loading3 (Att N)
☒Section 14.0 Glycol Dehydration Units4 (Att O)
☒Section 15.0 Blowdown and Pigging Operations (Att S)
☒Section 16.0 Fugitive Emission Components (NSPS, Subpart OOOOa) (Att J)
1 Applicants that are subject to Section 5 may also be subject to Section 6 if the applicant is subject to the NSPS,
Subpart OOOO/OOOOa control requirements or the applicable control device requirements of Section 7.
2 Applicants that are subject to Section 10 and 11 may also be subject to the applicable RICE requirements of
Section 12.
3 Applicants that are subject to Section 13 may also be subject to control device and emission reduction device
requirements of Section 7.
4 Applicants that are subject to Section 14 may also be subject to the requirements of Section 8 (reboilers). Applicants that are subject to Section 14 may also be subject to control device and emission reduction device
requirements of Section 7.
Attachment I
Emission Units/ERD Table
CE-01 1E Compressor Engine 01 - CAT G3616LE A4 TBD TBD 5,000 bhp NEW OxCat-01
CE-02 2E Compressor Engine 02 - CAT G3616LE A4 TBD TBD 5,000 bhp NEW OxCat-02
CE-03 3E Compressor Engine 03 - CAT G3616LE A4 TBD TBD 5,000 bhp NEW OxCat-03
CE-04 4E Compressor Engine 04 - CAT G3616LE A4 TBD TBD 5,000 bhp NEW OxCat-04
CRP 5E Compressor Rod Packing TBD TBD 5 Recip's NEW ---
Compressor Blowdown (CBD) 422 Events/yr
Emergency Shutdown (ESD) Testing 1 Event/yr
Pigging Operations (PIG) 156 Events/yr
FLR 7E SSM Flare - Zeeco MJ-16 (Comb. Only) TBD TBD 3.49 MMBtu/hr NEW ---
GT 8E Microturbine Generator - FlexEnergy GT1300S TBD TBD 1,742 bhp NEW ---
DFT 9E Dehydrator - Flash Tank
DSV 10E Dehydrator - Still Vent
RBV 11E Dehydrator - Reboiler Vent TBD TBD 2.0 MMBtu/hr NEW ---
TOx 12E Thermal Oxidizer - Zeeco Z-HTO (Comb. Only) TBD TBD 6.21 MMBtu/hr NEW ---
TK-01 13E Storage Tank 01 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-02 14E Storage Tank 02 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-03 15E Storage Tank 03 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-04 16E Storage Tank 04 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-05 17E Storage Tank 05 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-06 18E Storage Tank 06 - Stabilized Condensate TBD TBD 400 bbl NEW
TK-07 19E Storage Tank 07 - Produced Water TBD TBD 400 bbl NEW
TK-08 20E Storage Tank 08 - Produced Water TBD TBD 400 bbl NEW
Truck Load-Out - Stabilized Condensate 228,000 bbl/yr
Truck Load-Out - Produced Water 30,000 bbl/yr
Manufac.Date3
ControlDevice(s)5
1 For Emission Units (or Sources) use the following numbering system:1S, 2S, 3S,... or other appropriate designation.2 For Emission Points use the following numbering system:1E, 2E, 3E, ... or other appropriate designation.3 When required by rule4 New, modification, removal, existing 5 For Control Devices use the following numbering system: 1C, 2C, 3C,... or other appropriate designation.6 For ERDs use the following numbering system: 1D, 2D, 3D,... or other appropriate designation.
ATTACHMENT I - EMISSION UNITS / EMISSION REDUCTION DEVICES (ERD) TABLE
NEWTBDTBD21ETLO
VRU
TOxNEWTBD
6ESSM
TBD
ATTACHMENT I - EMISSION UNITS / EMISSION REDUCTION DEVICES (ERD) TABLE
MMscfd200
Include ALL emission units and air pollution control devices/ERDs that will be part of this permit application review. Do not include fugitive emission sourcesin this table. De-minimis storage tanks shall be listed in the Attachment K table. This information is required for all sources regardless of whether it is a construction, modification, or administrative update.
ERD(s)6Year Installed
Emission Point ID2
Emission Unit ID1
Emission Unit Description
DesignCapacity
Type4 and Date of Change
---NEWTBDTBD
Attachment J
Fugitive Emissions Summary Sheet(s)
12
ATTACHMENT J – FUGITIVE EMISSIONS SUMMARY SHEET Sources of fugitive emissions may include loading operations, equipment leaks, blowdown emissions, etc.
Use extra pages for each associated source or equipment if necessary. Source/Equipment: FUG-G/FUG-L
Leak Detection Method Used ☐ Audible, visual, and olfactory (AVO) inspections ☐ Infrared (FLIR) cameras ☐ Other (please describe) ☐ None
required Is the facility subject to quarterly LDAR monitoring under 40CFR60 Subpart OOOOa? ☒ Yes ☐ No. If no, why?
Component Type
Closed Vent
System Count Source of Leak Factors
(EPA, other (specify))
Stream type (gas, liquid,
etc.)
Estimated Emissions (tpy)
VOC HAP GHG (CO2e)
Pumps ☐ Yes ☒ No 14
EPA Protocol for Equipment Leak Emissions. Table 2-4
(EPA-453/R-95-017, 1995)
☐ Gas ☒ Liquid ☐ Both
0.45 0.06 ---
Valves ☐ Yes ☒ No
1,843 EPA Protocol for Equipment Leak Emissions.
Table 2-4 (EPA-453/R-95-017, 1995)
☐ Gas ☐ Liquid ☒ Both
3.05 0.31 53.41
Safety Relief Valves
☐ Yes ☐ No
☐ Gas
☐ Liquid ☐ Both
Open Ended Lines
☐ Yes ☒ No
65 EPA Protocol for Equipment Leak Emissions.
Table 2-4 (EPA-453/R-95-017, 1995)
☐ Gas ☐ Liquid ☒ Both
0.53 0.05 10.51
Sampling Connections
☐ Yes ☐ No
☐ Gas
☐ Liquid ☐ Both
Connections (Not sampling)
☐ Yes ☒ No
5,315 EPA Protocol for Equipment Leak Emissions.
Table 2-4 (EPA-453/R-95-017, 1995)
☐ Gas ☐ Liquid ☒ Both
0.35 0.03 6.78
Compressors ☐ Yes ☐ No
☐ Gas
☐ Liquid ☐ Both
Flanges ☐ Yes ☒ No
1,328 EPA Protocol for Equipment Leak Emissions.
Table 2-4 (EPA-453/R-95-017, 1995)
☐ Gas ☐ Liquid ☒ Both
1.34 0.08 47.20
Other1 ☐ Yes ☒ No
138 EPA Protocol for Equipment Leak Emissions.
Table 2-4 (EPA-453/R-95-017, 1995)
☐ Gas ☐ Liquid ☒ Both
5.66 0.58 97.93
1 Other equipment types may include compressor seals, relief valves, diaphragms, drains, meters, etc. Please indicate if there are any closed vent bypasses (include component): na
Specify all equipment used in the closed vent system (e.g. VRU, ERD, thief hatches, tanker truck loading, etc.) na
Attachment K
Storage Vessel(s) Data Sheet
13
ATTACHMENT K – STORAGE VESSEL DATA SHEET
Complete this data sheet if you are the owner or operator of a storage vessel that contains condensate and/or produced water. This form must be completed for each new or modified bulk liquid storage vessel(s) that contains condensate and/or produced water. (If you have more than one (1) identical tank (i.e. 4-400 bbl condensate tanks), then you can list all on one (1) data sheet). Include gas sample analysis, flashing emissions, working and breathing losses, USEPA Tanks, simulation software (ProMax, E&P Tanks, HYSYS, etc.), and any other supporting documents where applicable. The following information is REQUIRED: ☐ Composition of the representative sample used for the simulation ☐ For each stream that contributes to flashing emissions: ☐ Temperature and pressure (inlet and outlet from separator(s)) ☐ Simulation-predicted composition ☐ Molecular weight ☐ Flow rate ☐ Resulting flash emission factor or flashing emissions from simulation ☒ Working/breathing loss emissions from tanks and/or loading emissions if simulation is used to quantify those emissions Additional information may be requested if necessary.
GENERAL INFORMATION
1. Bulk Storage Area Name Threedubs Compressor Station (3WCS)
2. Tank Name 6 x 400 bbl Stabilized Condensate
Tanks 2. Emission Unit ID number
TK-01 thru TK-06
3. Emission Point ID number 13E thru 18E
5. Date Installed, Modified or Relocated (for existing tanks) TBD
Was the tank manufactured after August 23, 2011? ☒ Yes ☐ No
6. Type of change: ☒ New construction ☐ New stored material ☐ Other ☐ Relocation
7A. Description of Tank Modification (if applicable) na 7B. Will more than one material be stored in this tank? If so, a separate form must be completed for each material. ☒ Yes ☐ No (Six (6) tanks will normally store stabilized condensate; however, they may also store produced
water. Emissions for each of the six (6) tanks are based on storage of stabilize condensate as
this produces the highest emissions.) 7C. Was USEPA Tanks simulation software utilized? ☒ Yes ☐ No (Please refer to Appendix S5 – Emission Programs) If Yes, please provide the appropriate documentation and items 8-42 below are not required.
14
TANK INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs
8. Design Capacity (specify barrels or gallons). Use the internal cross-sectional area multiplied by internal height.
9A. Tank Internal Diameter (ft.) 9B. Tank Internal Height (ft.)
10A. Maximum Liquid Height (ft.) 10B. Average Liquid Height (ft.)
11A. Maximum Vapor Space Height (ft.) 11B. Average Vapor Space Height (ft.)
12. Nominal Capacity (specify barrels or gallons). This is also known as “working volume”.
13A. Maximum annual throughput (gal/yr) 13B. Maximum daily throughput (gal/day)
14. Number of tank turnovers per year 15. Maximum tank fill rate (gal/min)
16. Tank fill method ☐ Submerged ☐ Splash ☐ Bottom Loading
17. Is the tank system a variable vapor space system? ☐ Yes ☐ No
If yes, (A) What is the volume expansion capacity of the system (gal)?
(B) What are the number of transfers into the system per year?
18. Type of tank (check all that apply):
☐ Fixed Roof ☐ vertical ☐ horizontal ☐ flat roof ☐ cone roof ☐ dome roof ☐ other (describe)
☐ External Floating Roof ☐ pontoon roof ☐ double deck roof
☐ Domed External (or Covered) Floating Roof
☐ Internal Floating Roof ☐ vertical column support ☐ self-supporting
☐ Variable Vapor Space ☐ lifter roof ☐ diaphragm
☐ Pressurized ☐ spherical ☐ cylindrical
☐ Other (describe)
PRESSURE/VACUUM CONTROL DATA – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs
19. Check as many as apply:
☐ Does Not Apply ☐ Rupture Disc (psig)
☐ Inert Gas Blanket of _____________ ☐ Carbon Adsorption1
☐ Vent to Vapor Combustion Device1 (vapor combustors, flares, thermal oxidizers, enclosed combustors)
☐ Conservation Vent (psig) ☐ Condenser1
Vacuum Setting Pressure Setting
☐ Emergency Relief Valve (psig)
Vacuum Setting Pressure Setting
☐ Thief Hatch Weighted ☐ Yes ☐ No
1 Complete appropriate Air Pollution Control Device Sheet
20. Expected Emission Rate (submit Test Data or Calculations here or elsewhere in the application).
Material Name
Flashing Loss Breathing Loss Working Loss Total
Emissions Loss
Estimation Method1
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
1 EPA = EPA Emission Factor, MB = Material Balance, SS = Similar Source, ST = Similar Source Test, Throughput Data, O = Other (specify)
Remember to attach emissions calculations, including TANKS Summary Sheets and other modeling summary sheets if applicable.
15
TANK CONSTRUCTION AND OPERATION INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5
21. Tank Shell Construction:
☐ Riveted ☐ Gunite lined ☐ Epoxy-coated rivets ☐ Other (describe)
21A. Shell Color: 21B. Roof Color: 21C. Year Last Painted:
22. Shell Condition (if metal and unlined):
☐ No Rust ☐ Light Rust ☐ Dense Rust ☐ Not applicable
22A. Is the tank heated? ☐ Yes ☐ No 22B. If yes, operating temperature:
22C. If yes, how is heat provided to tank?
23. Operating Pressure Range (psig):
Must be listed for tanks using VRUs with closed vent system.
24. Is the tank a Vertical Fixed Roof Tank?
☐ Yes ☐ No
24A. If yes, for dome roof provide radius (ft):
24B. If yes, for cone roof, provide slop (ft/ft):
25. Complete item 25 for Floating Roof Tanks ☐ Does not apply ☐
25A. Year Internal Floaters Installed:
25B. Primary Seal Type (check one): ☐ Metallic (mechanical) shoe seal ☐ Liquid mounted resilient seal
☐ Vapor mounted resilient seal ☐ Other (describe):
25C. Is the Floating Roof equipped with a secondary seal? ☐ Yes ☐ No
25D. If yes, how is the secondary seal mounted? (check one) ☐ Shoe ☐ Rim ☐ Other (describe):
25E. Is the floating roof equipped with a weather shield? ☐ Yes ☐ No
25F. Describe deck fittings:
26. Complete the following section for Internal Floating Roof Tanks ☐ Does not apply
26A. Deck Type: ☐ Bolted ☐ Welded 26B. For bolted decks, provide deck construction:
26C. Deck seam. Continuous sheet construction:
☐ 5 ft. wide ☐ 6 ft. wide ☐ 7 ft. wide ☐ 5 x 7.5 ft. wide ☐ 5 x 12 ft. wide ☐ other (describe)
26D. Deck seam length (ft.):
26E. Area of deck (ft2):
26F. For column supported
tanks, # of columns:
26G. For column supported
tanks, diameter of column:
27. Closed Vent System with VRU? ☐ Yes ☐ No
28. Closed Vent System with Enclosed Combustor? ☐ Yes ☐ No
SITE INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs
29. Provide the city and state on which the data in this section are based:
30. Daily Avg. Ambient Temperature (°F): 31. Annual Avg. Maximum Temperature (°F):
32. Annual Avg. Minimum Temperature (°F): 33. Avg. Wind Speed (mph):
34. Annual Avg. Solar Insulation Factor (BTU/ft2-day): 35. Atmospheric Pressure (psia):
LIQUID INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs
36. Avg. daily temperature range of bulk
liquid (°F):
36A. Minimum (°F): 36B. Maximum (°F):
37. Avg. operating pressure range of tank
(psig):
37A. Minimum (psig): 37B. Maximum (psig):
38A. Minimum liquid surface temperature (°F): 38B. Corresponding vapor pressure (psia):
39A. Avg. liquid surface temperature (°F): 39B. Corresponding vapor pressure (psia):
40A. Maximum liquid surface temperature (°F): 40B. Corresponding vapor pressure (psia):
41. Provide the following for each liquid or gas to be stored in the tank. Add additional pages if necessary.
41A. Material name and composition:
41B. CAS number:
41C. Liquid density (lb/gal):
41D. Liquid molecular weight (lb/lb-mole):
41E. Vapor molecular weight (lb/lb-mole):
41F. Maximum true vapor pressure (psia):
41G. Maximum Reid vapor pressure (psia):
41H. Months Storage per year.
From: To:
42. Final maximum gauge pressure and
temperature prior to transfer into tank used as
inputs into flashing emission calculations.
16
ATTACHMENT K – STORAGE VESSEL DATA SHEET Complete this data sheet if you are the owner or operator of a storage vessel that contains condensate and/or produced water. This form must be completed for each new or modified bulk liquid storage vessel(s) that contains condensate and/or produced water. (If you have more than one (1) identical tank (i.e. 4-400 bbl condensate tanks), then you can list all on one (1) data sheet). Include gas sample analysis, flashing emissions, working and breathing losses, USEPA Tanks, simulation software (ProMax, E&P Tanks, HYSYS, etc.), and any other supporting documents where applicable. The following information is REQUIRED: ☐ Composition of the representative sample used for the simulation ☐ For each stream that contributes to flashing emissions: ☐ Temperature and pressure (inlet and outlet from separator(s)) ☐ Simulation-predicted composition ☐ Molecular weight ☐ Flow rate ☐ Resulting flash emission factor or flashing emissions from simulation ☒ Working/breathing loss emissions from tanks and/or loading emissions if simulation is used to quantify those emissions Additional information may be requested if necessary.
GENERAL INFORMATION
4. Bulk Storage Area Name Threedubs Compressor Station (3WCS)
2. Tank Name 2 x 400 bbl Produced Water Tanks
5. Emission Unit ID number TK-07 thru TK-08
6. Emission Point ID number 19E thru 20E
5. Date Installed, Modified or Relocated (for existing tanks) TBD
Was the tank manufactured after August 23, 2011? ☒ Yes ☐ No
6. Type of change: ☒ New construction ☐ New stored material ☐ Other ☐ Relocation
7A. Description of Tank Modification (if applicable) na 7B. Will more than one material be stored in this tank? If so, a separate form must be completed for each material. ☐ Yes ☒ No 7C. Was USEPA Tanks simulation software utilized? ☒ Yes ☐ No (Please refer to Appendix S5 – Emission Programs) If Yes, please provide the appropriate documentation and items 8-42 below are not required.
TANK INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs 8. Design Capacity (specify barrels or gallons). Use the internal cross-sectional area multiplied by internal height. 9A. Tank Internal Diameter (ft.) 9B. Tank Internal Height (ft.) 10A. Maximum Liquid Height (ft.) 10B. Average Liquid Height (ft.) 11A. Maximum Vapor Space Height (ft.) 11B. Average Vapor Space Height (ft.) 12. Nominal Capacity (specify barrels or gallons). This is also known as “working volume”. 13A. Maximum annual throughput (gal/yr) 13B. Maximum daily throughput (gal/day) 14. Number of tank turnovers per year 15. Maximum tank fill rate (gal/min) 16. Tank fill method ☐ Submerged ☐ Splash ☐ Bottom Loading 17. Is the tank system a variable vapor space system? ☐ Yes ☐ No If yes, (A) What is the volume expansion capacity of the system (gal)? (B) What are the number of transfers into the system per year? 18. Type of tank (check all that apply): ☐ Fixed Roof ☐ vertical ☐ horizontal ☐ flat roof ☐ cone roof ☐ dome roof ☐ other (describe) ☐ External Floating Roof ☐ pontoon roof ☐ double deck roof ☐ Domed External (or Covered) Floating Roof ☐ Internal Floating Roof ☐ vertical column support ☐ self-supporting ☐ Variable Vapor Space ☐ lifter roof ☐ diaphragm ☐ Pressurized ☐ spherical ☐ cylindrical ☐ Other (describe)
PRESSURE/VACUUM CONTROL DATA – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs
19. Check as many as apply: ☐ Does Not Apply ☐ Rupture Disc (psig) ☐ Inert Gas Blanket of _____________ ☐ Carbon Adsorption1 ☐ Vent to Vapor Combustion Device1 (vapor combustors, flares, thermal oxidizers, enclosed combustors) ☐ Conservation Vent (psig) ☐ Condenser1
Vacuum Setting Pressure Setting ☐ Emergency Relief Valve (psig) Vacuum Setting Pressure Setting ☐ Thief Hatch Weighted ☐ Yes ☐ No 1 Complete appropriate Air Pollution Control Device Sheet 20. Expected Emission Rate (submit Test Data or Calculations here or elsewhere in the application). Material Name
Flashing Loss Breathing Loss Working Loss Total Emissions Loss
Estimation Method1
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
1 EPA = EPA Emission Factor, MB = Material Balance, SS = Similar Source, ST = Similar Source Test, Throughput Data, O = Other (specify) Remember to attach emissions calculations, including TANKS Summary Sheets and other modeling summary sheets if applicable.
TANK CONSTRUCTION AND OPERATION INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 21. Tank Shell Construction: ☐ Riveted ☐ Gunite lined ☐ Epoxy-coated rivets ☐ Other (describe) 21A. Shell Color: 21B. Roof Color: 21C. Year Last Painted: 22. Shell Condition (if metal and unlined): ☐ No Rust ☐ Light Rust ☐ Dense Rust ☐ Not applicable
22A. Is the tank heated? ☐ Yes ☐ No 22B. If yes, operating temperature:
22C. If yes, how is heat provided to tank?
23. Operating Pressure Range (psig): Must be listed for tanks using VRUs with closed vent system. 24. Is the tank a Vertical Fixed Roof Tank? ☐ Yes ☐ No
24A. If yes, for dome roof provide radius (ft):
24B. If yes, for cone roof, provide slop (ft/ft):
25. Complete item 25 for Floating Roof Tanks ☐ Does not apply ☐ 25A. Year Internal Floaters Installed:
25B. Primary Seal Type (check one): ☐ Metallic (mechanical) shoe seal ☐ Liquid mounted resilient seal ☐ Vapor mounted resilient seal ☐ Other (describe): 25C. Is the Floating Roof equipped with a secondary seal? ☐ Yes ☐ No
25D. If yes, how is the secondary seal mounted? (check one) ☐ Shoe ☐ Rim ☐ Other (describe):
25E. Is the floating roof equipped with a weather shield? ☐ Yes ☐ No 25F. Describe deck fittings:
26. Complete the following section for Internal Floating Roof Tanks ☐ Does not apply
26A. Deck Type: ☐ Bolted ☐ Welded 26B. For bolted decks, provide deck construction:
26C. Deck seam. Continuous sheet construction: ☐ 5 ft. wide ☐ 6 ft. wide ☐ 7 ft. wide ☐ 5 x 7.5 ft. wide ☐ 5 x 12 ft. wide ☐ other (describe) 26D. Deck seam length (ft.):
26E. Area of deck (ft2):
26F. For column supported tanks, # of columns:
26G. For column supported tanks, diameter of column:
27. Closed Vent System with VRU? ☐ Yes ☐ No
28. Closed Vent System with Enclosed Combustor? ☐ Yes ☐ No
SITE INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs 29. Provide the city and state on which the data in this section are based: 30. Daily Avg. Ambient Temperature (°F): 31. Annual Avg. Maximum Temperature (°F): 32. Annual Avg. Minimum Temperature (°F): 33. Avg. Wind Speed (mph): 34. Annual Avg. Solar Insulation Factor (BTU/ft2-day): 35. Atmospheric Pressure (psia):
LIQUID INFORMATION – See EPA TANKS 4.0.9d Output in Appendix S5 Emission Programs 36. Avg. daily temperature range of bulk liquid (°F):
36A. Minimum (°F): 36B. Maximum (°F):
37. Avg. operating pressure range of tank (psig):
37A. Minimum (psig): 37B. Maximum (psig):
38A. Minimum liquid surface temperature (°F): 38B. Corresponding vapor pressure (psia): 39A. Avg. liquid surface temperature (°F): 39B. Corresponding vapor pressure (psia): 40A. Maximum liquid surface temperature (°F): 40B. Corresponding vapor pressure (psia): 41. Provide the following for each liquid or gas to be stored in the tank. Add additional pages if necessary. 41A. Material name and composition: 41B. CAS number: 41C. Liquid density (lb/gal): 41D. Liquid molecular weight (lb/lb-mole): 41E. Vapor molecular weight (lb/lb-mole): 41F. Maximum true vapor pressure (psia): 41G. Maximum Reid vapor pressure (psia): 41H. Months Storage per year. From: To:
42. Final maximum gauge pressure and temperature prior to transfer into tank used as inputs into flashing emission calculations.
16
STORAGE TANK DATA TABLE
List all de minimis storage tanks (i.e. lube oil, glycol, diesel etc.)
Source
ID #1
Status2
Content3
Volume4
TK-09 NEW Lube Oil 4,200
TK-10 NEW Used Oil 4,200
TK-11 NEW Coolant 4,200
TK-12 NEW Used Coolant 4,200
TK-13 NEW Methanol 4,200
TK-14 NEW Engine Oil 520
TK-15 NEW Engine Oil 520
TK-16 NEW Engine Oil 520
TK-17 NEW Engine Oil 520
TK-18 NEW Compressor Oil 520
TK-19 NEW Compressor Oil 520
TK-20 NEW Compressor Oil 520
TK-21 NEW Compressor Oil 520
TK-22 NEW Triethylene Glycol 1,000
1. Enter the appropriate Source Identification Numbers (Source ID #) for each storage tank located at the compressor station.
Tanks should be designated T01, T02, T03, etc.
2. Enter storage tank Status using the following: EXIST Existing Equipment
NEW Installation of New Equipment
REM Equipment Removed 3. Enter storage tank content such as condensate, pipeline liquids, glycol (DEG or TEG), lube oil, diesel, mercaptan etc.
4. Enter the maximum design storage tank volume in gallons.
ATTACHMENT L – SMALL HEATERS AND REBOILERS NOT SUBJECT TO 40CFR60 SUBPART DC
DATA SHEET Complete this data sheet for each small heater and reboiler not subject to 40CFR60 Subpart Dc at the facility. The Maximum Design Heat Input (MDHI) must be less than 10 MMBTU/hr. Emission Unit ID#1
Emission Point ID#2
Emission Unit Description (manufacturer, model #)
Year Installed/ Modified
Type3 and Date of Change
Maximum Design Heat Input (MMBTU/hr)4
Fuel Heating Value (BTU/scf)5
RBV 11E Dehydrator – Reboiler Vent TBD NEW 2.0 1,020
1 Enter the appropriate Emission Unit (or Source) identification number for each fuel burning unit located at the production pad. Gas Producing Unit Burners should be designated GPU-1, GPU-2, etc. Heater Treaters should be designated HT-1, HT-2, etc. Heaters or Line Heaters should be designated LH-1, LH-2, etc. For sources, use 1S, 2S, 3S…or other appropriate designation. Enter glycol dehydration unit Reboiler Vent data on the Glycol Dehydration Unit Data Sheet.
2 Enter the appropriate Emission Point identification numbers for each fuel burning unit located at the production pad. Gas Producing Unit Burners should be designated GPU-1, GPU-2, etc. Heater Treaters should be designated HT-1, HT-2, etc. Heaters or Line Heaters should be designated LH-1, LH-2, etc. For emission points, use 1E, 2E, 3E…or other appropriate designation.
3 New, modification, removal 4 Enter design heat input capacity in MMBtu/hr. 5 Enter the fuel heating value in BTU/standard cubic foot.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment M
Internal Combustion Engine Data Sheet(s)
ATTACHMENT M – INTERNAL COMBUSTION ENGINE DATA SHEET Complete this data sheet for each internal combustion engine at the facility. Include manufacturer performance data sheet(s) or any other supporting document if applicable. Use extra pages if necessary. Generator(s) and microturbine generator(s) shall also use this form. Emission Unit ID#1 CE-01 CE-02 CE-03
Engine Manufacturer/Model CAT G3616LE A4 CAT G3616LE A4 CAT G3616LE A4
Manufacturers Rated bhp/rpm 5,000 / 1,000 5,000 / 1,000 5,000 / 1,000
Source Status2 NEW NEW NEW
Date Installed/ Modified/Removed/Relocated3
TBD TBD TBD
Engine Manufactured /Reconstruction Date4
TBD TBD TBD
Check all applicable Federal Rules for the engine (include EPA Certificate of Conformity if applicable)5
☒40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
☒40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
☒40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
Engine Type6 4SLB 4SLB 4SLB
APCD Type7 A/F, OxCat A/F, OxCat A/F, OxCat
Fuel Type8 RG RG RG
H2S (gr/100 scf) <0.25 <0.25 <0.25
Operating bhp/rpm 5,000 / 1,000 5,000 / 1,000 5,000 / 1,000
BSFC (BTU/bhp-hr) 7,466 (HHV) 7,466 (HHV) 7,466 (HHV)
Hourly Fuel Throughput 36,598 ft3/hr
na gal/hr 36,598 ft
3/hr
na gal/hr 36,598 ft
3/hr
na gal/hr
Annual Fuel Throughput (Must use 8,760 hrs/yr unless emergency generator)
320.60 MMft3/yr
na gal/yr 320.60 MMft
3/yr
na gal/yr 320.60 MMft
3/yr
na gal/yr
Fuel Usage or Hours of Operation Metered
Yes ☒ No ☐ Yes ☒ No ☐ Yes ☒ No ☐
Calculation Methodology9 Pollutant10
Hourly PTE
(lb/hr)11
Annual PTE
(tons/year)
11
Hourly PTE
(lb/hr)11
Annual PTE
(tons/year)
11
Hourly PTE
(lb/hr) 11
Annual PTE
(tons/year)
11 MD NOx 4.41 19.31 4.41 19.31 4.41 19.31
MD CO 2.58 11.32 2.58 11.32 2.58 11.32
MD VOC 2.07 9.05 2.07 9.05 2.07 9.05
AP SO2 0.02 0.09 0.02 0.09 0.02 0.09
AP PM10 0.37 1.63 0.37 1.63 0.37 1.63
MD Formaldehyde 0.28 1.22 0.28 1.22 0.28 1.22
MD/AP Total HAPs 0.39 1.72 0.39 1.72 0.39 1.72
MD/AP GHG (CO2e) 5,401 23,656 5,401 23,656 5,401 23,656
ATTACHMENT M – INTERNAL COMBUSTION ENGINE DATA SHEET Complete this data sheet for each internal combustion engine at the facility. Include manufacturer performance data sheet(s) or any other supporting document if applicable. Use extra pages if necessary. Generator(s) and microturbine generator(s) shall also use this form. Emission Unit ID#1 CE-04 GT
Engine Manufacturer/Model CAT G3616LE A4 FlexEnergy GT1300S
Manufacturers Rated bhp/rpm 5,000 / 1,000 1,742 / ---
Source Status2 NEW NEW
Date Installed/ Modified/Removed/Relocated3
TBD TBD
Engine Manufactured /Reconstruction Date4
TBD TBD
Check all applicable Federal Rules for the engine (include EPA Certificate of Conformity if applicable)5
☒40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
☐40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
☐40CFR60 Subpart JJJJ ☐JJJJ Certified? ☐40CFR60 Subpart IIII ☐IIII Certified? ☐40CFR63 Subpart ZZZZ ☐ NESHAP ZZZZ/ NSPS JJJJ Window ☐ NESHAP ZZZZ Remote Sources
Engine Type6 4SLB Microturbine
APCD Type7 A/F, OxCat na
Fuel Type8 RG RG
H2S (gr/100 scf) <0.25 <0.25
Operating bhp/rpm 5,000 / 1,000 1,742 / ---
BSFC (BTU/bhp-hr) 7,466 (HHV) 17,002 (HHV)
Hourly Fuel Throughput 36,598 ft3/hr
na gal/hr 29,037 ft
3/hr
na gal/hr ft3/hr gal/hr
Annual Fuel Throughput (Must use 8,760 hrs/yr unless emergency generator)
320.60 MMft3/yr
na gal/yr 254.36 MMft
3/yr
na gal/yr MMft3/yr
gal/yr
Fuel Usage or Hours of Operation Metered
Yes ☒ No ☐ Yes ☒ No ☐ Yes ☐ No ☐
Calculation Methodology9 Pollutant10
Hourly PTE
(lb/hr)11
Annual PTE
(tons/year)
11
Hourly PTE
(lb/hr) 11
Annual PTE
(tons/year)
11
Hourly PTE
(lb/hr) 11
Annual PTE
(tons/year)
11 MD NOx 4.41 19.31 1.04 4.55
MD CO 2.58 11.32 2.86 12.51
MD VOC 2.07 9.05 0.28 1.23
AP SO2 0.02 0.09 0.10 0.44
AP PM10 0.37 1.63 0.20 0.86
MD Formaldehyde 0.28 1.22 0.02 0.09
MD/AP Total HAPs 0.39 1.72 0.03 0.14
MD/AP GHG (CO2e) 5,401 23,656 3,291 14,414
20
1 Enter the appropriate Source Identification Number for each natural gas-fueled reciprocating internal combustion compressor/generator engine located at the compressor station. Multiple compressor engines should be designated CE-1, CE-2, CE-3 etc. Generator engines should be designated GE-1, GE-2,
GE-3 etc. Microturbine generator engines should be designated MT-1, MT-2, MT-3 etc. If more than three (3) engines exist, please use additional sheets.
2 Enter the Source Status using the following codes:
NS Construction of New Source (installation) ES Existing Source
MS Modification of Existing Source RS Relocated Source REM Removal of Source
3 Enter the date (or anticipated date) of the engine’s installation (construction of source), modification, relocation or removal.
4 Enter the date that the engine was manufactured, modified or reconstructed.
5 Is the engine a certified stationary spark ignition internal combustion engine according to 40CFR60 Subpart IIII/JJJJ? If so, the engine and control device
must be operated and maintained in accordance with the manufacturer’s emission-related written instructions. You must keep records of conducted
maintenance to demonstrate compliance, but no performance testing is required. If the certified engine is not operated and maintained in accordance with the manufacturer’s emission-related written instructions, the engine will be considered a non-certified engine and you must demonstrate compliance as
appropriate.
Provide a manufacturer’s data sheet for all engines being registered.
6 Enter the Engine Type designation(s) using the following codes:
2SLB Two Stroke Lean Burn 4SRB Four Stroke Rich Burn
4SLB Four Stroke Lean Burn
7 Enter the Air Pollution Control Device (APCD) type designation(s) using the following codes:
A/F Air/Fuel Ratio IR Ignition Retard
HEIS High Energy Ignition System SIPC Screw-in Precombustion Chambers PSC Prestratified Charge LEC Low Emission Combustion
NSCR Rich Burn & Non-Selective Catalytic Reduction OxCat Oxidation Catalyst
SCR Lean Burn & Selective Catalytic Reduction
8 Enter the Fuel Type using the following codes:
PQ Pipeline Quality Natural Gas RG Raw Natural Gas /Production Gas D Diesel
9 Enter the Potential Emissions Data Reference designation using the following codes . Attach all reference data used.
MD Manufacturer’s Data AP AP-42
GR GRI-HAPCalcTM OT Other (please list)
10 Enter each engine’s Potential to Emit (PTE) for the listed regulated pollutants in pounds per hour and tons per year. PTE shall be calculated at manufacturer’s rated brake horsepower and may reflect reduction efficiencies of listed Air Pollution Control Devices. Emergency generator engines may use 500 hours of
operation when calculating PTE. PTE data from this data sheet shall be incorporated in the Emissions Summary Sheet.
11 PTE for engines shall be calculated from manufacturer’s data unless unavailable.
24
Engine Air Pollution Control Device (Emission Unit ID# CE-01 thru CE-04, use extra pages as necessary)
Air Pollution Control Device Manufacturer’s Data Sheet included?
Yes ☒ No ☐
☐ NSCR ☐ SCR ☒ Oxidation Catalyst
Provide details of process control used for proper mixing/control of reducing agent with gas stream: na Manufacturer: Catalytic Combustion Model #: REM-4815-D-20HB-HFX4 (or equivalent)
Design Operating Temperature: 814 oF Design gas volume: 31,291 acfm
Service life of catalyst: 24,000 hrs or 3 years, whichever comes first
Provide manufacturer data? ☒Yes ☐ No (See Appendix S4 – Vendor Data)
Volume of gas handled: 31,291 acfm at 814 oF Operating temperature range for NSCR/Ox Cat:
From 450 oF to 1,350
oF
Reducing agent used, if any: na Ammonia slip (ppm):
Pressure drop against catalyst bed (delta P): <2.0 inches of H2O
Provide description of warning/alarm system that protects unit when operation is not meeting design conditions: Engine is equipped with a monitoring device capable of measuring both the catalyst inlet and exit temperatures and to immediately shut the engine down should the catalyst exit temperature reach the 1,350oF limit.
Is temperature and pressure drop of catalyst required to be monitored per 40CFR63 Subpart ZZZZ? ☐ Yes ☒ No How often is catalyst recommended or required to be replaced (hours of operation)?
24,000
How often is performance test required? Initial Annual Every 8,760 hours of operation Field Testing Required No performance test required. If so, why (please list any maintenance required and the applicable sections in NSPS/GACT,
Attachment N
Tanker Truck Loading Data Sheet (If Applicable)
22
ATTACHMENT N – TANKER TRUCK LOADING DATA SHEET
Complete this data sheet for each new or modified bulk liquid transfer area or loading
rack at the facility. This is to be used for bulk liquid transfer operations to tanker
trucks. Use extra pages if necessary.
Truck Loadout Collection Efficiencies
The following applicable capture efficiencies of a truck loadout are allowed:
▪ For tanker trucks passing the MACT level annual leak test – 99.2%
▪ For tanker trucks passing the NSPS level annual leak test – 98.7%
▪ For tanker trucks not passing one of the annual leak tests listed above – 70%
Compliance with this requirement shall be demonstrated by keeping records of the applicable
MACT or NSPS Annual Leak Test certification for every truck and railcar loaded/unloaded.
This requirement can be satisfied if the trucking company provided certification that its entire
fleet was compliant. This certification must be submitted in writing to the Director of the
DAQ. These additional requirements must be noted in the Registration Application and will
be noted on the issued G35-D Registration.
Emission Unit ID#: TLO Emission Point ID#: 21E Year Installed/Modified: TBD
Emission Unit Description: Truck Load-Out of Stabilized Condensate and Produced Water
Loading Area Data
Number of Pumps: One (1) Number of Liquids Loaded: Two (2) Max number of trucks loading at one
(1) time: One (1)
Are tanker trucks pressure tested for leaks at this or any other location? ☐ Yes ☒ No ☐ Not Required
If Yes, please describe:
Provide description of closed vent system and any bypasses. na
Are any of the following truck loadout systems utilized?
☐ Closed System to tanker truck passing a MACT level annual leak test?
☐ Closed System to tanker truck passing a NSPS level annual leak test?
☒ Closed System to tanker truck not passing an annual leak test and has vapor return?
Projected Maximum Operating Schedule (for rack or transfer poi nt as a whole)
Time Jan – Mar Apr - Jun Jul – Sept Oct - Dec
Hours/day 6 6 6 6
Days/week 7 7 7 7
Bulk Liquid Data (use extra pages as necessary)
Liquid Name Stabilized Condensate Produced Water
Max. Daily Throughput (1000 gal/day)
Max. Annual Throughput
(1000 gal/yr) 9,576 1,260
Loading Method1 SUB SUB
Max. Fill Rate (gal/min) 250 250
Average Fill Time
(min/loading) 60 60
Max. Bulk Liquid
Temperature (oF) 50 50
True Vapor Pressure2 5.3 1.5
Cargo Vessel Condition3 U U
Control Equipment or
Method4 VRU VRU
23
Max. Collection Efficiency
(%) 70 70
Max. Control Efficiency (%)
95 95
Max. VOC Emission
Rate
Loading
(lb/hr) --- ---
Annual
(ton/yr) 7.51 0.14
Max. HAP
Emission Rate
Loading (lb/hr)
--- ---
Annual
(ton/yr) 1.08 0.02
Estimation Method5 EPA EPA
1 BF Bottom Fill SP Splash Fill SUB Submerged Fill
2 At maximum bulk liquid temperature B Ballasted Vessel C Cleaned U Uncleaned (dedicated service)
O Other (describe)
4 List as many as apply (complete and submit appropriate Air Pollution Control Device Sheets) CA Carbon Adsorption VB Dedicated Vapor Balance (closed system)
ECD Enclosed Combustion Device F Flare
TO Thermal Oxidization or Incineration 5 EPA EPA Emission Factor in AP-42 MB Material Balance
TM Test Measurement based upon test data submittal O Other (describe)
Attachment O
Glycol Dehydration Unit Data Sheet(s)
ATTACHMENT O – GLYCOL DEHYDRATION UNIT DATA SHEET
Complete this data sheet for each Glycol Dehydration Unit, Reboiler, Flash Tank and/or Regenerator at the facility. Include gas sample analysis and GRI- GLYCalcTM input and aggregate report. Use extra pages if necessary. Manufacturer: TBD Model: TBD
Max. Dry Gas Flow Rate: 200 MMscf/day Reboiler Design Heat Input: 2.0 MMBTU/hr
Design Type: ☒ TEG ☐ DEG ☐ EG Source Status1: NEW
Date Installed/Modified/Removed2: TBD Regenerator Still Vent APCD/ERD3: TOx
Control Device/ERD ID#3: TOx Fuel HV (BTU/scf): 1,020 (HHV)
H2S Content (gr/100 scf): <0.25 Operation (hours/year): 8,760
Pump Rate: 24.0 gpm (Electric/Primary) 7.5 gpm (Gas-Assist/Backup)
Water Content in: Wet Gas: Saturated Dry Gas: 7.0 lb/MMscf
Is the glycol dehydration unit exempt from 40CFR63 Section 764(d)? ☒ Yes ☐ No: If Yes, answer the following: The actual annual average flowrate of natural gas to the glycol dehydration unit is less than 85 thousand standard cubic meters per day, as determined by the procedures specified in §63.772(b)(1) of this subpart. ☐ Yes ☒ No The actual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere are less than 0.90 megagram per year (1 ton per year), as determined by the procedures specified in §63.772(b)(2) of this subpart. ☐ Yes ☐ No
Is the glycol dehydration unit located within an Urbanized Area (UA) or Urban Cluster (UC)? ☐ Yes ☒ No
Is a lean glycol pump optimization plan being utilized? ☐ Yes ☒ No
Recycling the glycol dehydration unit back to the flame zone of the reboiler. ☒ Yes ☐ No If yes: Is the reboiler configured to accept flash drum vapors (straight from the glycol dehydrator)? ☒ Yes ☐ No Is the reboiler configured to accept still vent vapors (after a condenser)? ☐ Yes ☒ No Is the reboiler configured to accept both in the same operation? ☐ Yes ☒ No Recycling the glycol dehydration unit back to the flame zone of the reboiler and mixed with fuel. ☒ Yes ☐ No What happens when temperature controller shuts off fuel to the reboiler?
Still vent emissions to the atmosphere. Still vent emissions to the thermal oxidizer. Still vent emissions stopped with valve. Flash Tank emissions to the thermal oxidizer. Still vent emissions to glow plug.
Please indicate if the following equipment is present. Flash Tank Burner management system that continuously burns condenser or flash tank vapors
Control Device Technical Data
Pollutants Controlled Manufacturer’s Guaranteed Control Efficiency (%)
VOC 98
HAP 98
25
Emissions Data
Emission Unit
ID / Emission
Point ID4
Description Calculation
Methodology5 PTE6
Controlled
Maximum
Hourly
Emissions
(lb/hr)
Controlled
Maximum
Annual
Emissions (tpy)
RBV Reboiler Vent
EPA AP-42 NOx 0.20 0.86
EPA AP-42 CO 0.16 0.72
EPA AP-42 VOC 0.01 0.05
EPA AP-42 SO2 1E-03 0.01
EPA AP-42 PM10 0.01 0.07
40CFR98 GHG (CO2e) 234 1,026
DSV Glycol
Regenerator Still Vent
GRI-GlyCalcTM VOC 1.47 6.46
GRI-GlyCalcTM Benzene 0.04 0.16
GRI-GlyCalcTM Toluene 0.17 0.74
GRI-GlyCalcTM Ethylbenzene 0.12 0.53
GRI-GlyCalcTM Xylenes 0.21 0.91
GRI-GlyCalcTM n-Hexane 0.06 0.27
DFT Glycol Flash
Tank
GRI-GlyCalcTM VOC 1.12 4.89
GRI-GlyCalcTM Benzene 4E-04 2E-03
GRI-GlyCalcTM Toluene 1E-03 5E-03
GRI-GlyCalcTM Ethylbenzene 5E-04 2E-03
GRI-GlyCalcTM Xylenes 5E-04 2E-03
GRI-GlyCalcTM n-Hexane 0.02 0.10
1 Enter the Source Status using the following codes:
NS Construction of New Source ES Existing Source MS Modification of Existing Source
2 Enter the date (or anticipated date) of the glycol dehydration unit’s installation (construction of source), modification or
removal. 3 Enter the Air Pollution Control Device (APCD)/Emission Reduction Device (ERD) type designation using the following codes
and the device ID number:
NA None CD Condenser FL Flare CC Condenser/Combustion Combination TO Thermal Oxidizer O Other (please list)
4 Enter the appropriate Emission Unit ID Numbers and Emission Point ID Numbers for the glycol dehydration unit reboiler vent
and glycol regenerator still vent. The glycol dehydration unit reboiler vent and glycol regenerator still vent should be designated RBV-1 and RSV-1, respectively. If the compressor station incorporates multiple glycol dehydration units, a Glycol
Dehydration Emission Unit Data Sheet shall be completed for eac h, using Source Identification RBV-2 and RSV-2, RBV-3
and RSV-3, etc. 5 Enter the Potential Emissions Data Reference designation using the following codes:
MD Manufacturer’s Data AP AP-42 GR GRI-GLYCalcTM OT Other (please list)
6 Enter the Reboiler Vent and Glycol Regenerator Still Vent Potential to Emit (PTE) for the listed regulated pollutants in lbs
per hour and tons per year. The Glycol Regenerator Still Vent potential emissions may be determined us ing the most recent version of the thermodynamic software model GRI-GLYCalcTM (Radian International LLC & Gas Research Institute). Attach
all referenced Potential Emissions Data (or calculations) and the GRI -GLYCalcTM Aggregate Calculations Report (shall
include emissions reports, equipment reports, and stream reports) to this Glycol Dehydration Emission Unit Data
Sheet(s). Backup pumps do not have to be considered as operating for purposes of PTE. This PTE data shall be
incorporated in the Emissions Summary Sheet.
Attachment P
Pneumatic Controllers Data Sheet(s)
ATTACHMENT P – PNEUMATIC CONTROLLERS DATA SHEET
Are there any continuous bleed natural gas driven pneumatic controllers at this facility that commenced construction, modification or reconstruction after August 23, 2011, and
on or before September 18, 2015?
Yes No
Please list approximate number.
Are there any continuous bleed natural gas driven pneumatic controllers at this facility that commenced construction, modification or reconstruction after September 18, 2015?
Yes No
Please list approximate number.
Are there any continuous bleed natural gas driven pneumatic controllers at this facility with a bleed rate greater than 6 standard cubic feet per hour that are required based on functional needs, including but not limited to response time, safety and positive actuation that commenced construction, modification or reconstruction after August 23, 2011, and
on or before September 18, 2015?
Yes No
Please list approximate number.
Are there any continuous bleed natural gas driven pneumatic controllers at this facility with a bleed rate greater than 6 standard cubic feet per hour that are required based on functional needs, including but not limited to response time, safety and positive actuation that commenced construction, modification or reconstruction after September 18, 2015?
Yes No
Please list approximate number.
Attachment Q
Centrifugal Compressor Data Sheet(s)
ATTACHMENT Q – CENTRIFUGAL COMPRESSOR DATA SHEET
Are there any centrifugal compressors at this facility that commenced construction,
modification or reconstruction after August 23, 2011, and on or before September 18, 2015?
Yes No
Please list:
Emission Unit ID#
Compressor Description
Are there any centrifugal compressors at this facility that commenced construction,
modification or reconstruction after September 18, 2015?
Yes No
Please list:
Emission Unit ID#
Compressor Description
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment R
Reciprocating Compressor Data Sheet(s)
ATTACHMENT R – RECIPROCATING COMPRESSOR
DATA SHEET
Are there any reciprocating compressors at this facility that commenced construction,
modification or reconstruction after August 23, 2011, and on or before September 18,
2015?
Yes No
Please list:
Emission
Unit ID#
Compressor Description
Are there any reciprocating compressors at this facility that commenced construction,
modification or reconstruction after September 18, 2015?
Yes No
Please list:
Emission
Unit ID#
Compressor Description
CRP Natural Gas Compressor 01
CRP Natural Gas Compressor 02
CRP Natural Gas Compressor 03
CRP Natural Gas Compressor 04
CRP Vapor Recovery Unit (VRU) Compressor 05
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment S
Blowdown and Pigging Operations Data Sheet(s)
ATTACHMENT S – BLOWDOWN AND PIGGING OPERATIONS
DATA SHEET
Will there be any blowdown and pigging operations that occur at this facility?
Yes No
Please list:
Type of
Event
# of Events
(event/yr)
Amount
Vented per
event
(scf/event)
MW of
vented gas
(lb/lb-mol)
Total
Emissions
(ton/yr)
VOC weight
fraction
VOC
emissions
(ton/yr)
Compressor
Blowdown 428 varies 4.04
Compressor
Startup
Plant
Shutdown 1 967,000 0.17
Low Pressure
Pig Venting 104 3823 0.08
High Pressure
Pig Venting 52 8,064 0.07
Type of
Event
# of Events
(event/yr)
Amount
Vented per
event
(scf/event)
MW of
vented gas
(lb/lb-mol)
Total
Emissions
(ton/yr)
HAP weight
fraction
HAP
emissions
(ton/yr)
Compressor
Blowdown
Compressor
Startup
Plant
Shutdown
Low Pressure
Pig Venting
High Pressure
Pig Venting
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment T
Air Pollution Control Device/Emission Reduction Device(s) Sheet(s)
ATTACHMENT T – AIR POLLUTION CONTROL DEVICE /
EMISSION REDUCTION DEVICE SHEETS
Complete the applicable air pollution control device sheets for each flare, vapor combustor,
thermal oxidizer, condenser, adsorption system, vapor recovery unit, BTEX Eliminator,
Reboiler with and without Glow Plug, etc. at the facility. Use extra pages if necessary.
Emissions calculations must be performed using the most conservative control device
efficiency.
The following five (5) rows are only to be completed if registering an alternative air pollution
control device.
Emission Unit ID: Make/Model:
Primary Control Device ID: Make/Model:
Control Efficiency (%): APCD/ERD Data Sheet Completed: ☐ Yes
☐ No
Secondary Control Device ID: Make/Model:
Control Efficiency (%): APCD/ERD Data Sheet Completed: ☐ Yes
☐ No
• Vapor Combustor – FLR
• Vapor Combustor – TOx
• Condenser - Not Applicable
• Adsorption System - Not Applicable
• Vapor Recovery Unit (VRU)
31
VAPOR COMBUSTION
(Including Enclosed Combustors)
General Information
Control Device ID#: FLR Installation Date: TBD
New Modified Relocated
Maximum Rated Total Flow Capacity
scfh scfd
Maximum Design
Heat Input (from mfg. spec sheet)
MMBTU/hr
Design Heat Content
1,343 BTU/scf
Control Device Information
Type of Vapor Combustion Control?
Enclosed Combustion Device Elevated Flare Ground Flare Thermal Oxidizer
Manufacturer: Zeeco
Model: MJ-16 Sonic Flare Hours of operation per year? 8,760 (Intermittent)
List the emission units whose emissions are controlled by this vapor control device (Emission Point ID# : 6E
Emission Unit ID#
Emission Source Description Emission Unit ID#
Emission Source Description
SSM Compressor Blowdown (CBD)
SSM Emergency Shutdown (ESD) Testing
SSM Pigging Operations (PIG)
If this vapor combustor controls emissions from more than six (6) emission units, please attach additional pages.
Assist Type (Flares only) Flare Height Tip Diameter Was the design per §60.18?
Steam Air
Pressure None
145 feet feet ☐ Yes ☒ No
Provide determination.
Waste Gas Information
Maximum Waste Gas Flow Rate (scfm)
Heat Value of Waste Gas Stream 1,342 1,343 BTU/ft3
Exit Velocity of the Emissions Stream (ft/s)
Provide an attachment with the characteristics of the waste gas stream to be burned.
Pilot Gas Information
Number of Pilot Lights Two (2)
Fuel Flow Rate to Pilot Flame per Pilot
50 scfh
Heat Input per Pilot 67,150 BTU/hr
Will automatic re-ignition be used?
☒ Yes ☐ No
If automatic re-ignition is used, please describe the method.
Is pilot flame equipped with a monitor to detect the
presence of the flame? ☒ Yes ☐ No
If Yes, what type? ☒ Thermocouple ☐ Infrared
☐ Ultraviolet ☐ Camera ☐ Other:
Describe all operating ranges and maintenance procedures required by the manufacturer to maintain the warranty. (If
unavailable, please indicate). na
Additional information attached? ☒ Yes ☐ No
Please attach copies of manufacturer’s data sheets, drawings, flame demonstration per §60.18 or §63.11(b) and
performance testing. (See Appendix S4 - Vendor Data)
32
VAPOR COMBUSTION
(Including Enclosed Combustors)
General Information
Control Device ID#: TOx Installation Date: TBD
New Modified Relocated
Maximum Rated Total Flow Capacity 9,984 scfh 239,616 scfd
Maximum Design Heat Input (from
mfg. spec sheet)
6.00 MMBTU/hr
Design Heat Content 622 BTU/scf
Control Device Information
Type of Vapor Combustion Control? Enclosed Combustion Device Elevated Flare Ground Flare
Thermal Oxidizer
Manufacturer: Zeeco
Model: Z-HTO (or equivalent) Hours of operation per year? 8,760
List the emission units whose emissions are controlled by this vapor control device (Emission Point ID# : 9E and 10E
Emission
Unit ID# Emission Source Description
Emission
Unit ID# Emission Source Description
DFT Dehydrator - Flash Tank
DSV Dehydrator - Still Vent
If this vapor combustor controls emissions from more than six (6) emission units, please attach addi tional pages.
Assist Type (Flares only) Flare Height Tip Diameter Was the design per §60.18?
Steam Air
Pressure None
20 feet feet ☐ Yes ☒ No
Provide determination.
Waste Gas Information
Maximum Waste Gas Flow Rate
160 (scfm) Heat Value of Waste Gas Stream
622 BTU/ft3 Exit Velocity of the Emissions Stream
(ft/s)
Provide an attachment with the characteristics of the waste gas stream to be burned.
Pilot Gas Information
Number of Pilot Lights
One (1) Fuel Flow Rate to Pilot
Flame per Pilot 100 scfh
Heat Input per Pilot
134,300 BTU/hr (HHV) Will automatic re-ignition
be used?
☒ Yes ☐ No
If automatic re-ignition is used, please describe the method. Electric spark
Is pilot flame equipped with a monitor to detect the
presence of the flame? ☒ Yes ☐ No
If Yes, what type? ☒ Thermocouple ☐ Infrared
☐ Ultraviolet ☐ Camera ☐ Other:
Describe all operating ranges and maintenance procedures required by the manufacturer to maintain the warranty. (If
unavailable, please indicate). na
Additional information attached? ☒ Yes ☐ No
Please attach copies of manufacturer’s data sheets, drawings, flame demonstration per §60.18 or §63.11(b) and performance testing. (See Appendix S4 - Vendor Data)
33
CONDENSER – Not Applicable
General Information
Control Device ID#: Installation Date:
New Modified Relocated
Manufacturer:
Model:
Control Device Name:
Control Efficiency (%):
Manufacturer’s required temperature range for control efficiency. oF
Describe the warning and/or alarm system that protects against operation when unit is not meeting the design requirements:
Describe all operating ranges and maintenance procedures required by the manufacturer to maintain the warranty.
Additional information attached? ☐ Yes ☐ No
Please attach copies of manufacturer’s data sheets.
Is condenser routed to a secondary APCD or ERD?
☐ Yes ☐ No
34
ADSORPTION SYSTEM – Not Applicable
General Information
Control Device ID#: Installation Date:
New Modified Relocated
Manufacturer:
Model:
Control Device Name:
Design Inlet Volume: scfm Adsorbent charge per adsorber vessel and number of
adsorber vessels:
Length of Mass Transfer Zone supplied by the manufacturer:
Adsorber diameter: ft Adsorber area: ft2
Adsorbent type and physical properties: Overall Control Efficiency (%):
Working Capacity of Adsorbent (%):
Operating Parameters
Inlet volume: scfm @ oF
Adsorption time per adsorption bed (life expectancy):
Breakthrough Capacity (lbs of VOC/100 lbs of adsorbent):
Temperature range of carbon bed adsorber. oF - oF
Control Device Technical Data
Pollutants Controlled Manufacturer’s Guaranteed Control Efficiency (%)
Describe the warning and/or alarm system that prot ects against operation when unit is not meeting the design requirements:
Has the control device been tested by the manufacturer and certified?
Describe all operating ranges and maintenance procedures required by t he manufacturer to maintain the warranty.
Additional information attached? ☐ Yes ☐ No
Please attach copies of manufacturer’s data sheets, drawings, and performance testing .
35
VAPOR RECOVERY UNIT
General Information
Emission Unit ID#: VRU Installation Date: TBD
New Modified Relocated
Device Information
Manufacturer: TBD
Model: TBD
List the emission units whose emissions are controlled by this vapor recovery unit (Emission Point ID#: 13E thru 21E
Emission
Unit ID# Emission Source Description
Emission
Unit ID# Emission Source Description
TK-01 thru 06 Stabilized Condensate Storage Tanks
TK-07 and 08 Produced Water Storage Tanks
TLO Truck Load-Out
If this vapor recovery unit controls emissions from more than six (6) emission units, please attach additional pages.
Additional information attached? ☐ Yes ☒ No
Please attach copies of manufacturer’s data sheets, drawings, and performance testing .
The registrant may claim a capture and control efficiency of 95 % (which accounts for 5% downtime) for the vapor recovery unit.
The registrant may claim a capture and control efficiency of 98% if the VRU has a backup flare that meet the requirements of
Section 8.1.2 of this general permit.
The registrant may claim a capture and control efficiency of 98% if the VRU has a backup VRU.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment U
Emission Calculations
ATTACHMENT U – EMISSIONS CALCULATIONS
Provide detailed potential to emit (PTE) emission calculations for criteria and hazardous air
pollutants (HAPs) for each emission point identified in the application. For hazardous air
pollutants and volatile organic compounds (VOCs), the speciated emission calculations must
be included.
Use the following guidelines to ensure complete emission calculations:
▪ All emission sources and fugitive emissions are included in the emission calculations,
as well as all methods used to calculate the emissions.
▪ Proper emission point identification numbers and APCD and ERD identification
numbers are used consistently in the emission calculations that are used throughout the
application.
▪ A printout of the emission summary sheets is attached to the registration application.
▪ Printouts of any modeling must be included with the emission calculations. The
modeling printout must show all inputs/outputs or assumptions that the modeled
emissions are based upon.
▪ If emissions are provided from the manufacturer, the manufacturer’s documentation
and/or certified emissions must also be included.
▪ The emission calculations results must match the emissions provided on the emissions
summary sheet.
▪ If calculations are based on a compositional analysis of the gas, attach the laboratory
analysis. Include the following information: the location that the sample was taken as
representative; the date the sample was taken; and, if the sample is considered
representative, the reasons that it is considered representative (same gas field, same
formation and depth, distance from actual site, etc.).
▪ Potential to emit (PTE) from the main or backup control device may be calculated
based on the highest emission from a control device that could handle the stream, plus
any intrinsic emission such as those from pilot flames.
▪ Provide any additional clarification as necessary. Additional clarification or
information is especially helpful when reviewing modeling calculations to assist the
engineer in understanding the basis of assumptions and/or inputs.
Please follow specific guidance provided on the emissions summary sheet when providing the
calculations.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment U
Emission Calculations - Continued
• Emission Summary Spreadsheets
o Potential to Emit (PTE) – Criteria Pollutants – Controlled 01 of 19 o Potential to Emit (PTE) – Hazardous Air Pollutants (HAP) – Controlled 02 of 19 o Potential to Emit (PTE) – Greenhouse Gases (GHG) – Controlled 03 of 19 o Potential to Emit (PTE) – Criteria Pollutants – PRE-Controlled 04 of 19 o Potential to Emit (PTE) – Hazardous Air Pollutants (HAP) – PRE-Controlled 05 of 19 o Potential to Emit (PTE) – Greenhouse Gases (GHG) – PRE-Controlled 06 of 19
• Unit-Specific Emission Spreadsheets
o Compressor Engines (CE-01 (1E) thru CE-04 (4E)) 07 of 19 o Compressor Rod Packing (CRP (5E)) 08 of 19 o Start/Stop/Maintenance (SSM (6E)) 09 of 19
▪ Compressor Blowdown (CBD) “ ▪ Emergency Shutdown (ESD) Testing “ ▪ Pigging Operations (PIG) “
o SSM Flare (FLR (7E)) 10 of 19 o Microturbine Generator (GT (8E)) 11 of 19 o Dehydrator (DHY) 12 of 19
▪ Dehydrator Flash Tanks (DFT (9E)) “ ▪ Dehydrator Still Vents (DSV (10E)) ”
o Reboilers (RBV (11E)) 13 of 19 o Thermal Oxidizer (Combustion Only) (TOx (12E)) 14 of 19 o Stabilized Condensate Storage Tanks (TK-01 (13E) thru TK-06 (18E)) 15 of 19 o Produced Water Storage Tanks (TK-07 (19E) and TK-08 (20E)) “ o Stabilized Condensate Truck Load-Out (TLO (21E)) 16 of 19 o Produced Water Truck Load-Out (TLO (21E)) ”
• Fugitive Emission Spreadsheets
o Process Piping Fugitives-Gas (FUG-G (1F)) 17 of 19 o Process Piping Fugitives-Light Liquid (FUG-L (2F)) 18 of 19 o Engine Crankcase (ECC (3F)) 19 of 19
lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy
CE-01 1E OxCat-01 Compressor Engine 01 - CAT G3616LE A4 5,000 bhp 4.41 19.31 2.58 11.32 2.07 9.05 0.37 1.63 0.02 0.10CE-02 2E OxCat-02 Compressor Engine 02 - CAT G3616LE A4 5,000 bhp 4.41 19.31 2.58 11.32 2.07 9.05 0.37 1.63 0.02 0.10CE-03 3E OxCat-03 Compressor Engine 03 - CAT G3616LE A4 5,000 bhp 4.41 19.31 2.58 11.32 2.07 9.05 0.37 1.63 0.02 0.10CE-04 4E OxCat-04 Compressor Engine 04 - CAT G3616LE A4 5,000 bhp 4.41 19.31 2.58 11.32 2.07 9.05 0.37 1.63 0.02 0.10CRP 5E --- Compressor Rod Packing 5 Recip's --- --- --- --- 6.88 30.15 --- --- --- ---
--- Compressor Blowdown (CBD) 422 Events/yr --- --- --- --- --- 4.06 --- --- --- --- --- Emergency Shutdown (ESD) Testing 1 Event/yr --- --- --- --- --- 0.17 --- --- --- --- --- Pigging Operations (PIG) 156 Events/yr --- --- --- --- --- 0.15 --- --- --- ---
FLR 7E --- SSM Flare - Zeeco MJ-16 (Comb. Only) 3.49 MMBtu/hr --- 1.50 --- 4.74 --- 1E-03 --- 0.11 --- 0.01GT 8E --- Microturbine Generator - FlexEnergy GT1300S 1,742 bhp 1.04 4.55 2.86 12.51 0.28 1.23 0.20 0.86 0.10 0.44
DFT 9E Dehydrator - Flash Tank --- --- --- --- 1.12 4.89 --- --- --- ---DSV 10E Dehydrator - Still Vent --- --- --- --- 1.47 6.46 --- --- --- ---RBV 11E --- Dehydrator - Reboiler Vent 2.0 MMBtu/hr 0.20 0.86 0.16 0.72 0.01 0.05 0.01 0.07 1E-03 0.01TOx 12E --- Thermal Oxidizer - Zeeco Z-HTO (Comb. Only) 6.21 MMBtu/hr 0.61 2.67 1.93 8.43 5E-04 2E-03 0.05 0.20 0.00 0.02
TK-01 13E Storage Tank 01 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-02 14E Storage Tank 02 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-03 15E Storage Tank 03 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-04 16E Storage Tank 04 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-05 17E Storage Tank 05 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-06 18E Storage Tank 06 - Stabilized Condensate 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-07 19E Storage Tank 07 - Produced Water 400 bbl --- --- --- --- 3E-04 1E-03 --- --- --- ---TK-08 20E Storage Tank 08 - Produced Water 400 bbl --- --- --- --- 3E-04 1E-03 --- --- --- ---
Truck Load-Out - Stabilized Condensate 228,000 bbl/yr --- --- --- --- --- 7.51 --- --- --- ---Truck Load-Out - Produced Water 30,000 bbl/yr --- --- --- --- --- 0.14 --- --- --- ---
19.48 86.82 15.28 71.67 18.12 91.38 1.75 7.77 0.19 0.86
TVOP Threshold**: 100 100 100 100 100
FUG-G 1F --- Process Piping Fugitives - Gas 4,981 Fittings --- --- --- --- 0.97 4.23 --- --- --- ---FUG-L 2F --- Process Piping Fugitives - Light Liquid 2,271 Fittings --- --- --- --- 1.63 7.15 --- --- --- ---ECC 3F --- Engine Crankcase 4 Engines 0.05 0.21 0.34 1.51 0.14 0.59 4E-03 2E-02 2E-04 1E-03
0.05 0.21 0.34 1.51 2.73 11.98 4E-03 2E-02 2E-04 1E-03
19.53 87.03 15.62 73.18 20.85 103.35 1.75 7.79 0.19 0.86
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.** = Fugitive emissions of criteria pollutants are not included in major source determination because the facility is not a listed source category.
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Fugitive Sources
Threedubs Compressor Station (3WCS) - Fugitive Sources
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Point Sources
Threedubs Compressor Station (3WCS)Attachment U - Emission Estimates - Page 01 of 19
Criteria Pollutants - ControlledApplication for G35-D General Permit Registration
Threedubs Compressor Station (3WCS) - Point Sources
MMscfd200
6ESSM
TOx
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Criteria Pollutants - Controlled
Site RatingPM10/2.5 SO2VOC (w/HCHO)CONOXUnit
IDDescription
Control
ID
Point
ID
TLO 21E
VRU
lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy
CE-01 0.05 0.22 0.03 0.13 3E-03 0.01 2E-03 0.01 2E-04 1E-03 0.28 1.22 0.01 0.03 0.01 0.07 2E-03 0.01 2E-03 0.01 2E-03 0.01 1E-03 5E-03 2E-03 0.01 0.39 1.72
CE-02 0.05 0.22 0.03 0.13 3E-03 0.01 2E-03 0.01 2E-04 1E-03 0.28 1.22 0.01 0.03 0.01 0.07 2E-03 0.01 2E-03 0.01 2E-03 0.01 1E-03 5E-03 2E-03 0.01 0.39 1.72
CE-03 0.05 0.22 0.03 0.13 3E-03 0.01 2E-03 0.01 2E-04 1E-03 0.28 1.22 0.01 0.03 0.01 0.07 2E-03 0.01 2E-03 0.01 2E-03 0.01 1E-03 5E-03 2E-03 0.01 0.39 1.72
CE-04 0.05 0.22 0.03 0.13 3E-03 0.01 2E-03 0.01 2E-04 1E-03 0.28 1.22 0.01 0.03 0.01 0.07 2E-03 0.01 2E-03 0.01 2E-03 0.01 1E-03 5E-03 2E-03 0.01 0.39 1.72
CRP --- --- --- --- 0.01 0.04 --- --- 0.01 0.04 --- --- 0.12 0.51 --- --- --- --- 0.01 0.04 0.01 0.04 0.01 0.04 --- --- 0.16 0.72
--- --- --- --- --- 0.01 --- --- --- 0.01 --- --- --- 0.07 --- --- --- --- --- 0.01 --- 0.01 --- 0.01 --- --- --- 0.10
--- --- --- --- --- 2E-04 --- --- --- 2E-04 --- --- --- 3E-03 --- --- --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- --- --- 4E-03
--- --- --- --- --- 2E-04 --- --- --- 2E-04 --- --- --- 2E-03 --- --- --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- --- --- 3E-03
FLR --- --- --- --- --- --- --- --- --- --- --- 1E-03 --- --- --- --- --- 1E-05 --- --- --- --- --- --- --- 2E-05 --- 1E-03
GT 1E-03 0.01 2E-04 8E-04 4E-04 2E-03 1E-05 6E-05 9E-04 4E-03 0.02 0.09 --- --- --- --- 1E-03 4E-03 4E-03 0.02 --- --- 2E-03 0.01 9E-04 4E-03 0.03 0.14
DFT --- --- --- --- 4E-04 2E-03 --- --- 5E-04 2E-03 --- --- 0.02 0.10 --- --- --- --- 1E-03 5E-03 4E-04 2E-03 5E-04 2E-03 --- --- 0.03 0.11
DSV --- --- --- --- 0.04 0.16 --- --- 0.12 0.53 --- --- 0.06 0.27 --- --- --- --- 0.17 0.74 1E-03 5E-03 0.21 0.91 --- --- 0.60 2.61
RBV --- --- --- --- 4E-06 2E-05 --- --- --- --- 1E-04 6E-04 4E-03 0.02 --- --- 1E-06 6E-06 7E-06 3E-05 --- --- --- --- 2E-06 1E-05 4E-03 0.02
TOx --- --- --- --- --- --- --- --- --- --- 5E-04 2E-03 --- --- --- --- 4E-06 2E-05 --- --- --- --- --- --- 7E-06 3E-05 5E-04 2E-03
TK-01 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-02 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-03 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-04 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-05 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-06 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-07 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
TK-08 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01
--- --- --- --- --- 6E-03 --- --- --- 0.16 --- --- --- 0.58 --- --- --- --- --- 0.08 --- 0.05 --- 0.21 --- --- --- 1.08
--- --- --- --- --- 1E-04 --- --- --- 3E-03 --- --- --- 0.01 --- --- --- --- --- 1E-03 --- 1E-03 --- 4E-03 --- --- --- 0.02
3WCS-PS 0.20 0.88 0.12 0.54 0.06 0.27 0.01 0.03 0.14 0.76 1.13 4.96 0.24 1.71 0.06 0.26 0.01 0.04 0.19 0.94 2E-02 0.14 0.23 1.21 0.01 0.04 2.41 11.77
FUG-G --- --- --- --- 0.01 0.01 --- --- 0.01 0.01 --- --- 0.07 0.07 --- --- --- --- 0.01 0.01 0.01 0.01 0.01 0.01 --- --- 0.10 0.10
FUG-L --- --- --- --- 1E-03 6E-03 --- --- 0.03 0.15 --- --- 0.13 0.55 --- --- --- --- 0.02 0.07 0.01 0.05 0.04 0.20 --- --- 0.23 1.03
ECC 3E-03 0.01 2E-03 0.01 2E-04 8E-04 1E-04 5E-04 2E-05 7E-05 0.02 0.07 4E-04 2E-03 1E-03 4E-03 1E-04 6E-04 2E-04 7E-04 1E-04 5E-04 7E-05 3E-04 1E-04 6E-04 0.02 0.11
3WCS-FUG 3E-03 0.01 2E-03 0.01 0.01 0.01 1E-04 5E-04 0.04 0.16 0.02 0.07 0.20 0.63 1E-03 4E-03 1E-04 6E-04 0.02 0.08 0.02 0.06 0.05 0.20 1E-04 6E-04 0.36 1.23
3WCS-TOT 0.20 0.89 0.13 0.55 0.07 0.28 0.01 0.03 0.18 0.91 1.15 5.03 0.44 2.34 0.06 0.27 0.01 0.04 0.22 1.02 0.04 0.20 0.28 1.41 0.01 0.04 2.77 13.00
TVOP**: 10 10 10 10 10 10 10 10 10 10 10 10 10 25
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.** = Fugitive emissions of hazardous air pollutants (HAP) are included in major source determination regardless of whether the source falls within a listed source category.
Threedubs Compressor Station (3WCS)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Hazardous Air Pollutants (HAP) - Controlled
Unit
ID
n-HexaneHCHOEthylbenzeneBenzene TOTAL HAPsXylenesTMP, 2,2,4- Other HAPAcetaldehyde Acrolein POM/PAHButadiene, 1,3-
Threedubs Compressor Station (3WCS) - Point Sources
TolueneMethanol
Attachment U - Emission Estimates - Page 02 of 19Hazardous Air Pollutants (HAP) - Controlled
Application for G35-D General Permit Registration
SSM
TLO
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Fugitive Sources
CO2 CO2e CH4 CO2e N2O CO2e
GWP: 1.00 GWP: 25.00 GWP: 298.00
hr/yr* tpy tpy tpy tpy tpy tpy lb/hr* tpy
CE-01 OxCat-01 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-02 OxCat-02 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-03 OxCat-03 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-04 OxCat-04 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CRP --- 5 Recip's --- 8,760 0.26 0.26 61.49 1,537 --- --- 351 1,537
--- 422 Events/yr --- --- 0.03 0.03 8.27 207 --- --- --- 207
--- 1 Event/yr --- --- 1E-03 1E-03 0.35 8.78 --- --- --- 8.78
--- 156 Events/yr --- --- 1E-03 1E-03 0.30 7.42 --- --- --- 7.42
FLR --- 3.49 MMBtu/hr 3.49 8,760 1,788 1,788 --- --- 3E-03 1.00 --- 1,789
GT --- 1,742 bhp 29.62 8,760 14,270 14,270 1.12 28 0.39 116 3,291 14,414
DFT --- 8,760 6.20 6.20 3.49 87.21 --- --- 21.33 93.41
DSV --- 8,760 4.69 4.69 0.20 4.90 --- --- 2.19 9.59
RBV --- 2.0 MMBtu/hr 2.00 8,760 1,025 1,025 0.02 0.48 2E-03 0.58 234 1,026
TOx --- 6.21 MMBtu/hr 6.21 8,760 3,182 3,182 --- --- 0.01 1.79 727 3,184
TK-01 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-02 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-03 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-04 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-05 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-06 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-07 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-08 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
228,000 bbl/yr --- --- --- --- --- --- --- --- --- ---
30,000 bbl/yr --- --- --- --- --- --- --- --- --- ---
105,830 105,830 436 10,909 0.54 162.31 26,230 116,901
FUG-G --- Process Piping Fugitives - Gas 4,981 Fittings --- 8,760 0.04 0.04 8.63 216 --- --- 49.27 216
FUG-L --- Process Piping Fugitives - Light Liquid 2,271 Fittings --- 8,760 --- --- --- --- --- --- --- ---
ECC --- 4 Engines --- --- 227.85 227.85 0.96 24.04 4E-04 0.11 57.54 252.01
227.88 227.88 9.59 240 4E-04 0.11 107 468
106,058 106,058 446 11,149 0.55 162.42 26,337 117,369
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.** = Greenhouse gases (GHG) are not treated as air pollutants for major source determination.
Pigging Operations (PIG)
Appalachia Midstream Services, LLC (AMS)
Unit
IDDescription
Application for G35-D General Permit Registration
TOTAL
CO2e
Hours of
OperationSite Rating
Heat Input
MMBtu/hr
(HHV)
Threedubs Compressor Station (3WCS)
Greenhouse Gas (GHG) Pollutants - Controlled
Threedubs Compressor Station (3WCS) - Point Sources
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Fugitive Sources
Engine Crankcase
Threedubs Compressor Station (3WCS) - Fugitive Sources
Threedubs Compressor Station (3WCS) - Total PTE
Attachment U - Emission Estimates - Page 03 of 19Greenhouse Gas (GHG) Pollutants - Controlled
VRU
TOx
Threedubs Compressor Station (3WCS) - Point Sources
Compressor Engine 02 - CAT G3616LE A4Compressor Engine 01 - CAT G3616LE A4
Compressor Engine 03 - CAT G3616LE A4Compressor Engine 04 - CAT G3616LE A4Compressor Rod Packing
Control
ID
Compressor Blowdown (CBD)Emergency Shutdown (ESD) TestingSSM
MMscfd
Storage Tank 03 - Stabilized Condensate
SSM Flare - Zeeco MJ-16 (Comb. Only)Microturbine Generator - FlexEnergy GT1300SDehydrator - Flash Tank
TLO
200
Truck Load-Out - Stabilized CondensateTruck Load-Out - Produced Water
Storage Tank 04 - Stabilized CondensateStorage Tank 05 - Stabilized CondensateStorage Tank 06 - Stabilized CondensateStorage Tank 07 - Produced WaterStorage Tank 08 - Produced Water
Dehydrator - Reboiler VentThermal Oxidizer - Zeeco Z-HTO (Comb. Only)Storage Tank 01 - Stabilized CondensateStorage Tank 02 - Stabilized Condensate
Dehydrator - Still Vent
lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy
CE-01 1E OxCat-01 Compressor Engine 01 - CAT G3616LE A4 5,000 bhp 4.41 19.31 32.30 141.46 10.58 46.35 0.37 1.63 0.02 0.10CE-02 2E OxCat-02 Compressor Engine 02 - CAT G3616LE A4 5,000 bhp 4.41 19.31 32.30 141.46 10.58 46.35 0.37 1.63 0.02 0.10CE-03 3E OxCat-03 Compressor Engine 03 - CAT G3616LE A4 5,000 bhp 4.41 19.31 32.30 141.46 10.58 46.35 0.37 1.63 0.02 0.10CE-04 4E OxCat-04 Compressor Engine 04 - CAT G3616LE A4 5,000 bhp 4.41 19.31 32.30 141.46 10.58 46.35 0.37 1.63 0.02 0.10CRP 5E --- Compressor Rod Packing 5 Recip's --- --- --- --- 6.88 30.15 --- --- --- ---
--- Compressor Blowdown (CBD) 422 Events/yr --- --- --- --- --- 4.06 --- --- --- --- --- Emergency Shutdown (ESD) Testing 1 Event/yr --- --- --- --- --- 0.17 --- --- --- --- --- Pigging Operations (PIG) 156 Events/yr --- --- --- --- --- 0.15 --- --- --- ---
FLR 7E --- SSM Flare - Zeeco MJ-16 (Comb. Only) 3.49 MMBtu/hrGT 8E --- Microturbine Generator - FlexEnergy GT1300S 1,742 bhp 1.04 4.55 2.86 12.51 0.28 1.23 0.20 0.86 0.10 0.44
DFT 9E Dehydrator - Flash Tank --- --- --- --- 55.78 244.33 --- --- --- ---DSV 10E Dehydrator - Still Vent --- --- --- --- 73.74 322.98 --- --- --- ---RBV 11E --- Dehydrator - Reboiler Vent 2.0 MMBtu/hr 0.20 0.86 0.16 0.72 0.01 0.05 0.01 0.07 1E-03 0.01TOx 12E --- Thermal Oxidizer - Zeeco Z-HTO (Comb. Only) 6.21 MMBtu/hr
TK-01 13E Storage Tank 01 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-02 14E Storage Tank 02 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-03 15E Storage Tank 03 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-04 16E Storage Tank 04 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-05 17E Storage Tank 05 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-06 18E Storage Tank 06 - Stabilized Condensate 400 bbl --- --- --- --- 0.69 3.04 --- --- --- ---TK-07 19E Storage Tank 07 - Produced Water 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---TK-08 20E Storage Tank 08 - Produced Water 400 bbl --- --- --- --- 0.01 0.06 --- --- --- ---
Truck Load-Out - Stabilized Condensate 228,000 bbl/yr --- --- --- --- --- 22.43 --- --- --- ---Truck Load-Out - Produced Water 30,000 bbl/yr --- --- --- --- --- 0.42 --- --- --- ---
18.87 82.66 132.21 579.09 183.22 829.73 1.70 7.46 0.19 0.83
FUG-G 1F --- Process Piping Fugitives - Gas 4,981 Fittings --- --- --- --- 4.12 18.04 --- --- --- ---FUG-L 2F --- Process Piping Fugitives - Light Liquid 2,271 Fittings --- --- --- --- 1.63 7.15 --- --- --- ---ECC 3F --- Engine Crankcase 4 Engines 0.05 0.21 0.34 1.51 0.14 0.59 4E-03 2E-02 2E-04 1E-03
0.05 0.21 0.34 1.51 5.89 25.79 4E-03 2E-02 2E-04 1E-03
18.92 82.86 132.56 580.59 189.11 855.51 1.71 7.47 0.19 0.83
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.
Threedubs Compressor Station (3WCS) - Fugitive Sources
21ETLO
Threedubs Compressor Station (3WCS) - Fugitive Sources
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS)Criteria Pollutants - PRE-Controlled
Application for G35-D General Permit RegistrationAttachment U - Emission Estimates - Page 04 of 19
Shading indicates Controlled Emissions
VRU
TOx
No PRE-Controlled Emissions from the SSM Flare
No PRE-Controlled Emissions from the Thermal Oxider
Threedubs Compressor Station (3WCS) - Point Sources
SSM 6E
200 MMscfd
Threedubs Compressor Station (3WCS) - Point Sources
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Criteria Pollutants - PRE-Controlled
Control
IDDescription Site Rating
NOX CO VOC (w/HCHO) PM10/2.5Point
ID
SO2Unit
ID
lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy lb/hr* tpy
CE-01 0.31 1.37 0.19 0.84 0.02 0.07 0.01 0.04 1E-03 0.01 1.54 6.76 0.04 0.18 0.09 0.41 0.01 0.06 0.02 0.07 0.01 0.04 0.01 0.03 0.01 0.05 2.27 9.93
CE-02 0.31 1.37 0.19 0.84 0.02 0.07 0.01 0.04 1E-03 0.01 1.54 6.76 0.04 0.18 0.09 0.41 0.01 0.06 0.02 0.07 0.01 0.04 0.01 0.03 0.01 0.05 2.27 9.93
CE-03 0.31 1.37 0.19 0.84 0.02 0.07 0.01 0.04 1E-03 0.01 1.54 6.76 0.04 0.18 0.09 0.41 0.01 0.06 0.02 0.07 0.01 0.04 0.01 0.03 0.01 0.05 2.27 9.93
CE-04 0.31 1.37 0.19 0.84 0.02 0.07 0.01 0.04 1E-03 0.01 1.54 6.76 0.04 0.18 0.09 0.41 0.01 0.06 0.02 0.07 0.01 0.04 0.01 0.03 0.01 0.05 2.27 9.93
CRP --- --- --- --- 0.01 0.04 --- --- 0.01 0.04 --- --- 0.12 0.51 --- --- --- --- 0.01 0.04 0.01 0.04 0.01 0.04 --- --- 0.16 0.72
--- --- --- --- --- 0.01 --- --- --- 0.01 --- --- --- 0.07 --- --- --- --- --- 0.01 --- 0.01 --- 0.01 --- --- --- 0.10
--- --- --- --- --- 2E-04 --- --- --- 2E-04 --- --- --- 3E-03 --- --- --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- --- --- 4E-03
--- --- --- --- --- 2E-04 --- --- --- 2E-04 --- --- --- 2E-03 --- --- --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- --- --- 3E-03
FLRGT 1E-03 0.01 2E-04 8E-04 4E-04 2E-03 1E-05 6E-05 9E-04 4E-03 0.02 0.09 --- --- --- --- 1E-03 4E-03 4E-03 0.02 --- --- 2E-03 0.01 9E-04 4E-03 0.03 0.14
DFT --- --- --- --- 0.02 0.09 --- --- 0.02 0.10 --- --- 1.12 4.91 --- --- --- --- 0.06 0.26 0.02 0.09 0.03 0.12 --- --- 1.27 5.58
DSV --- --- --- --- 1.87 8.18 --- --- 6.04 26.44 --- --- 3.11 13.61 --- --- --- --- 8.41 36.83 0.06 0.27 10.35 45.35 --- --- 29.84 131
RBV --- --- --- --- 4E-06 2E-05 --- --- --- --- 1E-04 6E-04 4E-03 0.02 --- --- 1E-06 6E-06 7E-06 3E-05 --- --- --- --- 2E-06 1E-05 4E-03 0.02
TOxTK-01 --- --- --- --- 5E-04 2E-03 --- --- 0.01 0.06 --- --- 0.05 0.23 --- --- --- --- 0.01 0.03 5E-03 0.02 0.02 0.08 --- --- 0.10 0.44TK-02 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01TK-03 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01TK-04 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01TK-05 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01TK-06 --- --- --- --- 1E-05 5E-05 --- --- 3E-04 1E-03 --- --- 1E-03 5E-03 --- --- --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 --- --- 2E-03 0.01TK-07 --- --- --- --- 2E-07 9E-07 --- --- 6E-06 3E-05 --- --- 2E-05 9E-05 --- --- --- --- 3E-06 1E-05 2E-06 8E-06 7E-06 3E-05 --- --- 4E-05 0.00TK-08 --- --- --- --- 2E-07 9E-07 --- --- 6E-06 3E-05 --- --- 2E-05 9E-05 --- --- --- --- 3E-06 1E-05 2E-06 8E-06 7E-06 3E-05 --- --- 4E-05 0.00
--- --- --- --- --- 0.02 --- --- --- 0.47 --- --- --- 1.73 --- --- --- --- --- 0.24 --- 0.16 --- 0.61 --- --- --- 3.22 --- --- --- --- --- 3E-04 --- --- --- 0.01 --- --- --- 0.03 --- --- --- --- --- 4E-03 --- 3E-03 --- 0.01 --- --- --- 0.06
3WCS-PS 1.25 5.47 0.77 3.36 1.97 8.63 0.04 0.17 6.09 27.17 6.19 27.13 4.57 21.87 0.37 1.64 0.05 0.23 8.55 37.69 0.14 0.77 10.44 46.36 0.05 0.21 40.49 180.71
FUG-G --- --- --- --- 0.03 0.03 --- --- 0.03 0.03 --- --- 0.30 0.30 --- --- --- --- 0.03 0.03 0.03 0.03 0.03 0.03 --- --- 0.43 0.43FUG-L --- --- --- --- 5E-03 0.02 --- --- 0.12 0.55 --- --- 0.46 2.02 --- --- --- --- 0.06 0.27 0.04 0.18 0.16 0.71 --- --- 0.86 3.75ECC 3E-03 0.01 2E-03 0.01 2E-04 8E-04 1E-04 5E-04 2E-05 7E-05 0.02 0.07 4E-04 2E-03 1E-03 4E-03 1E-04 6E-04 2E-04 7E-04 1E-04 5E-04 7E-05 3E-04 1E-04 6E-04 0.02 0.11
3WCS-FUG 3E-03 0.01 2E-03 0.01 0.03 0.05 1E-04 5E-04 0.15 0.57 0.02 0.07 0.76 2.32 1E-03 4E-03 1E-04 6E-04 0.09 0.30 0.07 0.21 0.19 0.74 1E-04 6E-04 1.31 4.29
3WCS-TOT 1.25 5.49 0.77 3.37 2.00 8.68 0.04 0.18 6.24 27.74 6.21 27.20 5.34 24.19 0.37 1.64 0.05 0.23 8.64 37.99 0.20 0.98 10.63 47.10 0.05 0.21 41.80 185.00
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.
Threedubs Compressor Station (3WCS)
SSM
Hazardous Air Pollutants (HAP) - PRE-ControlledApplication for G35-D General Permit Registration
Attachment U - Emission Estimates - Page 05 of 19
TLO
No PRE-Controlled Emissions from the Thermal Oxider
No PRE-Controlled Emissions from the SSM Flare
Shading indicates Controlled Emissions
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Fugitive Sources
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Hazardous Air Pollutants (HAP) - PRE-Controlled
Unit
ID
Acetaldehyde Acrolein Benzene Butadiene, 1,3- Ethylbenzene HCHO n-Hexane Other HAP TOTAL HAPs
Threedubs Compressor Station (3WCS) - Point Sources
Methanol POM/PAH Toluene TMP, 2,2,4- Xylenes
CO2 CO2e CH4 CO2e N2O CO2e
GWP: 1.00 GWP: 25.00 GWP: 298.00
hr/yr* tpy tpy tpy tpy tpy tpy lb/hr* tpy
CE-01 OxCat-01 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-02 OxCat-02 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-03 OxCat-03 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CE-04 OxCat-04 5,000 bhp 37.33 8,760 21,389 21,389 90.29 2,257 0.04 10.74 5,401 23,656
CRP --- 5 Recip's --- 8,760 0.26 0.26 61.49 1,537 --- --- 351 1,537
--- 422 Events/yr --- --- 0.03 0.03 8.27 206.84 --- --- --- 207
--- 1 Event/yr --- --- 1E-03 1E-03 0.35 8.78 --- --- --- 8.78
--- 156 Events/yr --- --- 1E-03 1E-03 0.30 7.42 --- --- --- 7.42
FLR --- 3.49 MMBtu/hr 3.49 8,760GT --- 1,742 bhp 29.62 8,760 14,270 14,270 1.12 28 0.39 116 3,291 14,414
DFT --- 8,760 6.20 6.20 174 4,360 --- --- 997 4,367
DSV --- 8,760 4.69 4.69 9.79 245 --- --- 56.97 250
RBV --- 2.0 MMBtu/hr 2.00 8,760 1,025 1,025 0.02 0.48 2E-03 0.58 234 1,026
TOx --- 6.21 MMBtu/hr 6.21 8,760TK-01 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-02 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-03 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-04 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-05 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-06 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-07 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
TK-08 400 bbl --- 8,760 --- --- --- --- --- --- --- ---
228,000 bbl/yr --- --- --- --- --- --- --- --- --- ---
30,000 bbl/yr --- --- --- --- --- --- --- --- --- ---
100,860 100,860 617 15,423 0.54 159.52 26,534 116,442
FUG-G --- Process Piping Fugitives - Gas 4,981 Fittings --- 8,760 0.04 0.04 8.63 216 --- --- 49 216
FUG-L --- Process Piping Fugitives - Light Liquid 2,271 Fittings --- 8,760 --- --- --- --- --- --- --- ---
ECC --- 4 Engines --- --- 227.85 227.85 0.96 24.04 4E-04 0.11 57.54 252.01
227.88 227.88 9.59 240 4E-04 0.11 107 468
101,088 101,088 626 15,662 0.54 159.63 26,641 116,910
* = lb/hr is based on 8,760 hr/yr, except Start/Stop/Maintenance (SSM), SSM Flare (FLR), and Truck Load-Out (TLO) which operate less frequent.
Threedubs Compressor Station (3WCS) - Fugitive Sources
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) - Total PTE
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Shading indicates Controlled Emissions
Attachment U - Emission Estimates - Page 06 of 19Greenhouse Gas (GHG) Pollutants - PRE-Controlled
Threedubs Compressor Station (3WCS) - Point Sources
SSM
200 MMscfd
Compressor Blowdown (CBD)Emergency Shutdown (ESD) TestingPigging Operations (PIG)
Compressor Rod Packing
Compressor Engine 01 - CAT G3616LE A4Compressor Engine 02 - CAT G3616LE A4Compressor Engine 03 - CAT G3616LE A4Compressor Engine 04 - CAT G3616LE A4
Unit
ID
Control
IDDescription Site Rating
Heat Input
MMBtu/hr
(HHV)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Greenhouse Gas (GHG) Pollutants - PRE-Controlled
Hours of
Operation
TOTAL
CO2e
Threedubs Compressor Station (3WCS) - Fugitive Sources
Engine Crankcase
TLO
VRUStorage Tank 05 - Stabilized CondensateStorage Tank 06 - Stabilized CondensateStorage Tank 07 - Produced WaterStorage Tank 08 - Produced WaterTruck Load-Out - Stabilized Condensate
Storage Tank 01 - Stabilized CondensateStorage Tank 02 - Stabilized CondensateStorage Tank 03 - Stabilized CondensateStorage Tank 04 - Stabilized Condensate
TOx
No PRE-Controlled Emissions from the SSM Flare
No PRE-Controlled Emissions from the Thermal Oxider
Truck Load-Out - Produced WaterThreedubs Compressor Station (3WCS) - Point Sources
Dehydrator - Reboiler Vent
Dehydrator - Flash TankDehydrator - Still Vent
SSM Flare - Zeeco MJ-16 (Comb. Only)Microturbine Generator - FlexEnergy GT1300S
Thermal Oxidizer - Zeeco Z-HTO (Comb. Only)
g/bhp-hr lb/MMBtu lb/hr tpy g/bhp-hr lb/hr tpy
Vendor Data# NOX 0.40 0.12 4.41 19.31 --- 0.40 4.41 19.31
Vendor Data CO 2.93 0.87 32.30 141.46 92.0% 0.23 2.58 11.32
Vendor Data NMNEHC 0.96 0.28 10.58 46.35 84.0% 0.15 1.69 7.42
Sum VOC (w/Aldehydes)* 1.15 0.34 12.72 55.73 83.8% 0.19 2.07 9.05
AP-42 Table 3.2-2 PM10/2.5 3.38E-02 9.99E-03 0.37 1.63 --- 0.03 0.37 1.63
AP-42 Table 3.2-2 SO2 1.99E-03 5.88E-04 0.02 0.10 --- 2E-03 0.02 0.10
AP-42 Table 3.2-2 *Acetaldehyde 2.83E-02 8.36E-03 0.31 1.37 84.0% 5E-03 0.05 0.22
5,000 bhp (Each) AP-42 Table 3.2-2 *Acrolein 1.74E-02 5.14E-03 0.19 0.84 84.0% 3E-03 0.03 0.13
8,760 hr/yr (Each) AP-42 Table 3.2-2 Benzene 1.49E-03 4.40E-04 0.02 0.07 84.0% 2E-04 3E-03 0.01
1,000 rpm, 16 cyl AP-42 Table 3.2-2 Butadiene, 1,3- 9.04E-04 2.67E-04 0.01 0.04 84.0% 1E-04 2E-03 0.01
1,294 in3/cyl AP-42 Table 3.2-2 Ethylbenzene 1.34E-04 3.97E-05 1E-03 6E-03 84.0% 2E-05 2E-04 1E-03
Vendor Data *Formaldehyde 0.14 0.04 1.54 6.76 82.0% 0.03 0.28 1.22
814 Exhaust Temp (oF) AP-42 Table 3.2-2 n-Hexane 3.76E-03 1.11E-03 0.04 0.18 84.0% 6E-04 0.01 0.03
31,291 Exhaust Flow (acfm) AP-42 Table 3.2-2 *Methanol 8.47E-03 2.50E-03 0.09 0.41 84.0% 1E-03 0.01 0.07
AP-42 Table 3.2-2 POM/PAH 1.17E-03 3.47E-04 0.01 0.06 84.0% 2E-04 2E-03 0.01
MFD: > 08/23/11 AP-42 Table 3.2-2 Toluene 1.38E-03 4.08E-04 0.02 0.07 84.0% 2E-04 2E-03 0.01
AP-42 Table 3.2-2 TMP, 2,2,4- 9.04E-04 2.67E-04 0.01 0.04 84.0% 1E-04 2E-03 0.01
AP-42 Table 3.2-2 Xylenes 6.23E-04 1.84E-04 0.01 0.03 84.0% 1E-04 1E-03 5E-03
7,466 Btu/bhp-hr (HHV) AP-42 Table 3.2-2 Other/Trace HAP 1.09E-03 3.21E-04 0.01 0.05 84.0% 2E-04 2E-03 0.01
37.33 MMBtu/hr (HHV) (Each) AP-42 Table 3.2-2 Total HAP 0.21 0.06 2.27 9.93 82.6% 0.04 0.39 1.72
36,598 scf/hr (Each) Vendor Data CO2 (GWP=1) 443 130.81 4,883 21,389 --- 443 4,883 21,389
320.60 MMscf/yr (Each) Vendor Data CH4 (GWP=25) 1.87 0.55 20.61 90.29 --- 1.87 20.61 90.29
1,020 Btu/scf (HHV) 40CFR98 - Table C2 N2O (GWP=298) 7.47E-04 2.20E-04 0.01 0.04 --- 7E-04 0.01 0.04
Weighted Sum CO2e 490 145 5,401 23,656 --- 490 5,401 23,656
# = Vendor data indicates NOX is 0.30 g/bhp-hr; however, 0.40 g/bhp-hr is more conservative and still less than the NSPS JJJJ limitation of 1.0 g/bhp-hr.* = As per vendor data, the VOC Emission Factor is the sum of NMNEHC plus Aldehydes and Methanol.
Notes: 1 - The emissions shown are based on operation at 100% of rated load for 8,760 hr/yr. Actual load and operating hours will be less. 2 - As per vendor data, emission values are based on adjustment to specified NOX level, all other emission values are "Not to Exceed" (i.e., Vendor Guarantee).3 - PM10/2.5 is filterable and condensable particulate matter; including PM10 and PM2.5
5 - The fuel heating value will vary, 1,020 Btu/scf (HHV) is at the low end of the range and results in a high (conservative) fuel consumption estimate.6 - Total NMNEHC, VOC, HCHO, HAP and CO2e emissions include Compressor Rod Packing (CRP), Compressor Blowdown (CBD), Engine Start-up (ESU), and Engine Crankcase (ECC) Emissions:
NMNEHC VOC HCHO Tot HAP CO2e
7.42 tpy 9.05 tpy 1.22 tpy 1.72 tpy 23,656 tpy6.46 tpy 6.46 tpy --- 0.15 tpy 329 tpy1.01 tpy 1.01 tpy --- 0.02 tpy 52 tpy
0.13 tpy 0.15 tpy 0.02 tpy 0.03 tpy 63.00 tpy15.02 tpy 16.67 tpy 1.23 tpy 1.93 tpy 24,101 tpy
Threedubs Compressor Station (3WCS)Attachment U - Emission Estimates - Page 07 of 19Compressor Engine (CE-01 thru CE-04) Emissions
Pre-Controlled
Emissions
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Compressor Engine (CE-01 thru CE-04) Emissions
Control
Efficiency
Controlled
Emissions
Engine Crankcase (ECC)
Compressor Blowdown (CBD)Compressor Rod Packing (CRP)
Source
ID
NSPS JJJJ Affected
Description Reference Pollutant
Application for G35-D General Permit Registration
CE-01 (1E)CE-02 (2E)CE-03 (3E)CE-04 (4E)
(Each)
Engine Operations (See Above)
Engine Start-up (ESU)
Description (Each Engine w/ Compressor)
TOTAL:
Caterpillar (CAT) G3616LE A4 (4SLB)
Compressor Engines 01 thru 04 (Each)
(OxCat-01 thru OxCat-04)
4 - "Other/Trace HAPs" includes: Carbon Tetrachloride, Chlorobenzene, Chloroform, Dichloropropene, 1,3-Dichloropropene, Ethylene Dibromide, Methylene Chloride, Phenol, Propylene Oxide, Styrene, 1,1,2,2-Tetrachloroethane, 1,1,2-Trichloroethane, and Vinyl Chloride (as per AP-42).
Electric or Pneumatic Starters are utilized
scfh MMscfy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
6 12.0 15% 82.80 0.73 1.48 6.46 0.01 0.06 3.01 13.18 75 3296 12.0 15% 82.80 0.73 1.48 6.46 0.01 0.06 3.01 13.18 75 3296 12.0 15% 82.80 0.73 1.48 6.46 0.01 0.06 3.01 13.18 75 3296 12.0 15% 82.80 0.73 1.48 6.46 0.01 0.06 3.01 13.18 75 3294 12.0 15% 55.20 0.48 0.98 4.31 0.01 0.04 2.01 8.78 50 220
TOTAL: 386.40 3.38 TOTAL: 6.88 30.15 0.06 0.26 14.04 61.49 351 1,537
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
2E-03 0.01 2E-03 0.01 0.02 0.11 2E-03 0.01 2E-03 0.01 2E-03 0.01 0.04 0.152E-03 0.01 2E-03 0.01 0.02 0.11 2E-03 0.01 2E-03 0.01 2E-03 0.01 0.04 0.152E-03 0.01 2E-03 0.01 0.02 0.11 2E-03 0.01 2E-03 0.01 2E-03 0.01 0.04 0.152E-03 0.01 2E-03 0.01 0.02 0.11 2E-03 0.01 2E-03 0.01 2E-03 0.01 0.04 0.151E-03 0.01 1E-03 0.01 0.02 0.07 1E-03 0.01 1E-03 0.01 1E-03 0.01 0.02 0.100.01 0.04 0.01 0.04 0.12 0.51 1E-02 0.04 1E-02 0.04 1E-02 0.04 0.16 0.72
Notes:
%Total %VOC
127 lb/MMscf 153 lb/MMscf 0.224 0.85830,275 lb/MMscf 36,331 lb/MMscf 53.343 203.92913,808 lb/MMscf 13,808 lb/MMscf 20.274 77.50814,846 lb/MMscf 17,815 lb/MMscf 26.158 100.00059,057 lb/MMscf 68,107 lb/MMscf 100.000 ---
1.60 lb/MMscf 25.00 lb/MMscf 0.037 0.1403.71 lb/MMscf 25.00 lb/MMscf 0.037 0.140181 lb/MMscf 300 lb/MMscf 0.440 1.684
5.80 lb/MMscf 25.00 lb/MMscf 0.037 0.1405.51 lb/MMscf 25.00 lb/MMscf 0.037 0.140
4 lb/MMscf 25.00 lb/MMscf 0.037 0.140202 lb/MMscf 425 lb/MMscf 0.624 2.386
CRP(5E)
CRP(5E)
425
lb/MMscf lb/MMscf
25.00
Recip Compressor - 05 (Electric Motor)
Recip Compressor - 01 (Gas Engine)
Recip Compressor - 01 (Gas Engine)Recip Compressor - 02 (Gas Engine)
Recip Compressor - 05 (Electric Motor)
lb/MMscf
Tot HAP
Recip Compressor - 02 (Gas Engine)
25.00 25.00
Threedubs Compressor Station (3WCS)Compressor Rod Packing (CRP) Emissions
Attachment U - Emission Estimates - Page 08 of 19Application for G35-D General Permit Registration
Total HAP
TOTAL Gas
Source
ID
Benzene
CO2Methane (CH4)
Xylenes
VOC
Benzene
lb/MMscf
Unit Description
(Compressor Rod Packing)
2,2,4-TMP
Ethylbenzenen-HexaneToluene
N2/Water/Ethane/Etc
TOTAL:
2 - The results of a representative Wet Gas Analysis were used to determine the following worst-case components (See Appendix S1 - Wet Gas Summary):
Pollutant Wet Gas Worst Case
Min. Contingency:
1 - As per the manufacturer (Ariel): "Packing in new and broken-in condition will leak 5-10 scfh through the vent. This leakage rate will increase over time due to wear of the non-metallic sealing rings." The Williams' engineering department provides a conservative leak rate estimate of 12 scfh/cylinder.
20% VOC and GHG
Appalachia Midstream Services, LLC (AMS)
Application for G35-D General Permit Registration
Unit Description
(Compressor Rod Packing) lb/MMscf
300
CO2Total Fugitive
Leak RateNo of
Cylinders
scfh per
Cylinder lb/MMscf
Threedubs Compressor Station (3WCS)
CO2e
Source
ID
VOC
Compressor Rod Packing (CRP) Emissions
Contin-
gencyCH4 GWP = 25
n-Hexane
CH4
Toluene 2,2,4-TMP Xylene
36,33117,815
lb/MMscf
Recip Compressor - 03 (Gas Engine)Recip Compressor - 04 (Gas Engine)
lb/MMscf
Control
Efficiency
153
na
E-Benzene
Recip Compressor - 04 (Gas Engine)
25.00
lb/MMscf lb/MMscf
25.00
Recip Compressor - 03 (Gas Engine)
17,815 Gas 153 Gas 36,331 Gas
bhp scf/bhp scf/Event Events/yr Mscf/yr lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
5,000 10.95 54,732 104 5,692 --- 1.01 --- 0.01 --- 2.07 --- 51.71
5,000 10.95 54,732 104 5,692 --- 1.01 --- 0.01 --- 2.07 --- 51.71
5,000 10.95 54,732 104 5,692 --- 1.01 --- 0.01 --- 2.07 --- 51.71
5,000 10.95 54,732 104 5,692 --- 1.01 --- 0.01 --- 2.07 --- 51.71
50 8.00 400 6 2.40 --- 4E-04 --- 4E-06 --- 9E-04 --- 0.02
50 8.00 400 6 2.40 --- 4E-04 --- 2E-04 --- 9E-04 --- 0.02
20,050 48.23 967,000 1 967 --- 0.17 --- 1E-03 --- 0.35 --- 8.78
--- --- 3,823 52 199 --- 0.04 --- 3E-04 --- 0.07 --- 1.81
--- --- 3,823 52 199 --- 0.04 --- 3E-04 --- 0.07 --- 1.81
--- --- 8,064 52 419 --- 0.07 --- 6E-04 --- 0.15 --- 3.81
Assumes 1 hr/Event TOTAL: 585 24,557 TOTAL: --- 4.37 --- 0.04 --- 8.92 --- 223.08
Pre-Control: 219 1.89 446 11,154
25.00 Gas 25.00 Gas 300.00 Gas 25.00 Gas 25.00 Gas 25.00 Gas 425.00 Gas
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
--- 1E-03 --- 1E-03 --- 0.02 --- 1E-03 --- 1E-03 --- 1E-03 1.21 0.02
--- 1E-03 --- 1E-03 --- 0.02 --- 1E-03 --- 1E-03 --- 1E-03 1.21 0.02
--- 1E-03 --- 1E-03 --- 0.02 --- 1E-03 --- 1E-03 --- 1E-03 1.21 0.02
--- 1E-03 --- 1E-03 --- 0.02 --- 1E-03 --- 1E-03 --- 1E-03 1.21 0.02
--- 6E-07 --- 6E-07 --- 7E-06 --- 6E-07 --- 6E-07 --- 6E-07 5E-04 1E-05
--- 6E-07 --- 6E-07 --- 7E-06 --- 6E-07 --- 6E-07 --- 6E-07 5E-04 1E-05
--- 2E-04 --- 2E-04 --- 3E-03 --- 2E-04 --- 2E-04 --- 2E-04 0.21 4E-03
--- 5E-05 --- 5E-05 --- 6E-04 --- 5E-05 --- 5E-05 --- 5E-05 0.04 8E-04
--- 5E-05 --- 5E-05 --- 6E-04 --- 5E-05 --- 5E-05 --- 5E-05 0.04 8E-04
--- 1E-04 --- 1E-04 --- 1E-03 --- 1E-04 --- 1E-04 --- 1E-04 0.09 2E-03
Assumes 1 hr/Event TOTAL: --- 0.01 --- 0.01 --- 0.07 --- 0.01 --- 0.01 --- 0.01 5.22 0.10
Pre-Control: 0.31 0.31 3.68 0.31 0.31 0.31 5.22
Notes: 1 - The results of a representative Wet Gas Analysis were used to determine the following worst-case components (See Appendix S1 - Wet Gas Summary):
%Total %VOC
127 lb/MMscf 153 lb/MMscf 0.224 0.858
30,275 lb/MMscf 36,331 lb/MMscf 53.343 203.929
13,808 lb/MMscf 13,808 lb/MMscf 20.274 77.508
14,846 lb/MMscf 17,815 lb/MMscf 26.158 100.000
59,057 lb/MMscf 68,107 lb/MMscf 100.000 ---
1.60 lb/MMscf 25.00 lb/MMscf 0.037 0.140
3.71 lb/MMscf 25.00 lb/MMscf 0.037 0.140
181 lb/MMscf 300 lb/MMscf 0.440 1.684
5.80 lb/MMscf 25.00 lb/MMscf 0.037 0.140
5.51 lb/MMscf 25.00 lb/MMscf 0.037 0.140
4 lb/MMscf 25.00 lb/MMscf 0.037 0.140
202 lb/MMscf 425 lb/MMscf 0.624 2.386
n-Hexane Toluene
lb/MMscf
Control
%
Recip Comp - 04 (Gas Engine) (CBD)
Blowdown
Gas
2,2,4-TMP Xylene
lb/MMscflb/MMscf lb/MMscf
Benzene
CH4 GWP = 25
CH4VOC CO2
lb/MMscf
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
lb/MMscf
Appalachia Midstream Services, LLC (AMS)
Source
IDUnit Description
Site
Rating
lb/MMscf
Total HAP
Blowdown
and ESD
Recip Comp - 02 (Gas Engine) (CBD)
Ethylbenzene
Start/Stop/Maintenance (SSM - CBD/ESD/PIG) Emissions
CO2e
lb/MMscf
Recip Comp - 03 (Gas Engine) (CBD)
SSM (6E)
lb/MMscf
Source
ID
Recip Comp - 05 (Electric Motor) (CBD)
16" Receiver A (PIG)
16" Receiver B (PIG)
16" Launcher (PIG)
Rotary Comp - 06 (Electric Motor) (CBD)
lb/MMscf
Total Gas
Vented
98%
Unit Description
Emission
Factor
Recip Comp - 01 (Gas Engine) (CBD)
Emergency Shutdown (ESD) Testing
Recip Comp - 02 (Gas Engine) (CBD)
Rotary Comp - 06 (Electric Motor) (CBD)
2,2,4-TMP
Wet GasPollutant
Min. Contingency:
SSM (6E)
Recip Comp - 03 (Gas Engine) (CBD)
Threedubs Compressor Station (3WCS)
CO2
Methane (CH4)
N2/Water/Ethane/Etc
VOC
Benzene
16" Receiver B (PIG)
16" Launcher (PIG)
Recip Comp - 04 (Gas Engine) (CBD)
Recip Comp - 05 (Electric Motor) (CBD)
Emergency Shutdown (ESD) Testing
16" Receiver A (PIG)
Recip Comp - 01 (Gas Engine) (CBD)
n-Hexane
Start/Stop/Maintenance (SSM - CBD/ESD/PIG) Emissions
Total HAP
Ethylbenzene
20% VOC and GHG
Attachment U - Emission Estimates - Page 09 of 19Application for G35-D General Permit Registration
Xylenes
Toluene
TOTAL Gas
Worst Case
lb/MMscf lb/MMBtu lb/hr tpy
NOX 132 0.10 --- 1.50
CO 416 0.31 --- 4.74
NMNEHCVOC 0.10 7.54E-05 --- 1E-03
PM10/2.5 10.00 7.45E-03 --- 0.11
SO2 0.79 5.88E-04 --- 0.01
Acetaldehyde --- --- --- ---
Acrolein --- --- --- ---
BenzeneButadiene, 1,3- --- --- --- ---
Ethylbenzene3.49 MMBtu/hr (HHV) (Ave) Formaldehyde 0.10 7.35E-05 --- 1E-03
98.0% Net Control Efficiency n-HexaneMethanol
POM/PAH 9.2E-04 6.85E-07 --- 1E-05
Toluene1,343 Btu/scf (HHV) TMP, 2,2,4-
Xylenes8,760 hr/yr (intermittent) Other/Trace HAP 1.6E-03 1.18E-06 --- 2E-05
Total HAP 0.10 7.54E-05 --- 1E-03
2,599 scf/hr (Ave) CO2 (GWP=1) 157,058 117 --- 1,788
62 Mscf/dy CH4 (GWP=25)22.77 MMscf/yr N2O (GWP=298) 0.30 2.20E-04 --- 3E-03
CO2e 157,146 117 --- 1,789
Notes: 1 - The average Heat Input to the SSM Flare was determined as follows:
scf/hr (ave) Btu/scf (HHV) MMBtu/hr (ave)
649.79 1,343 0.87649.79 1,343 0.87649.79 1,343 0.87649.79 1,343 0.870.27 1,343 4E-040.27 1,343 4E-04110 1,343 0.15
93.26 1,343 0.13850 1,343 1.14
20% Contingency 520 1,343 0.702,599 1,343 3.49
2 - Reference: Worst-Case Wet Gas Analysis, Vendor Data, and Engineering Judgment.
Zeeco MJ-16 Sonic Flare
3 - The SSM Flare only operates during compressor blowdown (CBD), emergency shutdown (ESD), and pigging operations (PIG).
Threedubs Compressor Station (3WCS)Attachment U - Emission Estimates - Page 10 of 19
SSM Flare (FLR) EmissionsApplication for G35-D General Permit Registration
Total Gas to the SSM Flare:
Emergency Shutdown (ESD) TestingRotary Comp - 06 (Electric Motor) (CBD)
Pigging
Waste/Pilot Gas Stream
Recip Comp - 05 (Electric Motor) (CBD)
Recip Comp - 01 (Gas Engine) (CBD)
Purge, Fuel, and Pilot Gas
Recip Comp - 02 (Gas Engine) (CBD)Recip Comp - 03 (Gas Engine) (CBD)Recip Comp - 04 (Gas Engine) (CBD)
See SSM (CBD, ESD, PIG)
40CFR98 - Table A-1
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)40CFR98 - Table C-2
See SSM (CBD, ESD, PIG)40CFR98 - Table C-1
EPA AP-42 Table 1.4-3SUM
Zeeco MJ-16 Sonic Flare
(Combustion Only)
Controls SSM
(CBD, ESD, PIG)
EPA AP-42 Table 1.4-4
See SSM (CBD, ESD, PIG)
Site Rating See SSM (CBD, ESD, PIG)EPA AP-42 Table 1.4-3
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)
EPA AP-42 Table 1.4-3
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)See SSM (CBD, ESD, PIG)See SSM (CBD, ESD, PIG)
EPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3
See SSM (CBD, ESD, PIG)
See SSM (CBD, ESD, PIG)Combustion Related HAPs
FLR (7E)
(Controls CBD, ESD, and PIG)
EPA AP-42 Table 1.4-1EPA AP-42 Table 13.5-1
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
SSM Flare (FLR) Emissions
Source
IDDescription Reference Pollutant
Emission
Factor Emissions
See SSM (CBD, ESD, PIG)See SSM (CBD, ESD, PIG)
g/bhp-hr lb/MMBtu lb/hr tpy g/bhp-hr lb/hr tpy
Vendor Data x 2 NOX 0.27 3.51E-02 1.04 4.55 --- 0.27 1.04 4.55
Vendor Data x 2 CO 0.74 9.64E-02 2.86 12.51 --- 0.74 2.86 12.51
Vendor Data x 2 NMNEHC 6.76E-02 8.77E-03 0.26 1.14 --- 0.07 0.26 1.14
SUM VOC (w/Aldehydes)* 7.34E-02 9.52E-03 0.28 1.23 --- 0.07 0.28 1.23
AP-42 Table 3.1-2a PM10/2.5 5.11E-02 6.63E-03 0.20 0.86 --- 0.05 0.20 0.86
AP-42 Table 3.1-2a SO2 2.62E-02 3.40E-03 0.10 0.44 --- 0.03 0.10 0.44
AP-42 Table 3.1-3 *Acetaldehyde 3.08E-04 4.00E-05 1E-03 0.01 --- 3E-04 1E-03 0.01
AP-42 Table 3.1-3 *Acrolein 4.94E-05 6.40E-06 2E-04 8E-04 --- 5E-05 2E-04 8E-04
AP-42 Table 3.1-3 Benzene 9.25E-05 1.20E-05 4E-04 2E-03 --- 9E-05 4E-04 2E-03
1,742 bhp AP-42 Table 3.1-3 Butadiene, 1,3- 3.32E-06 4.30E-07 1E-05 6E-05 --- 3E-06 1E-05 6E-05
8,760 hr/yr AP-42 Table 3.1-3 Ethylbenzene 2.47E-04 3.20E-05 9E-04 4E-03 --- 2E-04 9E-04 4E-03
AP-42 Table 3.1-3 *Formaldehyde 5.48E-03 7.10E-04 0.02 0.09 --- 0.01 0.02 0.09
535 Exhaust Temp (oF) AP-42 Table 3.1-3 n-Hexane --- --- --- --- --- --- --- ---
AP-42 Table 3.1-3 Methanol --- --- --- --- --- --- --- ---
AP-42 Table 3.1-3 POM/PAH 2.51E-04 3.25E-05 1E-03 4E-03 --- 3E-04 1E-03 4E-03
AP-42 Table 3.1-3 Toluene 1.00E-03 1.30E-04 4E-03 0.02 --- 1E-03 4E-03 0.02
AP-42 Table 3.1-3 TMP, 2,2,4- --- --- --- --- --- --- --- ---
17,002 Btu/bhp-hr (HHV) AP-42 Table 3.1-3 Xylenes 4.94E-04 6.40E-05 2E-03 8E-03 --- 5E-04 2E-03 0.01
29.62 MMBtu/hr (HHV) AP-42 Table 3.1-3 Other/Trace HAP 2.24E-04 2.90E-05 9E-04 4E-03 --- 2E-04 9E-04 4E-03
29,037 scf/hr Sum Total HAP 8.15E-03 1.06E-03 0.03 0.14 --- 0.01 0.03 0.14
254.36 MMscf/yr 40CFR98 - Table C1 CO2 (GWP=1) 848.32 1.10E+02 3,258 14,270 --- 848 3,258 14,270
40CFR98 - Table C2 CH4 (GWP=25) 6.66E-02 8.64E-03 0.26 1.12 --- 0.07 0.26 1.12
1,020 Btu/scf (HHV) 40CFR98 - Table C2 N2O (GWP=298) 2.31E-02 3.00E-03 0.09 0.39 --- 0.02 0.09 0.39
Weighted Sum CO2e 857 111 3,291 14,414 --- 857 3,291 14,414
* = Aldehyde/MeOH added to NMNEHC to get VOCNotes: 1 - The emissions estimates are based on operation at 100% of rated load for 8,760 hr/yr. Actual load and operating hours will be less.
3 - PM10/2.5 is filterable and condensable particulate matter; including PM10 and PM2.54 - The fuel heating value will vary, 1,020 Btu/scf (HHV) is at the low end of the range and results in a high (conservative) fuel consumption estimate.
Appalachia Midstream Services, LLC (AMS)
Source
ID
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Microturbine Generator (GT) Emissions
Pollutant
Pre-Controlled
EmissionsControl
Efficiency
Controlled
Emissions
2 - A footnote to AP-42 Table 3.4-1 indicates that "THC is based on EPA Test Method 25A" and "VOC = THC - Methane". However, EPA Method 25A does NOT measure aldehydes (or methanol). Accordingly, and to be conservative, total VOC is estimated by NMNEHC + aldehydes.
5 - The turbine’s operating load has a considerable effect on the resulting emission levels. At reduced loads (lower than 80 percent) the NOx, CO, and THC (NMNEHC, VOC, HAP, and CH4) emissions are expected to be higher. A manufacturer with similar equipment (Capstone) states that "fuel flows can be up to two times higher than steady state values." Accordingly, and to be conservative, the vendor, AP-42, and 40CFR98 [full load, steady-state] emission factor data are increased by a factor of two (2).
Description Reference
Microturbine Generator (GT) EmissionsAttachment U - Emission Estimates - Page 11 of 19
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
GT (8E)
Non-EmergencyMicroturbine Generator
FlexEnergy GT-1300S(1300 kWe)
(4 x 325 kWe Units)
Fuel flows shown are 2X higher
than steady state values
VOC/CH4: 20% Margin
HAP: 100% Margin
lb/hr tpy lb/hr tpy % lb/hr tpy
VOC 46.49 203.61 55.78 244 1.12 4.89
Benzene 0.01 0.05 0.02 0.09 4E-04 2E-03
Flow Rate Ethylbenzene 0.01 0.05 0.02 0.10 5E-04 2E-03
200 n-Hexane 0.56 2.46 1.12 4.91 0.02 0.10
MMscfd Toluene 0.03 0.13 0.06 0.26 1E-03 0.01
2,2,4-TMP 0.01 0.05 0.02 0.09 4E-04 2E-03
Xylenes 0.01 0.06 0.03 0.12 5E-04 2E-03
8,760 Tot HAP 0.64 2.79 1.27 5.58 0.03 0.11
CO2 1.18 5.17 1.42 6.20 --- 1.42 6.20
hr/yr CH4 33.18 145 39.82 174 98.0% 0.80 3.49
CO2e 830.80 3,639 997 4,367 97.9% 21.33 93.41
VOC 61.45 269.15 73.74 322.98 1.47 6.46
Benzene 0.93 4.09 1.87 8.18 0.04 0.16
Flow Rate Ethylbenzene 3.02 13.22 6.04 26.44 0.12 0.53
200 n-Hexane 1.55 6.81 3.11 13.61 0.06 0.27
MMscfd Toluene 4.20 18.41 8.41 36.83 0.17 0.74
2,2,4-TMP 0.03 0.13 0.06 0.27 1E-03 0.01
Xylenes 5.18 22.67 10.35 45.35 0.21 0.91
8,760 Tot HAP 14.92 65.34 29.84 130.68 0.60 2.61
CO2 0.89 3.91 1.07 4.69 --- 1.07 4.69
hr/yr CH4 1.86 8.16 2.24 9.79 98.0% 0.04 0.20
CO2e 46.58 208 56.97 250 96.2% 2.19 9.59
VOC 107.94 473 130 567 2.59 11.35
Benzene 0.94 4.14 1.89 8.27 0.04 0.17
Flow Rate Ethylbenzene 3.03 13.27 6.06 26.54 0.12 0.53
200 n-Hexane 2.12 9.26 4.23 18.53 0.08 0.37
MMscfd Toluene 4.23 18.54 8.47 37.09 0.17 0.74
2,2,4-TMP 0.04 0.18 0.08 0.36 2E-03 0.01
Xylenes --- --- 10.38 45.47 0.21 0.91
8,760 Tot HAP 15.55 68.13 31.11 136 0.62 2.73
CO2 2.07 9.08 2.49 10.89 --- 2.49 10.89
hr/yr CH4 35.05 154 42.06 184 98.0% 0.84 3.68
CO2e 877.38 3,847 1,054 4,616 97.8% 23.52 103.00
Notes: 1 - Used GRI-GLYCalc V4.0 to calculate Flash Tank and Regenerator/Still Vent emissions.2 - GRI-GLYCalc 4.0 Model Results are based on the following input:
80 oF and 1,000 psig, H2O Saturated Electric/Pneumatic Pump (Primary), Gas-Assist (Backup)See Supplement S1 - Wet Gas Summary 110 oF, 60 psig, 98% Combustion200.0 MMscfd, 7.0 lb-H2O/MMscf None1.5 wt% H2O, 24.0 gpm (Primary), 7.5 gpm (Backup) Regen Control: 98% Combustion
3 - Total HAP includes n-hexane, benzene, toluene, ethylbenzene, xylene, and other components.4 - A contingency has been added to the GRI-GLYCalc model results to account for potential future changes in gas composition.
98.0%
98.0%
98.0%
GRI-GLYCalc 4.0
Application for G35-D General Permit Registration
GRI-GLYCalc 4.0
40CFR98 - Table A-1
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
Dehydrator Still Vent (DSV)
Still Vent Off-Gas Controlled by 98% T-Ox
(TOx)
GRI-GLYCalc 4.0GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0GRI-GLYCalc 4.0GRI-GLYCalc 4.0GRI-GLYCalc 4.0
Threedubs Compressor Station (3WCS)
DHY Dehydrator (Total)
GRI-GLYCalc 4.0
Attachment U - Emission Estimates - Page 12 of 19Dehydrator (DFT and DSV) Emissions
Lean Glycol:
Glycol Pump:Wet Gas:
DFT (9E)
Flash Tank:Stripping Gas:
Wet Gas Analysis: Dry Gas:
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0GRI-GLYCalc 4.0GRI-GLYCalc 4.0
40CFR98 - Table A-1
GRI-GLYCalc 4.0
DSV (10E)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Dehydrator (DFT and DSV) Emissions
Net
Control
Efficiency
Controlled
Emissions
Worst-CaseGRI-GLYCalc
Pre-Controlled
EmissionsUnit ID Description Capacity Reference Pollutant
Dehydrator Flash Tank (DFT)
Flash Tank Off-Gas Controlled by 98% T-Ox
(TOx)
40CFR98 - Table A-1
GRI-GLYCalc 4.0GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
GRI-GLYCalc 4.0
lb/MMscf lb/MMBtu lb/hr tpy
NOX 1525 9.80E-02 0.20 0.86
CO 1281 8.24E-02 0.16 0.72
NMNEHC 83.9 5.39E-03 0.01 0.05
VOC 83.9 5.39E-03 0.01 0.05
PM10/2.5 115.9 7.45E-03 0.01 0.07
SO2 9.2 5.88E-04 1E-03 0.01
Acetaldehyde --- --- --- ---
Acrolein --- --- --- ---
2.0 MMBtu/hr (HHV) Benzene 3.20E-02 2.06E-06 4E-06 2E-05
Butadiene, 1,3- --- --- --- ---
Ethylbenzene --- --- --- ---
Formaldehyde 1.14E+00 7.35E-05 1E-04 6E-04
n-Hexane 27.45 1.76E-03 4E-03 0.02
Methanol --- --- --- ---
15,555 Btu/scf (HHV) POM/PAH 1.06E-02 6.85E-07 1E-06 6E-06
Toluene 5.19E-02 3.33E-06 7E-06 3E-05
TMP, 2,2,4- --- --- --- ---
8,760 hr/yr Xylenes --- --- --- ---
Other/Trace HAP 1.83E-02 1.18E-06 2E-06 1E-05
Total HAP 28.71 1.85E-03 4E-03 0.02
129 scf/hr CO2 (GWP=1) 1,819,582 117 234 1,025
1.13 MMscf/yr CH4 (GWP=25) 34.29 2.20E-03 4E-03 0.02
N2O (GWP=298) 3.43 2.20E-04 4E-04 2E-03
CO2e 1,821,461 117 234 1,026
Notes: 1 - The emissions shown are based on operation at 100% of rated load for 8,760 hr/yr. Actual load and operating hours will be less. 2 - The fuel heating value will vary, 1,020 Btu/scf (HHV) is at the low end of the range and results in a high (conservative) fuel consumption estimate.3 - PM10/2.5 is filterable and condensable particulate matter; including PM10 and PM2.5
Reboiler (RBV) EmissionsApplication for G35-D General Permit Registration
Attachment U - Emission Estimates - Page 13 of 19
EPA AP-42 Table 1.4-3
40CFR98 - Table A-1
EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3
SUM40CFR98 - Table C-140CFR98 - Table C-240CFR98 - Table C-2
4 - "Other/Trace HAPs" includes: CarbonTetrachloride, Chlorobenzene, Chloroform, Dichloropropene, 1,3-Dichloropropene, Ethylene Dibromide, Methylene Chloride, Phenol, Propylene Oxide, Styrene, 1,1,2,2-Tetrachloroethane, 1,1,2-Trichloroethane, and Vinyl Chloride (as per AP-42).
Threedubs Compressor Station (3WCS)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Reboiler (RBV) Emissions
EmissionsSource
IDDescription Reference Pollutant
Emission
Factor
RBV (11E)
Dehydrator Reboiler
EPA AP-42 Table 1.4-1EPA AP-42 Table 1.4-1EPA AP-42 Table 1.4-2
EPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3
EPA AP-42 Table 1.4-2
EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-4EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3
lb/MMscf lb/MMBtu lb/hr tpy
NOX 61 0.10 0.61 2.67
CO 193 0.31 1.93 8.43
NMNEHCVOC 4.69E-02 7.54E-05 5E-04 2E-03
PM10/2.5 4.63 7.45E-03 0.05 0.20
SO2 0.37 5.88E-04 4E-03 0.02
Acetaldehyde --- --- --- ---
Acrolein --- --- --- ---
BenzeneButadiene, 1,3- --- --- --- ---
Ethylbenzene6.21 MMBtu/hr (HHV) Formaldehyde 4.57E-02 7.35E-05 5E-04 2E-03
98.0% Net Control Efficiency n-HexaneMethanol
POM/PAH 4.26E-04 6.85E-07 4E-06 2E-05
Toluene622 Btu/scf (HHV) TMP, 2,2,4-
Xylenes8,760 hr/yr Other/Trace HAP 7.32E-04 1.18E-06 7E-06 3E-05
Total HAP 4.69E-02 7.54E-05 5E-04 2E-03
9,984 scf/hr CO2 (GWP=1) 72,759 117 726 3,182
240 Mscf/dy CH4 (GWP=25)87.46 MMscf/yr N2O (GWP=298) 0.14 2.20E-04 1E-03 0.01
CO2e 72,800 117 727 3,184
Notes:
2 - Heat Input to the Thermal Oxidizer was determined as follows:
scf/hr Btu/scf (HHV) MMBtu/hr
1,590 1,622 2.585,880 247 1.45850 1,343 1.14
20% Contingency 1,664 622 1.039,984 622 6.21
3 - Reference: GRI-GLYCalc Results, Worst-Case Gas Analysis, Vendor Data, and Engineering Judgment.
RSV - Regenerator/Still Vent Gas
1 - Dehydrator flash tank off-gases are generally burned as fuel in the reboiler. However, to be conservative, all flash tank off-gases are shown as being routed to the Thermal Oxidizer (T-Ox).
Purge, Fuel, and Pilot Gas
Total Gas to the Thermal Oxidizer:
Threedubs Compressor Station (3WCS)Thermal Oxidizer (TOx) Emissions
Application for G35-D General Permit RegistrationAttachment U - Emission Estimates - Page 14 of 19
See DHY (DFT and DSV)EPA AP-42 Table 1.4-3
SUM40CFR98 - Table C-1
DFT - Flash Tank Off-Gas
EPA AP-42 Table 1.4-4See DHY (DFT and DSV) See DHY (DFT and DSV)EPA AP-42 Table 1.4-3
See DHY (DFT and DSV) See DHY (DFT and DSV)
Waste/Pilot Gas Stream
See DHY (DFT and DSV) See DHY (DFT and DSV)
Site Rating
See DHY (DFT and DSV) See DHY (DFT and DSV)EPA AP-42 Table 1.4-3
See DHY (DFT and DSV) See DHY (DFT and DSV)
See DHY (DFT and DSV) See DHY (DFT and DSV)40CFR98 - Table C-240CFR98 - Table A-1
See DHY (DFT and DSV)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Thermal Oxidizer (TOx) Emissions
Source
IDDescription Reference Pollutant
Emission
Factor Emissions
See DHY (DFT and DSV)
TOx (12E)
(Controls Dehydrator
Still Vent andFlash Tank)
ZEECO Z-HTO Thermal Oxidizer
(Combustion Only)
EPA AP-42 Table 1.4-1EPA AP-42 Table 13.5-1See DHY (DFT and DSV) See DHY (DFT and DSV)
Controls DHY
(DFT and DSV)
Combustion Related HAPsEPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-2EPA AP-42 Table 1.4-3EPA AP-42 Table 1.4-3
See DHY (DFT and DSV)
--- VOC --- VOC
bbl bbl/yr lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
TK-01 (13E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-02 (14E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-03 (15E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-04 (16E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-05 (17E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-06 (18E) 400 95.0 38,000 0.139 0.021 0.01 0.06 --- --- --- --- --- ---TK-07 (19E) 400 37.5 15,000 0.007 0.001 3E-04 1E-03 --- --- --- --- --- ---TK-08 (20E) 400 37.5 15,000 0.007 0.001 3E-04 1E-03 --- --- --- --- --- ---
TOTAL: 3,200 80.6 258,000 TOTAL: 0.08 0.37 --- --- --- --- --- ---
PRE-Control: 4.19 18.36 --- --- --- --- --- ---
0.079% VOC 2.087% VOC 7.720% VOC 1.049% VOC 0.703% VOC 2.732% VOC 14.369% VOC
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
TK-01 (13E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-02 (14E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-03 (15E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-04 (16E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-05 (17E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-06 (18E) 1E-05 5E-05 3E-04 1E-03 1E-03 5E-03 --- --- 1E-04 6E-04 1E-04 4E-04 4E-04 2E-03 2E-03 0.01TK-07 (19E) 2E-07 9E-07 6E-06 3E-05 2E-05 9E-05 --- --- 3E-06 1E-05 2E-06 8E-06 7E-06 3E-05 4E-05 2E-04TK-08 (20E) 2E-07 9E-07 6E-06 3E-05 2E-05 9E-05 --- --- 3E-06 1E-05 2E-06 8E-06 7E-06 3E-05 4E-05 2E-04
TOTAL: 7E-05 3E-04 2E-03 8E-03 6E-03 0.03 --- --- 9E-04 4E-03 6E-04 3E-03 2E-03 0.01 0.01 0.05
PRE-Control: 3E-03 0.01 0.09 0.38 0.32 1.42 --- --- 0.04 0.19 0.03 0.13 0.11 0.50 0.60 2.64
Notes: 1 - Produced water storage tanks are heated to approximately 60 degrees Fahrenheit to prevent freezing.
20% VOC 100% HAP
%Total %VOC
--- lb/MMscf --- lb/MMscf --- --- --- lb/MMscf --- lb/MMscf --- ---
0.05 lb/MMscf 0.05 lb/MMscf 2E-05 2E-05268,162 lb/MMscf 321,795 lb/MMscf 100.00 100.00268,162 lb/MMscf 321,795 lb/MMscf 100.00 ---
127 lb/MMscf 253 lb/MMscf 0.08 0.083,357 lb/MMscf 6,714 lb/MMscf 2.09 2.09
12,422 lb/MMscf 24,843 lb/MMscf 7.72 7.721,687 lb/MMscf 3,375 lb/MMscf 1.05 1.051,132 lb/MMscf 2,264 lb/MMscf 0.70 0.704,395 lb/MMscf 8,790 lb/MMscf 2.73 2.73
23,120 lb/MMscf 46,239 lb/MMscf 14.37 14.37
98%
Toluene
Williams Ohio Valley Midstream LLC (OVM)
Stabilized Condensate
Unit ID Material StoredTurnovers
per Year
Stabilized Condensate
Capacity
Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Storage Tank (TK-01 thru TK-08) Emissions
Attachment U - Supporting Emissions Calculations
VRU
Control
Efficiency
ThroughputTANKS 4.0
(Breathing
Losses)
TANKS 4.0
(Working
Losses)
Xylenes (C8) Total HAP
Unit ID
Benzene Ethylbenzene n-Hexane (C6) Methanol
(MeOH)
Toluene (C7) 2,2,4-TMP
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration Attachment U - Supporting Emissions Calculations Page 15 of 19
Storage Tank (TK-01 thru TK-08) Emissions
XylenesTotal HAP
Produced Water
Stabilized CondensateProduced Water
Stabilized CondensateStabilized CondensateStabilized Condensate
CH4
CH4 GWP = 25VOC
CO2 CO2e
Ethylbenzene
2 - The results of a representative Condensate Analysis were used to determine the following worst-case components (See Appendix S1 - Condensate Summary):
Min. Contingency:
Pollutant Condensate Worst Case
CO2Methane (CH4)
N2/Water/Ethane/EtcVOC
TOTAL GasBenzene
2,2,4-TMP
n-Hexane
--- VOC --- VOC
sat. fac. psia lb/lb-mol oR % lb/Mgal Mgal/yr lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
Stabilized Condensate 0.60 5.30 60.30 510 1.57 9,576 --- 7.51 --- --- --- --- --- ---Produced Water 0.60 1.50 30.00 510 0.22 1,260 --- 0.14 --- --- --- --- --- ---
TOTAL: 10,836 --- 7.65 --- --- --- --- --- ---
--- 22.85 --- --- --- --- --- ---
0.079% VOC 2.087% VOC 7.720% VOC 1.049% VOC 0.703% VOC 2.732% VOC 14.369% VOC
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
--- 6E-03 --- 0.16 --- 0.58 --- --- --- 0.08 --- 0.05 --- 0.21 --- 1.08 --- 1E-04 --- 3E-03 --- 0.01 --- --- --- 1E-03 --- 1E-03 --- 4E-03 --- 0.02
TOTAL: --- 6E-03 --- 0.16 --- 0.59 --- --- --- 0.08 --- 0.05 --- 0.21 --- 1.10
PRE-Control: --- 0.02 --- 0.48 --- 1.76 --- --- --- 0.24 --- 0.16 --- 0.62 --- 3.28Notes: 1 - Emission factors and formulas are from AP-42 Section 5.2 "Transportation and Marketing of Petroleum Liquids":
LL = 12.46 x S x P x M / T x (1 - CE)
where: LL = loading loss, lb/1000 gal of liquid loaded M = molecular weight of vapors, lb/lb-mol. S = saturation factor, use 0.60 for submerged fill. T = temperature of bulk liquid loaded, °R = °F + 460P = true vapor pressure of liquid loaded, psia. CE = overall emission reduction efficiency (70% collection efficiency x 95% VRU).
2 - Produced water vapor pressure, molecular weight, and temperature are based on operator experience and sampling data at similar locations.3 - It is assumed each tanker truck holds 7,000 gallons and can be loaded in one hour: 1,548 hr/yr 4.2 hr/dy(Ave)
20% VOC 100% HAP
%Total %VOC
--- lb/MMscf --- lb/MMscf --- --- --- lb/MMscf --- lb/MMscf --- --- --- lb/MMscf --- lb/MMscf --- ---
268,162 lb/MMscf 321,795 lb/MMscf 100.000 100.000268,162 lb/MMscf 321,795 lb/MMscf 100.000 ---126.59 lb/MMscf 253 lb/MMscf 0.079 0.079
3,357.16 lb/MMscf 6,714 lb/MMscf 2.087 2.08712,422 lb/MMscf 24,843 lb/MMscf 7.720 7.720
1,687.46 lb/MMscf 3,375 lb/MMscf 1.049 1.0491,131.80 lb/MMscf 2,264 lb/MMscf 0.703 0.703
4,395 lb/MMscf 8,790 lb/MMscf 2.732 2.73223,120 lb/MMscf 46,239 lb/MMscf 14.369 14.369
Xylenes (C8) Total HAP
66.5%
Methanol
(MeOH)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Stabilized Condensate and Produced Water (TLO) Truck Load-Out Emissions
Source
IDDescription
S P M TCE
(VRU)LL
CH4CO2 CO2e
CH4 GWP = 25
PRE-Control:
100.00%T-Put
VOC
Threedubs Compressor Station (3WCS) Application for G35-D General Permit RegistrationAttachment U - Emission Estimates - Page 16 of 19
Methane (CH4)N2/Water/Ethane/Etc
n-Hexane
VOC
Stabilized Condensate and Produced Water (TLO) Truck Load-Out Emissions
Total HAP
Toluene (C7) 2,2,4-TMP
TOTAL GasBenzene
Ethylbenzene
Benzene Ethylbenzene n-Hexane (C6)
4 - The results of a representative Condensate Analysis were used to determine the following worst-case components (See Appendix S1 - Condensate Summary):
Pollutant Condensate Worst Case
CO2
Min. Contingency:
TLO (21E)
TLO (21E)
Toluene2,2,4-TMP
Xylenes
Source
ID
26.16 Wgt% 0.86% VOC 204% VOC
120% lb/hr/Unit lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
960 1,152 9.92E-03 92% 0.91 4.00 0.24 1.05 2E-03 0.01 0.49 2.14 12.20 53 --- --- --- --- --- --- --- --- --- --- --- --- --- ---72 86 1.94E-02 --- 1.68 7.34 0.44 1.92 4E-03 0.02 0.89 3.92 22.36 97.93
3,132 3,758 4.41E-04 93% 0.12 0.51 0.03 0.13 3E-04 1E-03 0.06 0.27 1.55 6.78783 940 8.60E-04 --- 0.81 3.54 0.21 0.93 2E-03 0.01 0.43 1.89 10.78 47.2034 41 4.41E-03 --- 0.18 0.79 0.05 0.21 4E-04 2E-03 0.10 0.42 2.40 10.51
TOTAL: 4,981 5,977 TOTAL: 0.97 4.23 TOTAL: 0.01 0.04 1.97 8.63 49.27 216
PRE Control: 4.12 18.04 0.01 0.04 8.40 36.80 210 920
0.140% VOC 0.140% VOC 1.68% VOC 0.140% VOC 0.140% VOC 0.140% VOC 2.386% VOC
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
1E-03 1E-03 1E-03 1E-03 0.02 0.02 --- --- 1E-03 1E-03 1E-03 1E-03 1E-03 1E-03 0.02 0.02 --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- ---
3E-03 3E-03 3E-03 3E-03 3E-02 0.03 --- --- 3E-03 3E-03 3E-03 3E-03 3E-03 3E-03 5E-02 0.052E-04 2E-04 2E-04 2E-04 2E-03 2E-03 --- --- 2E-04 2E-04 2E-04 2E-04 2E-04 2E-04 3E-03 3E-031E-03 1E-03 1E-03 1E-03 0.02 0.02 --- --- 1E-03 1E-03 1E-03 1E-03 1E-03 1E-03 0.02 0.023E-04 3E-04 3E-04 3E-04 3E-03 3E-03 --- --- 3E-04 3E-04 3E-04 3E-04 3E-04 3E-04 5E-03 5E-03
TOTAL: 0.01 0.01 0.01 0.01 0.07 0.07 --- --- 0.01 0.01 0.01 0.01 0.01 0.01 0.10 0.10
PRE Control: 0.03 0.03 0.03 0.03 0.30 0.30 --- --- 0.03 0.03 0.03 0.03 0.03 0.03 0.43 0.43
Notes: 1 - Assumed 8,760 hours per year of fugitive emissions.
%Total %VOC
127 lb/MMscf 153 lb/MMscf 0.224 0.858kg/hr lb/hr/unit kg/hr lb/hr/unit kg/hr lb/hr/unit 30,275 lb/MMscf 36,331 lb/MMscf 53.343 203.929
Valves 4.5E-03 9.92E-03 2.5E-03 5.51E-03 9.8E-05 2.16E-04 13,808 lb/MMscf 13,808 lb/MMscf 20.274 77.508Pump Seals --- --- 1.3E-02 2.87E-02 2.4E-05 5.29E-05 14,846 lb/MMscf 17,815 lb/MMscf 26.158 100.000Others 8.8E-03 1.94E-02 7.5E-03 1.65E-02 1.4E-02 3.09E-02 59,057 lb/MMscf 68,107 lb/MMscf 100.000 ---Connectors 2.0E-04 4.41E-04 2.1E-04 4.63E-04 1.1E-04 2.43E-04 1.60 lb/MMscf 25.00 lb/MMscf 0.037 0.140Flanges 3.9E-04 8.60E-04 1.1E-04 2.43E-04 2.9E-06 6.39E-06 3.71 lb/MMscf 25.00 lb/MMscf 0.037 0.140Open-Ended Lines 2.0E-03 4.41E-03 1.4E-03 3.09E-03 2.5E-04 5.51E-04 181 lb/MMscf 300 lb/MMscf 0.440 1.684
5.80 lb/MMscf 25.00 lb/MMscf 0.037 0.1403 - "Other” components include pressure relief devices (PRD), compressors, diaphragms, drains, meters, etc. 5.51 lb/MMscf 25.00 lb/MMscf 0.037 0.140
4 lb/MMscf 25.00 lb/MMscf 0.037 0.140202 lb/MMscf 425 lb/MMscf 0.624 2.386
20% VOC
FUG-G(1F)
Threedubs Compressor Station (3WCS)
2 - Gas/Vapor emissions calculated using EPA Protocol for Equipment Leak Emission Estimates, EPA-453/R-95-017, Nov 1995; Table 2-4, Oil and Gas Production Operations:
GasEquipment Type
Water/Oil
4 - The results of a representative Wet Gas Analysis were used to determine the following worst-case components (See Appendix S1 - Wet Gas Summary):
Min. Contingency:
Pollutant Wet Gas Worst Case
CO2Methane (CH4)
N2/Water/Ethane/EtcVOC
Process Piping and Equipment Leak – Gas (FUG-G) EmissionAttachment U - Emission Estimates - Page 17 of 19
Application for G35-D General Permit Registration
Light Liquid
Process Piping and Equipment Leaks
(Gas)
ValvesPump Seals
OtherConnectors
FlangesOpen-ended Lines
n-Hexane (C6)Ethylbenzene Total HAPMethanol
(MeOH)
2,2,4-TMPToluene (C7) Xylenes (C8)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Process Piping and Equipment Leak – Gas (FUG-G) Emission
Source
IDDescription
LDAR
Control
Credit
Controlled
Leaks
VOC
CH4 GWP = 25
CH4CO2 CO2eUnit
Count
Cons'tive
Multiplier
Component
(Unit) Type
(Gas)
Leak
Factor
FUG-G(1F)
Source
IDDescription
Process Piping and Equipment Leaks
(Gas)
(Gas)
Valves
Open-ended Lines
Component
(Unit) Type
Flanges
Pump SealsOther
Connectors
Benzene
TOTAL Gas
XylenesTotal HAP
BenzeneEthylbenzene
n-HexaneToluene
2,2,4-TMP
100.00 Wgt% --- VOC --- VOC
120% lb/hr/Unit lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
576 691 5.51E-03 88% 0.46 2.00 0.46 2.00 --- --- --- --- --- ---12 14 2.87E-02 75% 0.10 0.45 0.10 0.45 --- --- --- --- --- ---43 52 1.65E-02 --- 0.85 3.74 0.85 3.74 --- --- --- --- --- ---
1,296 1,555 4.63E-04 93% 0.05 0.22 0.05 0.22 --- --- --- --- --- ---324 389 2.43E-04 --- 0.09 0.41 0.09 0.41 --- --- --- --- --- ---20 24 3.09E-03 --- 0.07 0.32 0.07 0.32 --- --- --- --- --- ---
TOTAL: 2,271 2,725 TOTAL: 1.63 7.15 TOTAL: --- --- --- --- --- ---
PRE Control: 5.96 26.12 --- --- --- --- --- ---
0.079% VOC 2.09% VOC 7.72% VOC 1.05% VOC 0.70% VOC 2.73% VOC 14.37% VOC
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
4E-04 2E-03 0.01 0.04 0.04 0.15 --- --- 5E-03 0.02 3E-03 0.01 0.01 0.05 0.07 0.298E-05 4E-04 2E-03 0.01 0.01 0.03 --- --- 1E-03 5E-03 7E-04 3E-03 3E-03 0.01 0.01 0.067E-04 3E-03 0.02 0.08 0.07 0.29 --- --- 0.01 0.04 6E-03 0.03 0.02 0.10 0.12 0.544E-05 2E-04 1E-03 5E-03 4E-03 0.02 --- --- 5E-04 2E-03 4E-04 2E-03 1E-03 6E-03 0.01 0.037E-05 3E-04 2E-03 0.01 0.01 0.03 --- --- 1E-03 4E-03 7E-04 3E-03 3E-03 0.01 0.01 0.066E-05 3E-04 2E-03 0.01 6E-03 0.03 --- --- 8E-04 3E-03 5E-04 2E-03 2E-03 0.01 0.01 0.05
TOTAL: 1E-03 6E-03 0.03 0.15 0.13 0.55 --- --- 0.02 0.07 0.01 0.05 0.04 0.20 0.23 1.03
PRE Control: 5E-03 0.02 0.12 0.55 0.46 2.02 --- --- 0.06 0.27 0.04 0.18 0.16 0.71 0.86 3.75
Notes: 1 - Assumed 8,760 hours per year of fugitive emissions.
20% VOC 100% HAP
%Total %VOC
--- lb/MMscf --- lb/MMscf --- ---kg/hr lb/hr/unit kg/hr lb/hr/unit kg/hr lb/hr/unit --- lb/MMscf --- lb/MMscf --- ---
Valves 4.5E-03 9.92E-03 2.5E-03 5.51E-03 9.8E-05 2.16E-04 --- lb/MMscf --- lb/MMscf --- ---Pump Seals --- --- 1.3E-02 2.87E-02 2.4E-05 5.29E-05 268,162 lb/MMscf 321,795 lb/MMscf 100.000 100.000Others 8.8E-03 1.94E-02 7.5E-03 1.65E-02 1.4E-02 3.09E-02 268,162 lb/MMscf 321,795 lb/MMscf 100.000 ---Connectors 2.0E-04 4.41E-04 2.1E-04 4.63E-04 1.1E-04 2.43E-04 126.59 lb/MMscf 253.18 lb/MMscf 0.079 0.079Flanges 3.9E-04 8.60E-04 1.1E-04 2.43E-04 2.9E-06 6.39E-06 3,357.16 lb/MMscf 6,714.31 lb/MMscf 2.087 2.087Open-Ended Lines 2.0E-03 4.41E-03 1.4E-03 3.09E-03 2.5E-04 5.51E-04 12,422 lb/MMscf 24,843 lb/MMscf 7.720 7.720
1,687.46 lb/MMscf 3,374.93 lb/MMscf 1.049 1.0493 - "Other” components include pressure relief devices (PRD), diaphragms, drains, meters, etc. 1,131.80 lb/MMscf 2,263.61 lb/MMscf 0.703 0.703
4,395 lb/MMscf 8,790.15 lb/MMscf 2.732 2.73223,120 lb/MMscf 46,239 lb/MMscf 14.369 14.369
0 0
CO2e
CH4 GWP = 25
Methanol
(MeOH)
Benzene
2 - Light Liquid emissions calculated using EPA Protocol for Equipment Leak Emission Estimates, EPA-453/R-95-017, Nov 1995; Table 2-4, Oil and Gas Production Operations:
Total HAPEthylbenzene n-Hexane (C6) Toluene (C7) 2,2,4-TMP Xylenes (C8)
Valves
4 - The results of a representative Condensate Analysis were used to determine the following worst-case components (See Appendix S1 - Condensate Summary):
Pollutant Condensate Worst Case
Application for G35-D General Permit Registration
Pump SealsOther
ConnectorsFlanges
Open-ended Lines
Equipment TypeGas
Threedubs Compressor Station (3WCS)Process Piping and Equipment Leaks – Light Liquid (FUG-L) Emission
Attachment U - Emission Estimates - Page 18 of 19
Light Liquid Water/Oil
FUG-L(2F)
Process Piping and Equipment Leaks
(Light Liquid)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Process Piping and Equipment Leaks – Light Liquid (FUG-L) Emission
Source
IDDescription
(Light Liquid)
Component
(Unit) Type
Leak
FactorLDAR
Control
Credit
Controlled
LeaksUnit
Count
Cons'tive
Multiplier
VOC CH4CO2
FUG-L(2F)
Source
IDDescription
Component
(Unit) Type
(Light Liquid)
Process Piping and Equipment Leaks
(Light Liquid)
ValvesPump Seals
OtherConnectors
FlangesOpen-ended Lines
XylenesTotal HAP
Min. Contingency:
BenzeneEthylbenzene
n-HexaneToluene
2,2,4-TMP
CO2Methane (CH4)
N2/Water/Ethane/EtcVOC
TOTAL Condenate
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
5,000 bhp 8,760 hr/yr 0.01 0.05 0.09 0.38 0.03 0.15 1E-03 4E-03 6E-05 3E-04 13.00 56.96 0.05 0.24 2E-05 1E-04 14.38 63.005,000 bhp 8,760 hr/yr 0.01 0.05 0.09 0.38 0.03 0.15 1E-03 4E-03 6E-05 3E-04 13.00 56.96 0.05 0.24 2E-05 1E-04 14.38 63.005,000 bhp 8,760 hr/yr 0.01 0.05 0.09 0.38 0.03 0.15 1E-03 4E-03 6E-05 3E-04 13.00 56.96 0.05 0.24 2E-05 1E-04 14.38 63.005,000 bhp 8,760 hr/yr 0.01 0.05 0.09 0.38 0.03 0.15 1E-03 4E-03 6E-05 3E-04 13.00 56.96 0.05 0.24 2E-05 1E-04 14.38 63.00
TOT: 0.05 0.21 0.34 1.51 0.14 0.59 4E-03 2E-02 2E-04 1E-03 TOT: 52.02 228 0.22 0.96 9E-05 4E-04 57.54 252
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
CE-01 8E-04 4E-03 5E-04 2E-03 4E-05 2E-04 3E-05 1E-04 4E-06 2E-05 4E-03 0.02 1E-04 5E-04 2E-04 1E-03 3E-05 2E-04 4E-05 2E-04 3E-05 1E-04 2E-05 8E-05 3E-05 1E-04 0.01 0.03CE-02 8E-04 4E-03 5E-04 2E-03 4E-05 2E-04 3E-05 1E-04 4E-06 2E-05 4E-03 0.02 1E-04 5E-04 2E-04 1E-03 3E-05 2E-04 4E-05 2E-04 3E-05 1E-04 2E-05 8E-05 3E-05 1E-04 0.01 0.03CE-03 8E-04 4E-03 5E-04 2E-03 4E-05 2E-04 3E-05 1E-04 4E-06 2E-05 4E-03 0.02 1E-04 5E-04 2E-04 1E-03 3E-05 2E-04 4E-05 2E-04 3E-05 1E-04 2E-05 8E-05 3E-05 1E-04 0.01 0.03CE-04 8E-04 4E-03 5E-04 2E-03 4E-05 2E-04 3E-05 1E-04 4E-06 2E-05 4E-03 0.02 1E-04 5E-04 2E-04 1E-03 3E-05 2E-04 4E-05 2E-04 3E-05 1E-04 2E-05 8E-05 3E-05 1E-04 0.01 0.03
TOTAL: 3E-03 0.01 2E-03 0.01 2E-04 8E-04 1E-04 5E-04 2E-05 7E-05 0.02 0.07 4E-04 2E-03 1E-03 4E-03 1E-04 6E-04 2E-04 7E-04 1E-04 5E-04 7E-05 3E-04 1E-04 6E-04 0.02 0.11
2 - Blowby emission rates converted from "actual" cubic feet to "standard" cubic feet: scf = acf * [(P+14.6959)/14.6959] * [527.67/(T+459.67)]
3 - Engine Exhaust Flow Rates converted from "actual" cubic feet per minute to "standard" cubic feet per minute: scf = acf * [(P+14.6959)/14.6959] * [527.67/(T+459.67)]
CE-03 18.15
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
20,000 bhp
2.270.010.010.010.02
1 - As per Caterpillar's Application & Installation Guide - Crankcase Ventilation Systems: "[B]low-by on a new engine is approx. 0.5 ft3 /bhp-hr and design for a worn engine should be 1.0 ft3 /bhp-hr." http://s7d2.scene7.com/is/content/Caterpillar/CM20160713-53120-62603
1.54
lb/hrlb/hrlb/hr lb/hrlb/hrlb/hr
0.010.01 2.910.02
Actual to Standard Conversions
(@ 814 oF vs. 68 oF (Ignore Δ psi):
Engine Crankcase (ECC) EmissionsAttachment U - Emission Estimates - Page 19 of 19
Acetaldehyde
12,964acfm = scfm31,291
lb/MMscflb/MMscflb/MMscflb/MMscflb/MMscf
scf0.41
Total HAPsOther/TraceXylenesTMP, 2,2,4-TolueneMethanol
0.01
acf =1.0
0.02
Notes:
lb/MMscf
0.250.40
0.31
lb/hr lb/hrSource
ID
Acrolein
0.02
n-HexaneHCHO
lb/hrlb/hr
lb/MMscflb/MMscf lb/MMscflb/MMscf
0.0126.50
CO SO2 CH4
lb/MMscf
6,278
lb/MMscf
lb/hr lb/hrlb/hr
lb/MMscf lb/MMscf lb/MMscf
lb/hr
4.41 32.30 12.72 0.02
lb/hr
lb/MMscf lb/MMscf
NOx
Operations
lb/MMscf
lb/MMscf
lb/hr lb/hr lb/hr lb/hr
0.02
lb/hr
35,040 hr/yr
0.020.120.05
18.15
18.15
Butadiene
18.15
VOCCAT G3616 A4
Emission
Rates lb/hr
scf/bhp-hr
N2O
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Engine Crankcase (ECC) Emissions
Application for G35-D General Permit Registration
CO2e
41.52 16.36 0.03
CO2
0.41
PM
0.485.67 6,944Site Rating
MMscf/yr
lb/MMscf
5,401
lb/hr
4,883 20.61 0.01
lb/hr
0.37
CE-04
CE-02CE-01
Source
ID
TOTAL:
ECC(3F)
Unit
ID
Actual to Standard Conversions
(@ 814 oF vs. 68 oF (Ignore Δ psi):
Benzene
2E-03 1.98
0.010.090.04
72.58
lb/MMscflb/MMscflb/MMscf
0.01
Ethylbenzene POM/PAH
1E-030.19
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Attachment V
Facility-wide Emission Summary Sheet(s)
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
CE-01 4.41 19.31 2.58 11.32 2.07 9.05 0.02 0.10 0.37 1.63 0.37 1.63 5,401 23,656
CE-02 4.41 19.31 2.58 11.32 2.07 9.05 0.02 0.10 0.37 1.63 0.37 1.63 5,401 23,656
CE-03 4.41 19.31 2.58 11.32 2.07 9.05 0.02 0.10 0.37 1.63 0.37 1.63 5,401 23,656
CE-04 4.41 19.31 2.58 11.32 2.07 9.05 0.02 0.10 0.37 1.63 0.37 1.63 5,401 23,656
CRP --- --- --- --- 6.88 30.15 --- --- --- --- --- --- 351 1,537
SSM-CBD --- --- --- --- --- 4.06 --- --- --- --- --- --- --- 207
SSM-ESD --- --- --- --- --- 0.17 --- --- --- --- --- --- --- 8.78
SSM-PIG --- --- --- --- --- 0.15 --- --- --- --- --- --- --- 7.42
FLR --- 1.50 --- 4.74 --- 1E-03 --- 0.01 --- 0.11 --- 0.11 --- 1,789
GT 1.04 4.55 2.86 12.51 0.28 1.23 0.10 0.44 0.20 0.86 0.20 0.86 3,291 14,414
DFT --- --- --- --- 1.12 4.89 --- --- --- --- --- --- 21.33 93.41
DSV --- --- --- --- 1.47 6.46 --- --- --- --- --- --- 2.19 9.59
RBV 0.20 0.86 0.16 0.72 0.01 0.05 1E-03 0.01 0.01 0.07 0.01 0.07 234 1,026
TOx 0.61 2.67 1.93 8.43 5E-04 2E-03 4E-03 0.02 0.05 0.20 0.05 0.20 727 3,184
TK-01 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-02 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-03 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-04 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-05 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-06 --- --- --- --- 0.01 0.06 --- --- --- --- --- --- --- ---
TK-07 --- --- --- --- 3E-04 1E-03 --- --- --- --- --- --- --- ---
TK-08 --- --- --- --- 3E-04 1E-03 --- --- --- --- --- --- --- ---
TLO-SC --- --- --- --- --- 7.51 --- --- --- --- --- --- --- ---
TLO-PW --- --- --- --- --- 0.14 --- --- --- --- --- --- --- ---
TOTAL 19.48 86.82 15.28 71.67 18.12 91.38 0.19 0.86 1.75 7.77 1.75 7.77 26,230 116,901
Annual emissions shall be based on 8,760 hours per year of operation for all emission units except emergency generators.According to 45CSR14 Section 2.43.e, fugitive emissions are not included in the major source determination because it is not listed as one of the source categories in Table 1. Therefore, fugitive emissions shall not be included in the PTE above.
ATTACHMENT V - FACILITY-WIDE CONTROLLED EMISSIONS SUMMARY SHEET
Emission
Unit ID
List all sources of emissions in this table. Use extra pages if necessary.
ATTACHMENT V - FACILITY-WIDE CONTROLLED EMISSIONS SUMMARY SHEET
GHG (CO2e)PM2.5PM10SO2VOCCONOX
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
CE-01 0.28 1.22 3E-03 0.01 2E-03 0.01 2E-04 1E-03 1E-03 5E-03 0.01 0.03 0.39 1.72
CE-02 0.28 1.22 3E-03 0.01 2E-03 0.01 2E-04 1E-03 1E-03 5E-03 0.01 0.03 0.39 1.72
CE-03 0.28 1.22 3E-03 0.01 2E-03 0.01 2E-04 1E-03 1E-03 5E-03 0.01 0.03 0.39 1.72
CE-04 0.28 1.22 3E-03 0.01 2E-03 0.01 2E-04 1E-03 1E-03 5E-03 0.01 0.03 0.39 1.72
CRP --- --- 0.01 0.04 0.01 0.04 0.01 0.04 0.01 0.04 0.12 0.51 0.16 0.72
SSM-CBD --- --- --- 0.01 --- 0.01 --- 0.01 --- 0.01 --- 0.07 --- 0.10
SSM-ESD --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- 2E-04 --- 3E-03 --- 4E-03
SSM-PIG --- --- --- 2E-04 --- 2E-04 --- 2E-04 --- 2E-04 --- 2E-03 --- 3E-03
FLR --- 1E-03 --- --- --- --- --- --- --- --- --- --- --- 1E-03
GT 0.02 0.09 4E-04 2E-03 4E-03 0.02 9E-04 4E-03 2E-03 0.01 --- --- 0.03 0.14
DFT --- --- 4E-04 2E-03 1E-03 0.01 5E-04 2E-03 5E-04 2E-03 0.02 0.10 0.03 0.11
DSV --- --- 0.04 0.16 0.17 0.74 0.12 0.53 0.21 0.91 0.06 0.27 0.60 2.61
RBV 1E-04 6E-04 4E-06 2E-05 7E-06 3E-05 --- --- --- --- 4E-03 0.02 4E-03 0.02
TOx 5E-04 2E-03 --- --- --- --- --- --- --- --- --- --- 5E-04 2E-03
TK-01 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-02 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-03 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-04 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-05 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-06 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-07 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TK-08 --- --- 1E-05 5E-05 1E-04 6E-04 3E-04 1E-03 4E-04 2E-03 1E-03 5E-03 2E-03 0.01
TLO-SC --- --- --- 0.01 --- 0.08 --- 0.16 --- 0.21 --- 0.58 --- 1.08
TLO-PW --- --- --- 1E-04 --- 1E-03 --- 3E-03 --- 4E-03 --- 0.01 --- 0.02
TOTAL 1.13 4.96 0.06 0.27 0.19 0.94 0.14 0.76 0.23 1.21 0.24 1.71 2.41 11.77
Annual emissions shall be based on 8,760 hours per year of operation for all emission units except emergency generators.According to 45CSR14 Section 2.43.e, fugitive emissions are not included in the major source determination because it is not listed as one of the source categories in Table 1. Therefore, fugitive emissions shall not be included in the PTE above.
ATTACHMENT V - FACILITY-WIDE HAP CONTROLLED EMISSIONS SUMMARY SHEET
ATTACHMENT V - FACILITY-WIDE HAP CONTROLLED EMISSIONS SUMMARY SHEET
List all sources of emissions in this table. Use extra pages if necessary.
Emission
Unit ID
Formaldehyde Benzene Toluene Ethylbenzene Xylenes Hexane Total HAPs
Attachment W
Class I Legal Advertisement
87.03 tons of nitrogen oxides per year73.18 tons of carbon monoxide per year
103.35 tons of volatile organic compounds per year7.79 tons of particulate matter per year0.86 tons of sulfur dioxide per year
13.00 tons of total hazardous air pollutants per year117,369 tons of carbon dioxide equivalent per year
Dated this the 18 day of May 2018.
By: Appalachia Midstream Services, LLCMr. Paul V. HunterVice PresidentPark Place Corporate Center 22000 Commerce DrivePittsburgh, PA 15275-1026
Threedubs Compressor Station (3WCS)ATTACHMENT W
Application for G35-D General Permit RegistrationPublic Notice
Written comments will be received by the West Virginia Department of Environmental Protection, Division ofAir Quality, 601 57th Street, SE, Charleston, WV 25304, for at least 30 calendar days from the date ofpublication of this notice.
Any questions regarding this permit application should be directed to the DAQ at (304) 926-0499, extension1250, during normal business hours.
Notice of Application
Notice is given that Appalachia Midstream Services, LLC (AMS) has applied to the West Virginia Departmentof Environmental Protection, Division of Air Quality, for a G35-D General Permit Registration for the ThreedubsCompressor Station (3WCS), located at the end of Grizzle Ln (Approximately 0.3 mi East of Apple Pie RidgeRd), Wellsburg, in Brooke County, West Virginia 26070.
The latitude and longitude coordinates are 40.19278°North x -80.61861°West.
The applicant estimates the potential to discharge the following regulated air pollutants will be:
Startup of operation is planned to begin late 2018 or early 2019.
AIR QUALITY PUBLIC NOTICE
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
ATTACHMENT W
Public Notice
Note: Affidavit of Publication will be submitted upon receipt by AMS from the publisher.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendices
to Application for G35-D General Permit Registration
• Appendix S1 – Lab Analysis
• Appendix S2 – AP-42 / EPA Emission Factors
• Appendix S3 – Btu Loading
• Appendix S4 – Vendor Data
• Appendix S5 – Emission Programs
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendix S1
Lab Analysis
• Wet Gas – Summary
• Wet Gas – Lab Analysis
• Condensate – Summary
• Condensate – Lab Analysis
Sampled: From Pioneer CF Process Simulation GPSA-Sec 23
Water 109-86-4 H2O 18.015 --- --- --- --- --- --- --- ---Carbon Dioxide 124-38-9 CO2 44.010 0.1098 0.048 127.36 0.2157 --- --- --- ---Hydrogen Sulfide 2148-87-8 H2S 34.086 --- --- --- --- --- --- 638 ---Nitrogen 7727-37-9 N2 28.013 0.4144 0.116 305.91 0.5180 --- --- --- ---Methane* 75-82-8 CH4 16.042 71.6162 11.489 30,275.47 51.2647 51.6435 --- 1,010 723.323Ethane* 74-84-0 C2H6 30.069 17.0404 5.124 13,502.33 22.8631 23.0321 --- 1,770 301.564Propane** 74-98-6 C3H8 44.096 6.6780 2.945 7,759.82 13.1395 13.2366 52.2684 2,516 168.032iso-Butane** 75-28-5 i-C4H10 58.122 0.6673 0.388 1,021.98 1.7305 1.7433 6.8838 3,252 21.699n-Butane** 106-97-8 n-C4H10 58.122 2.1619 1.257 3,311.15 5.6067 5.6481 22.3032 3,262 70.529iso-Pentane** 78-78-4 i-C5H12 72.149 0.3376 0.244 641.90 1.0869 1.0950 4.3237 4,001 13.508n-Pentane** 109-66-0 n-C5H12 72.149 0.5333 0.385 1,013.91 1.7168 1.7295 6.8294 4,009 21.379Cyclopentane** 287-92-3 C5H10 70.100 --- --- --- --- --- --- 3,764 ---Cyclohexane** 110-82-7 C6H12 84.162 0.0162 0.014 35.90 0.0608 0.0612 0.2418 4,482 0.725Other Hexanes** Various C6H14 86.175 0.1863 0.161 422.98 0.7162 0.7215 2.8491 4,750 8.848Heptanes** 142-82-5 C7H16 100.205 0.0934 0.094 246.68 0.4177 0.4208 1.6615 5,503 5.140Methylcyclohexane** 108-87-2 C7H14 98.186 0.0191 0.019 49.41 0.0837 0.0843 0.3328 5,216 0.996C8+ Heavies** Various C8+ 138.00 est. 0.0386 0.053 140.43 0.2378 0.2396 0.9459 7,000 2.703Benzene*** 71-43-2 C6H6 78.112 0.0008 0.001 1.60 0.0027 0.0027 0.0108 3,742 0.029Ethylbenzene*** 100-41-4 C8H10 106.165 0.0013 0.001 3.71 0.0063 0.0063 0.0250 5,222 0.069n-Hexane*** 110-54-3 C6H14 86.175 0.0796 0.069 180.86 0.3062 0.3085 1.2182 4,756 3.788Toluene*** 108-88-3 C7H8 92.138 0.0024 0.002 5.80 0.0098 0.0099 0.0390 4,475 0.1072,2,4-Trimethylpentane*** 540-84-1 C8H18 114.229 0.0018 0.002 5.51 0.0093 0.0094 0.0371 6,214 0.114Xylenes*** 1330-20-7 C8H10 106.165 0.0016 0.002 4.48 0.0076 0.0076 0.0302 5,209 0.083
Totals: 100.00 22.41 59,057 100.00 --- --- 1,343
THC: 99.48 22.25 58,624 99.27 100.00 ---
Total VOC: 10.82 5.63 14,846 25.14 25.32 100.00
Total HAP: 0.09 0.08 202 0.34 0.34 1.36 1,020
Mole % Wgt % lb/MMscf Wgt % lb/MMscf
0.11 0.22 127 0.22 153 20% Margin
71.62 51.26 30,275 53.34 36,331 20% Margin
17.45 23.38 13,808 20.27 13,808 0% Margin
10.82 25.14 14,846 26.16 17,815 20% Margin
100.00 100.00 59,057 100.00 68,107
0.00 0.00 1.60 0.01 25 1465% Margin
0.00 0.01 3.71 0.04 25 574% Margin
0.08 0.31 181 0.44 300 66% Margin
0.00 0.01 5.80 0.04 25 331% Margin
* = Hydrocarbon (HC) 0.00 0.01 5.51 0.04 25 354% Margin
** = also Volatile Organic Compound (VOC) 0.00 0.01 4.48 0.04 25 458% Margin
*** = also Hazardous Air Pollutant (HAP) 0.09 0.34 202 0.62 425
Threedubs Compressor Station (3WCS) Application for G35-D General Permit RegistrationWet Gas - Summary
Supplement S1 - Wet Gas Analysis
Total HAP***
Xylenes***
2,2,4-Trimethylpentane***
Toluene***
n-Hexane***
Ethylbenzene***
Benzene***
TOTAL GAS
VOC**
Other (N2, C2, O2, CO, H2O)
Methane*
CO2
Component
Calculated
Btu/scf
(HHV):
Worst-Case
Btu/scf
(HHV):
lb "X"/scf =(M% of "X") x (MW of "X") / #UGC
#UGC (Universal Gas Constant) = 379.482 scf/lb-mol @ 60 oF and 14.6959 psia.
Margin for Changes
in Future Gas Composition
Representative Wet Gas AnalysisAssumed "Worst-Case"
120% VOC and GHG
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Wet Gas - Summary
Component CAS FormulaMolecular
Weight (MW)
Mole %
(M% = V%)
Mole
Fraction
(MF)
lb/MMscf
(WS/UGC#)
Weight %
Total
Btu/scf
(HHV)
Weight %
THC
Weight %
VOC
Component
Btu/scf (HHV)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Wet Gas - Lab Analysis
Application for G35-D General Permit RegistrationThreedubs Compressor Station (3WCS)
Sampled: From Pioneer CF Process Simulation GPSA-Sec 23
Water 109-86-4 H2O 18.015 --- --- --- --- --- --- --- ---Carbon Dioxide 124-38-9 CO2 44.010 --- --- --- --- --- --- --- ---Nitrogen 7727-37-9 N2 28.013 --- --- --- --- --- --- --- ---Methane* 75-82-8 CH4 16.042 --- --- --- --- --- --- 1,010 ---Ethane* 74-84-0 C2H6 30.069 0.0001 0.000 0.05 0.0000 0.0000 --- 1,770 0.001Propane** 74-98-6 C3H8 44.096 1.1300 0.498 1,313.05 0.4896 0.4896 0.4896 2,516 28.433iso-Butane** 75-28-5 i-C4H10 58.122 1.7000 0.988 2,603.75 0.9710 0.9710 0.9710 3,252 55.284n-Butane** 106-97-8 n-C4H10 58.122 9.2900 5.400 14,228.74 5.3060 5.3060 5.3060 3,262 303.077iso-Pentane** 78-78-4 i-C5H12 72.149 4.3300 3.124 8,232.39 3.0699 3.0699 3.0699 4,001 173.239n-Pentane** 109-66-0 n-C5H12 72.149 9.4400 6.811 17,947.74 6.6929 6.6929 6.6929 4,009 378.440Cyclopentane** 287-92-3 C5H10 70.100 --- --- --- --- --- --- 3,764 ---Cyclohexane** 110-82-7 C6H12 84.162 1.2750 1.073 2,827.71 1.0545 1.0545 1.0545 4,482 57.140Other Hexanes** Various C6H14 86.175 8.6600 7.463 19,665.72 7.3335 7.3335 7.3335 4,750 411.376Heptanes** 142-82-5 C7H16 100.205 16.7567 16.791 44,247.29 16.5002 16.5002 16.5002 5,503 922.037Methylcyclohexane** 108-87-2 C7H14 98.186 4.1700 4.094 10,789.34 4.0234 4.0234 4.0234 5,216 217.503C8+ Heavies** Various C8+ 138.00 est. 33.8747 46.747 123,186.69 45.9374 45.9374 45.9374 7,000 2371.231Benzene*** 71-43-2 C6H6 78.112 0.0615 0.048 126.59 0.0472 0.0472 0.0472 3,742 2.301Ethylbenzene*** 100-41-4 C8H10 106.165 1.2000 1.274 3,357.16 1.2519 1.2519 1.2519 5,222 62.664n-Hexane*** 110-54-3 C6H14 86.175 5.4700 4.714 12,421.65 4.6321 4.6321 4.6321 4,756 260.153Toluene*** 108-88-3 C7H8 92.138 0.6950 0.640 1,687.46 0.6293 0.6293 0.6293 4,475 31.1012,2,4-Trimethylpentane*** 540-84-1 C8H18 114.229 0.3760 0.429 1,131.80 0.4221 0.4221 0.4221 6,214 23.363Xylenes*** 1330-20-7 C8H10 106.165 1.5710 1.668 4,395.08 1.6390 1.6390 1.6390 5,209 81.828
Totals: 100.00 101.76 268,162 100.00 --- --- 5,379
THC: 100.00 101.76 268,162 100.00 100.00 ---
Total VOC: 100.00 101.76 268,162 100.00 100.00 100.00
Total HAP: 9.37 8.77 23,120 8.62 8.62 8.62
120% VOC 200% HAP
Mole % Wgt % lb/MMscf Wgt % lb/MMscf
--- --- --- --- --- --- --- --- --- ---
7E-05 2E-05 0.05 2E-05 0.05 0% Margin
100.00 100.00 268,162 100.00 321,795 20% Margin
100.00 100.00 268,162 100.00 321,795
0.06 0.05 127 0.09 253 100% Margin
1.20 1.25 3,357 2.09 6,714 100% Margin
5.47 4.63 12,422 7.72 24,843 100% Margin
0.70 0.63 1,687 1.05 3,375 100% Margin
* = Hydrocarbon (HC) 0.38 0.42 1,132 0.70 2,264 100% Margin
** = also Volatile Organic Compound (VOC) 1.57 1.64 4,395 2.73 8,790 100% Margin
*** = also Hazardous Air Pollutant (HAP) 9.37 8.62 23,120 14.37 46,239
Btu/scf
(HHV)
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Condensate - Summary
Component CAS FormulaMolecular
Weight (MW)
Mole %
(M% = V%)
Mole
Fraction
(MF)
lb/MMscf
(WS/UGC#)
Weight %
Total
Weight %
THC
Weight %
VOC
Component
Btu/scf (HHV)
#UGC (Universal Gas Constant) = 379.482 scf/lb-mol @ 60 oF and 14.6959 psia.
Calculated
Btu/scf
(HHV):
lb "X"/scf =(M% of "X") x (MW of "X") / #UGC
ComponentRepresentative Condensate Analysis
Assumed "Worst-Case" Margin for Changes
in Future Condensate
Composition
---
---
Xylenes***
CO2
Methane*
Other (N2, C2, O2, CO, H2O)
VOC**
TOTAL RAW CONDENSATE
Benzene***
Ethylbenzene***
n-Hexane***
Toluene***
2,2,4-Trimethylpentane***
Total HAP***
Threedubs Compressor Station (3WCS)Supplement S1 - Raw Condensate Analysis
Application for G35-D General Permit RegistrationCondensate - Summary
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Condensate - Lab Analysis
Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendix S2
AP-42 / EPA Emission Factors
• AP-42 – Combustion Emission Factor Summary
• EPA Protocol for Equipment Leak Emission Estimates
2SLB 4SLB 4SRB Uncontrolled Water Injection Lean Pre-Mix#
lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu
NOX (≥ 90% Load) 3.17E+00 4.08E+00 2.21E+00 3.23E-01 1.28E-01 9.91E-02CO (≥ 90% Load) 3.86E-01 3.17E-01 3.72E+00 8.23E-02 2.95E-02 1.51E-02VOC 1.20E-01 1.18E-01 2.96E-02 2.10E-03 2.10E-03 2.10E-03PM10/2.5 (Total) 4.83E-02 9.99E-03 1.94E-02 6.63E-03 6.63E-03 6.63E-03SO2 5.88E-04 5.88E-04 5.88E-04 3.40E-03 3.40E-03 3.40E-03Acetaldehyde 7.76E-03 8.36E-03 2.79E-03 4.00E-05 4.00E-05 4.00E-05Acrolein 7.78E-03 5.14E-03 2.63E-03 6.40E-06 6.40E-06 6.40E-06Benzene 1.94E-03 4.40E-04 1.58E-03 1.20E-05 1.20E-05 9.10E-07Butadiene, 1,3- 8.20E-04 2.67E-04 6.63E-04 4.30E-07 4.30E-07 4.30E-07Ethylbenzene 1.08E-04 3.97E-05 2.48E-05 3.20E-05 3.20E-05 3.20E-05Formaldehyde (HCHO) 5.52E-02 5.28E-02 2.05E-02 7.10E-04 7.10E-04 2.00E-05n-Hexane 4.45E-04 1.11E-03 --- --- --- ---Methanol (MeOH) 2.48E-03 2.50E-03 3.06E-03 --- --- ---Polycyclic Organic Matter (POM/PAH) 1.34E-04 3.47E-04 9.71E-05 3.25E-05 3.25E-05 3.25E-05Toluene 9.63E-04 4.08E-04 5.58E-04 1.30E-04 1.30E-04 1.30E-04Trimethylpentane, 2,2,4- (i-Octane) 8.46E-04 2.50E-04 --- --- --- ---Xylenes 2.68E-04 1.84E-04 1.95E-04 6.40E-05 6.40E-05 6.40E-05Other/Trace HAP* 6.57E-04 3.21E-04 1.79E-04 2.90E-05 2.90E-05 2.90E-05TOTAL HAP 7.94E-02 7.22E-02 3.23E-02 1.06E-03 1.06E-03 3.55E-04CO2 (GWP=1) 1.10E+02 1.10E+02 1.10E+02 1.10E+02 1.10E+02 1.10E+02CH4 (GWP=25) 1.45E+00 1.25E+00 2.30E-01 8.64E-03 8.64E-03 8.64E-03N2O (GWP=298) (40CFR98 ) 2.20E-04 2.20E-04 2.20E-04 3.00E-03 3.00E-03 3.00E-03CO2e (40CFR98 ) 1.46E+02 1.41E+02 1.16E+02 1.11E+02 1.11E+02 1.11E+02
(#Lean Pre-Mix - aka: Dry Low Emissions (DLE or DLN) or SoLoNOx)FLARE DIESEL ENGINES DIESEL ENGINES
13.5-1 06/17 3.3-1; 3.3-2 10/96 Tier 4 ≥ 751 bhpUncontrolled LoNOx Burners Flue Gas Recirc Combustion Uncontrolled Controlled
lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu lb/MMBtu
NOX (≥ 90% Load) 9.80E-02 4.90E-02 3.14E-02 External Comb. 4.41E+00 4.18E+00CO (≥ 90% Load) 8.24E-02 8.24E-02 8.24E-02 3.10E-01 9.50E-01 2.35E+00VOC 5.39E-03 5.39E-03 5.39E-03 98% Control 3.53E-01 1.28E-01PM10/2.5 (Total) 7.45E-03 7.45E-03 7.45E-03 External Comb. 3.10E-01 1.35E-01SO2 5.88E-04 5.88E-04 5.88E-04 External Comb. 2.90E-01 2.90E-01Acetaldehyde --- --- --- 7.67E-04 2.77E-04Acrolein --- --- --- 9.25E-05 3.35E-05Benzene 2.06E-06 2.06E-06 2.06E-06 9.33E-04 3.38E-04Butadiene, 1,3- --- --- --- 3.91E-05 1.41E-05Ethylbenzene --- --- --- --- ---Formaldehyde (HCHO) 7.35E-05 7.35E-05 7.35E-05 1.18E-03 4.27E-04n-Hexane 1.76E-03 1.76E-03 1.76E-03 --- ---Methanol (MeOH) --- --- --- --- ---Polycyclic Organic Matter (POM/PAH) 6.85E-07 6.85E-07 6.85E-07 1.68E-04 6.08E-05Toluene 3.33E-06 3.33E-06 3.33E-06 4.09E-04 1.48E-04Trimethylpentane, 2,2,4- (i-Octane) --- --- --- --- ---Xylenes --- --- --- 2.85E-04 1.03E-04Other/Trace HAP* 1.18E-06 1.18E-06 1.18E-06 --- ---TOTAL HAP 1.85E-03 1.85E-03 1.85E-03 3.87E-03 1.40E-03CO2 (GWP=1) 1.18E+02 1.18E+02 1.18E+02 1.64E+02 1.64E+02CH4 (GWP=25) 2.25E-03 2.25E-03 2.25E-03 6.61E-03 6.61E-03
N2O (GWP=298) (40CFR98 ) 2.16E-03 6.27E-04 6.27E-04 1.32E-03 1.32E-03
CO2e (40CFR98 ) 1.18E+02 1.18E+02 1.18E+02 1.65E+02 1.65E+02
Weighted SumCarbon Dioxide Methane Nitrous Oxide CO2e
lb CO2/MMBtu lb CH4/MMBtu lb N2O/MMBtu lb CO2e/MMBtu
Fuel Oil No. 2 (Diesel) 138,000 Btu/gal 1.63E+02 6.61E-03 1.32E-03 1.64E+02Propane 91,000 Btu/gal 1.39E+02 6.61E-03 1.32E-03 1.39E+02Natural Gas 1,026 Btu/scf 1.17E+02 2.20E-03 2.20E-04 1.17E+02
CO2 CH4 N2O
1 25 298Reviewed and Revised: 02/28/18 - CAR
Supplement S2 - Emission Factors
CR
ITER
IAPotentially Applicable
AP-42 and GHG EMISSION FACTORS(Preferentially use test data or vendor data where available)
Global Warming Potential (100 Yr) (GWP)
Table A-1 to Subpart A of Part 98*Other/Trace HAPs include: CarbonTetrachloride, Chlorobenzene, Chloroform, Dichloropropene, 1,3-Dichloropropene, Ethylene Dibromide, Methylene Chloride, Phenol, Propylene Oxide, Styrene, 1,1,2,2-Tetrachloroethane, 1,1,2-Trichloroethane, and Vinyl Chloride (as per AP-42).
Fuel TypeDefault HHV
Table C-1 to Subpart C of Part 98 Table C-2 to Subpart C of Part 98
40 CFR 98 - DEFAULT EMISSION FACTORS
Use External
Combustion or 98% Control,As Applicable
AP-42 Table 1.4-1; 1.4-2; 1.4-3 (<100 MMBtu/hr) 07/98
GH
G
GAS-FIRED EXTERNAL COMBUSTION
CR
ITER
IAH
APs
Pollutant
Pollutant
GAS-FIRED ENGINES GAS-FIRED TURBINES
AP-42 Table 3.2-1; 3.2-2; 3.2-3 07/00 AP-42 Table 3.1-1; 3.1-2a; 3.1-3 04/00
GH
GH
APs
Supplement S2 - Emission Factors
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendix S3
Btu Loading
• Btu Loading – Zeeco MJ-16 Sonic Flare (FLR)
• Btu Loading – Zeeco Z-HTO Thermal Oxidizer (TOx)
Ave Flowrate:
2,803
Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr MMBtu/Hr
Water --- --- --- --- --- --- --- --- --- --- --- ---
Carbon Monoxide --- --- --- --- --- --- --- --- --- --- --- ---
Nitrogen --- 0.4144 --- 0.4144 --- 0.4144 --- 0.4144 --- 0.4144 --- ---
Oxygen --- --- --- --- --- --- --- --- --- --- --- ---
Hydrogen Sulfide 637.64 --- --- --- --- --- --- --- --- --- --- ---
Carbon Dioxide --- 0.1098 --- 0.1098 --- 0.1098 --- 0.1098 --- 0.1098 --- ---
Methane 1,010.00 71.6162 1.8800 71.6162 0.0002 71.6162 0.0002 71.6162 0.0798 71.6162 0.0675 2.0277
Ethane 1,769.70 17.0404 0.7838 17.0404 0.0001 17.0404 0.0001 17.0404 0.0333 17.0404 0.0281 0.8454
Propane 2,516.20 6.6780 0.4367 6.6780 0.0000 6.6780 0.0000 6.6780 0.0185 6.6780 0.0157 0.4710
i-Butane 3,252.00 0.6673 0.0564 0.6673 0.0000 0.6673 0.0000 0.6673 0.0024 0.6673 0.0020 0.0608
n-Butane 3,262.40 2.1619 0.1833 2.1619 0.0000 2.1619 0.0000 2.1619 0.0078 2.1619 0.0066 0.1977
Cyclopentane 3,763.60 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
i-Pentane 4,000.90 0.3376 0.0351 0.3376 0.0000 0.3376 0.0000 0.3376 0.0015 0.3376 0.0013 0.0379
n-Pentane 4,008.90 0.5333 0.0556 0.5333 0.0000 0.5333 0.0000 0.5333 0.0024 0.5333 0.0020 0.0599
Cyclohexane 4,481.60 0.0162 0.0019 0.0162 0.0000 0.0162 0.0000 0.0162 0.0001 0.0162 0.0001 0.0020
Other Hexanes 4,750.30 0.1863 0.0230 0.1863 0.0000 0.1863 0.0000 0.1863 0.0010 0.1863 0.0008 0.0248
Methylcyclohexane 5,215.90 0.0185 0.0025 0.0185 0.0000 0.0185 0.0000 0.0185 0.0001 0.0185 0.0001 0.0027
Heptanes 5,502.50 0.0899 0.0129 0.0899 0.0000 0.0899 0.0000 0.0899 0.0005 0.0899 0.0005 0.0139
C8+ Heavies 7,150.00 est 0.0376 0.0070 0.0376 0.0000 0.0376 0.0000 0.0376 0.0003 0.0376 0.0003 0.0075
Benzene 3,741.90 0.0008 0.0001 0.0008 0.0000 0.0008 0.0000 0.0008 0.0000 0.0008 0.0000 0.0001
Ethylbenzene 5,222.00 0.0013 0.0002 0.0013 0.0000 0.0013 0.0000 0.0013 0.0000 0.0013 0.0000 0.0002
n-Hexane 4,756.00 0.0796 0.0098 0.0796 0.0000 0.0796 0.0000 0.0796 0.0004 0.0796 0.0004 0.0106
Toluene 4,474.90 0.0024 0.0003 0.0024 0.0000 0.0024 0.0000 0.0024 0.0000 0.0024 0.0000 0.0003
2,2,4-TMP (i-Octane) 6,213.60 0.0018 0.0003 0.0018 0.0000 0.0018 0.0000 0.0018 0.0000 0.0018 0.0000 0.0003
Xylenes 5,208.67 0.0016 0.0002 0.0016 0.0000 0.0016 0.0000 0.0016 0.0000 0.0016 0.0000 0.0002
99.99 99.99Average MMBtu/hr: 3.49 4E-04 4E-04 0.15 0.13 3.76
Average scf/hr: 2,599 0.27 0.27 110 93.26 2,803
Average Btu/scf: 1,342 1,342 1,342 1,342 1,342 1,342
Ave Flowrate:
0.27 scf/hr
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Btu Loading – Zeeco MJ-16 Sonic Flare (FLR)
Component
Component
Btu/scf
(HHV)
Comp Blowdown
(CE-01 thru CE-04)TOTAL
Application for G35-D General Permit Registration
Mol%=Vol% Values from
Wet Gas Lab Analysis
Threedubs Compressor Station (3WCS) Btu Loading – Zeeco MJ-16 Sonic Flare (FLR)
Comp Blowdown
(CE-05)
Pigging
(PIG)
Ave Flowrate: Ave Flowrate:
110 scf/hr 93.26 scf/hr
Ave Flowrate:
2,599 scf/hr
Ave Flowrate:
0.27 scf/hr
Emergency S/D
(ESD)
Comp Blowdown
(CE-06)
Ave Flowrate:
7,470
Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr Mol% MMBtu/hr MMBtu/Hr
Water --- 0.1330 --- 91.9000 --- --- --- --- --- --- --- ---
Carbon Monoxide --- --- --- --- --- --- --- --- --- --- --- ---
Nitrogen --- 0.3560 --- 0.0052 --- --- --- --- --- --- --- ---
Oxygen --- --- --- --- --- --- --- --- --- --- --- ---
Hydrogen Sulfide 637.64 --- --- --- --- --- --- --- --- --- --- ---
Carbon Dioxide --- 0.6410 --- 1.3100 --- --- --- --- --- --- --- ---
Methane 1,010.00 49.5000 0.7949 0.7490 0.0445 --- --- --- --- --- --- 0.8394
Ethane 1,769.70 28.0000 0.7879 1.5800 0.1644 --- --- --- --- --- --- 0.9523
Propane 2,516.20 12.5000 0.5001 1.5700 0.2323 --- --- --- --- --- --- 0.7324
i-Butane 3,252.00 1.3300 0.0688 0.2620 0.0501 --- --- --- --- --- --- 0.1189
n-Butane 3,262.40 4.9100 0.2547 1.3000 0.2494 --- --- --- --- --- --- 0.5041
Cyclopentane 3,763.60 --- --- --- --- --- --- --- --- --- --- 0.0000
i-Pentane 4,000.90 0.6330 0.0403 0.1970 0.0463 --- --- --- --- --- --- 0.0866
n-Pentane 4,008.90 1.1200 0.0714 0.4450 0.1049 --- --- --- --- --- --- 0.1763
Cyclohexane 4,481.60 0.0471 0.0034 0.1420 0.0374 --- --- --- --- --- --- 0.0408
Other Hexanes 4,750.30 0.3490 0.0264 0.1940 0.0542 --- --- --- --- --- --- 0.0805
Methylcyclohexane 5,215.90 0.0414 0.0034 0.1650 0.0506 --- --- --- --- --- --- 0.0540
Heptanes 5,502.50 0.1620 0.0142 0.2600 0.0841 --- --- --- --- --- --- 0.0983
C8+ Heavies 7,150.00 est 0.0075 0.0008 0.1340 0.0563 --- --- --- --- --- --- 0.0572
Benzene 3,741.90 0.0033 0.0002 0.0771 0.0170 --- --- --- --- --- --- 0.0172
Ethylbenzene 5,222.00 0.0027 0.0002 0.1830 0.0562 --- --- --- --- --- --- 0.0564
n-Hexane 4,756.00 0.1560 0.0118 0.1160 0.0324 --- --- --- --- --- --- 0.0442
Toluene 4,474.90 0.0077 0.0005 0.2940 0.0774 --- --- --- --- --- --- 0.0779
2,2,4-TMP (i-Octane) 6,213.60 0.0022 0.0002 0.0017 0.0006 --- --- --- --- --- --- 0.0008
Xylenes 5,208.67 0.0031 0.0003 0.3140 0.0962 --- --- --- --- --- --- 0.0964
99.90 101.20Average MMBtu/hr: 2.58 1.45 --- --- --- 4.03
Average scf/hr: 1,590 5,880 --- --- --- 7,470
Average Btu/scf: 1,622 247 --- --- --- 540
Appalachia Midstream Services, LLC (AMS)Threedubs Compressor Station (3WCS)
Application for G35-D General Permit Registration
Btu Loading – Zeeco Z-HTO Thermal Oxidizer (TOx)
Component
Component
Btu/scf
(HHV)
Ave Flowrate:
DFT - Flash Gas DSV - Still Vent TOTAL
Btu Loading – Zeeco Z-HTO Thermal Oxidizer (TOx)
1,590 scf/hr 5,880 scf/hr
Application for G35-D General Permit Registration
Mol%=Vol% Values from
GRI-GLYCalc Model Results
Threedubs Compressor Station (3WCS)
Ave Flowrate:
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendix S4
Vendor Data
• 5,000 bhp CAT G3616LE A4 w/ OxCat (CE-01 thru CE-04)
• Zeeco MJ-16 Sonic Flare (FLR)
• 1,746 bhp FlexEnergy GT1300S Microturbine Generator (GT)
• Zeeco Z-HTO Thermal Oxidizer (TOx)
G3616 GAS ENGINE SITE SPECIFIC TECHNICAL DATAGAS COMPRESSION APPLICATION
PREPARED BY:Data generated by Gas Engine Rating Pro Version 6.04.00Ref. Data Set EM1426-04-001, Printed 03May2017 Page 1 of 4
ENGINE SPEED (rpm): 1000 RATING STRATEGY: STANDARDCOMPRESSION RATIO: 7.6 RATING LEVEL: CONTINUOUSAFTERCOOLER TYPE: SCAC FUEL SYSTEM: GAVAFTERCOOLER - STAGE 2 INLET (°F): 130 WITH AIR FUEL RATIO CONTROLAFTERCOOLER - STAGE 1 INLET (°F): 174 SITE CONDITIONS:JACKET WATER OUTLET (°F): 190 FUEL: PioneerASPIRATION: TA FUEL PRESSURE RANGE(psig): (See note 1) 58.0-70.3COOLING SYSTEM: JW+1AC, OC+2AC FUEL METHANE NUMBER: 53.9CONTROL SYSTEM: ADEM4 FUEL LHV (Btu/scf): 1214EXHAUST MANIFOLD: DRY ALTITUDE(ft): 500COMBUSTION: LOW EMISSION MAXIMUM INLET AIR TEMPERATURE(°F): 77NOx EMISSION LEVEL (g/bhp-hr NOx): 0.3 STANDARD RATED POWER: 5000 bhp@1000rpmSET POINT TIMING: 16
MAXIMUMRATING
SITE RATING AT MAXIMUMINLET AIR TEMPERATURE
RATING NOTES LOAD 100% 100% 75% 50% ENGINE POWER (WITHOUT FAN) (2) bhp 5000 5000 3750 2500
INLET AIR TEMPERATURE °F 77 77 77 77
ENGINE DATA FUEL CONSUMPTION (LHV) (3) Btu/bhp-hr 6782 6782 6950 7414
FUEL CONSUMPTION (HHV) (3) Btu/bhp-hr 7466 7466 7651 8162
AIR FLOW (@inlet air temp, 14.7 psia) (WET) (4)(5) ft3/min 12425 12425 9379 6385
AIR FLOW (WET) (4)(5) lb/hr 55092 55092 41587 28311
FUEL FLOW (60ºF, 14.7 psia) scfm 466 466 358 254
INLET MANIFOLD PRESSURE (6) in Hg(abs) 107.9 107.9 80.6 56.3
EXHAUST TEMPERATURE - ENGINE OUTLET (7) °F 814 814 860 926
EXHAUST GAS FLOW (@engine outlet temp, 14.5 psia) (WET) (8)(5) ft3/min 31291 31291 24493 17538
EXHAUST GAS MASS FLOW (WET) (8)(5) lb/hr 56722 56722 42839 29202
EMISSIONS DATA - ENGINE OUT NOx (as NO2) (9)(10) g/bhp-hr 0.30 0.30 0.30 0.30
CO (9)(10) g/bhp-hr 2.93 2.93 2.93 2.94
THC (mol. wt. of 15.84) (9)(10) g/bhp-hr 3.72 3.72 4.08 4.33
NMHC (mol. wt. of 15.84) (9)(10) g/bhp-hr 1.85 1.85 2.03 2.15
NMNEHC (VOCs) (mol. wt. of 15.84) (9)(10)(11) g/bhp-hr 0.96 0.96 1.05 1.11
HCHO (Formaldehyde) (9)(10) g/bhp-hr 0.14 0.14 0.15 0.20
CO2 (9)(10) g/bhp-hr 443 443 460 487
EXHAUST OXYGEN (9)(12) % DRY 11.1 11.1 10.8 10.5
HEAT REJECTION HEAT REJ. TO JACKET WATER (JW) (13) Btu/min 53172 53172 43238 36471
HEAT REJ. TO ATMOSPHERE (13) Btu/min 18171 18171 16968 15506
HEAT REJ. TO LUBE OIL (OC) (13) Btu/min 30493 30493 27342 24075
HEAT REJ. TO A/C - STAGE 1 (1AC) (13)(14) Btu/min 46733 46733 24091 6534
HEAT REJ. TO A/C - STAGE 2 (2AC) (13)(14) Btu/min 11576 11576 8103 4994
COOLING SYSTEM SIZING CRITERIA TOTAL JACKET WATER CIRCUIT (JW+1AC) (14)(15) Btu/min 107559
TOTAL STAGE 2 AFTERCOOLER CIRCUIT (OC+2AC) (14)(15) Btu/min 48747
A cooling system safety factor of 0% has been added to the cooling system sizing criteria.
CONDITIONS AND DEFINITIONSEngine rating obtained and presented in accordance with ISO 3046/1, adjusted for fuel, site altitude and site inlet air temperature. 100% rating at maximum inlet air temperature is the maximum enginecapability for the specified fuel at site altitude and maximum site inlet air temperature. Maximum rating is the maximum capability at the specified aftercooler inlet temperature for the specified fuel atsite altitude and reduced inlet air temperature. Lowest load point is the lowest continuous duty operating load allowed. No overload permitted at rating shown.
For notes information consult page three.
G3616 GAS ENGINE SITE SPECIFIC TECHNICAL DATAGAS COMPRESSION APPLICATION
Engine Power vs. Inlet Air TemperatureData represents temperature sweep at 500 ft and 1000 rpm
No Rating AvailableRange for Site Conditions
Continuous OperatingRange for Site Conditions
Low Load IntermittentOperating Range
Air Temperature, °FAir Temperature, °FAir Temperature, °FAir Temperature, °F30303030 40404040 50505050 60606060 70707070 80808080 90909090 100100100100 110110110110 120120120120 130130130130
EE EEnn nn
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0000
500500500500
1000100010001000
1500150015001500
2000200020002000
2500250025002500
3000300030003000
3500350035003500
4000400040004000
4500450045004500
5000500050005000
5500550055005500
EEEEnnnn
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eeeePPPP
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eeeerrrr ,,,,
bbbbhhhh
pppp
0000
500500500500
1000100010001000
1500150015001500
2000200020002000
2500250025002500
3000300030003000
3500350035003500
4000400040004000
4500450045004500
5000500050005000
5500550055005500
Engine Power vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF
No Rating AvailableRange for Site Conditions
Continuous OperatingRange for Site Conditions
Low Load IntermittentOperating Range
Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)750750750750 800800800800 850850850850 900900900900 950950950950 1000100010001000
EE EEnn nn
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ee eePP PP
oo ooww ww
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bb bbhh hh
pp pp
0000
500500500500
1000100010001000
1500150015001500
2000200020002000
2500250025002500
3000300030003000
3500350035003500
4000400040004000
4500450045004500
5000500050005000
5500550055005500
0000
500500500500
1000100010001000
1500150015001500
2000200020002000
2500250025002500
3000300030003000
3500350035003500
4000400040004000
4500450045004500
5000500050005000
5500550055005500
Engine Torque vs. Engine SpeedData represents speed sweep at 500 ft and 77 ºF
No Rating AvailableRange for Site Conditions
Continuous OperatingRange for Site Conditions
Low Load IntermittentOperating Range
Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)Engine Speed (rpm)750750750750 800800800800 850850850850 900900900900 950950950950 1000100010001000
EE EEnn nn
gg ggii iinn nn
ee eeTT TT
oo oorr rrqq qq
uu uuee ee
,, ,,ff fftt tt
-- --ll llbb bb
0000
5000500050005000
10000100001000010000
15000150001500015000
20000200002000020000
25000250002500025000
30000300003000030000
0000
5000500050005000
10000100001000010000
15000150001500015000
20000200002000020000
25000250002500025000
30000300003000030000
Note: At site conditions of 500 ft and 77°F inlet air temp., constant torque can be maintained down to 750 rpm.The minimum speed for loading at these conditions is 750 rpm.
PREPARED BY:Data generated by Gas Engine Rating Pro Version 6.04.00Ref. Data Set EM1426-04-001, Printed 03May2017 Page 2 of 4
G3616 GAS ENGINE SITE SPECIFIC TECHNICAL DATAGAS COMPRESSION APPLICATION
NOTES1. Fuel pressure range specified is to the engine gas shutoff valve (GSOV). Additional fuel train components should be considered in pressure and flow calculations.
2. Engine rating is with two engine driven water pumps. Tolerance is ± 3% of full load.
3. Fuel consumption tolerance is ± 2.5% of full load data.
4. Air flow value is on a 'wet' basis. Flow is a nominal value with a tolerance of ± 5 %.
5. Inlet and Exhaust Restrictions must not exceed A&I limits based on full load flow rates from the standard technical data sheet.
6. Inlet manifold pressure is a nominal value with a tolerance of ± 5 %.
7. Exhaust temperature is a nominal value with a tolerance of (+)63°F, (-)54°F.
8. Exhaust flow value is on a "wet" basis. Flow is a nominal value with a tolerance of ± 6 %.
9. Emissions data is at engine exhaust flange prior to any after treatment.
10. Values listed are higher than nominal levels to allow for instrumentation, measurement, and engine-to-engine variations. They indicate the maximum values expected understeady state conditions. Fuel methane number cannot vary more than ± 3. THC, NMHC, and NMNEHC do not include aldehydes. An oxidation catalyst may be required to meetFederal, State or local CO or HC requirements.
11. VOCs - Volatile organic compounds as defined in US EPA 40 CFR 60, subpart JJJJ
12. Exhaust Oxygen level is the result of adjusting the engine to operate at the specified NOx level. Tolerance is ± 0.5.
13. Heat rejection values are nominal. Tolerances, based on treated water, are ± 10% for jacket water circuit, ± 50% for radiation, ± 20% for lube oil circuit, and ± 5% for aftercoolercircuit.
14. Aftercooler heat rejection includes an aftercooler heat rejection factor for the site elevation and inlet air temperature specified. Aftercooler heat rejection values at part load arefor reference only. Do not use part load data for heat exchanger sizing.
15. Cooling system sizing criteria are maximum circuit heat rejection for the site, with applied tolerances.
PREPARED BY:Data generated by Gas Engine Rating Pro Version 6.04.00Ref. Data Set EM1426-04-001, Printed 03May2017 Page 3 of 4
Constituent Abbrev Mole % NormWater Vapor H2O 0.0050 0.0050Methane CH4 71.6162 71.8339Ethane C2H6 17.0404 17.0922Propane C3H8 6.6780 6.6983Isobutane iso-C4H1O 0.6673 0.6693Norbutane nor-C4H1O 2.1619 2.1685Isopentane iso-C5H12 0.3376 0.3386Norpentane nor-C5H12 0.5333 0.5349Hexane C6H14 0.0796 0.0798Heptane C7H16 0.0408 0.0409Nitrogen N2 0.4144 0.4157Carbon Dioxide CO2 0.1098 0.1101Hydrogen Sulfide H2S 0.0000 0.0000Carbon Monoxide CO 0.0000 0.0000Hydrogen H2 0.0000 0.0000Oxygen O2 0.0000 0.0000Helium HE 0.0000 0.0000Neopentane neo-C5H12 0.0000 0.0000Octane C8H18 0.0102 0.0102Nonane C9H20 0.0024 0.0024Ethylene C2H4 0.0000 0.0000Propylene C3H6 0.0000 0.0000TOTAL (Volume %) 99.6969 99.9998
Fuel Makeup: Pioneer
Unit of Measure: English
Calculated Fuel PropertiesCalculated Fuel PropertiesCalculated Fuel PropertiesCalculated Fuel Properties
Caterpillar Methane Number: 53.9
Lower Heating Value (Btu/scf): 1214
Higher Heating Value (Btu/scf): 1336
WOBBE Index (Btu/scf): 1387
THC: Free Inert Ratio: 189.18
Total % Inerts (% N2, CO2, He): 0.53%
RPC (%) (To 905 Btu/scf Fuel): 100%
Compressibility Factor: 0.996
Stoich A/F Ratio (Vol/Vol): 12.57
Stoich A/F Ratio (Mass/Mass): 16.40
Specific Gravity (Relative to Air): 0.766
Fuel Specific Heat Ratio (K): 1.271
CONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCONDITIONS AND DEFINITIONSCaterpillar Methane Number represents the knock resistance of a gaseous fuel. It should be used with the Caterpillar Fuel Usage Guide for the engine and rating to determine the rating for the fuelspecified. A Fuel Usage Guide for each rating is included on page 2 of its standard technical data sheet.
RPC always applies to naturally aspirated (NA) engines, and turbocharged (TA or LE) engines only when they are derated for altitude and ambient site conditions.
Project specific technical data sheets generated by the Caterpillar Gas Engine Rating Pro program take the Caterpillar Methane Number and RPC into account when generating a site rating.
Fuel properties for Btu/scf calculations are at 60F and 14.696 psia.
Caterpillar shall have no liability in law or equity, for damages, consequently or otherwise, arising from use of program and related material or any part thereof.
FUEL LIQUIDSFUEL LIQUIDSFUEL LIQUIDSFUEL LIQUIDSField gases, well head gases, and associated gases typically contain liquid water and heavy hydrocarbons entrained in the gas. To prevent detonation and severe damage to the engine, hydrocarbonliquids must not be allowed to enter the engine fuel system. To remove liquids, a liquid separator and coalescing filter are recommended, with an automatic drain and collection tank to preventcontamination of the ground in accordance with local codes and standards.
To avoid water condensation in the engine or fuel lines, limit the relative humidity of water in the fuel to 80% at the minimum fuel operating temperature.
PREPARED BY:Data generated by Gas Engine Rating Pro Version 6.04.00Ref. Data Set EM1426-04-001, Printed 03May2017 Page 4 of 4
FEATURES AND BENEFITS
Cat® Engine Specifi cationsV-16, 4-Stroke-Cycle
Bore300 mm (11.8 in)
Stroke300 mm (11.8 in)
Displacement339 L (20,698 cu. in)
AspirationTurbocharged-Aftercooled
Digital Engine Management Governor and ProtectionElectronic (ADEM™ A4)
CombustionLow Emission (Lean Burn)
G3616 with ADEM™ A4 Gas Engine 3729-3990 bkW (5000-5350 bhp) @ 1000 rpm0.3 g/bhp-hr NOx (NTE)
Engine Design• Industry-leading power with ambient-based rating capability• ADEM A4 engine control system provides complete engine control,
monitoring, and protection while maintaining emissions.• Widest fuel tolerance in the industry for application fl exibility• Proven reliability and durability with the lowest owning and
operating costs• Factory-installed thermostats
EmissionsMeets U.S. EPA Spark Ignited Stationary NSPS Emissions for 2010 with the use of an oxidation catalyst
Lean Burn Engine TechnologyLean-burn engines operate with large amounts of excess air. The excess air absorbs heat during combustion reducing the combustion temperature and pressure, greatly reducing levels of NOx. Lean-burn design also provides longer component life and excellent fuel consumption.
Ease of OperationSide covers on block allow for inspection of internal components
Advanced Digital Engine ManagementADEM A4 engine management system integrates speed control, air/fuel ratio control, and ignition/detonation controls into a complete engine management system. ADEM A4 has improved: user interface, display system, shutdown controls, and system diagnostics.
Full Range of AttachmentsLarge variety of factory-installed attachments reduces packaging time.
TestingEvery engine is full-load tested to ensure proper engine performance.
Gas Engine Rating Pro (GERP)GERP is a PC-based program designed to provide site performance capabilities for Cat natural gas engines for the gas compression industry. GERP provides engine data for your site‘s altitude, ambient temperature, fuel, engine coolant heat rejection, performance data, installation drawings, spec sheets, and pump curves.
Product Support Offered Through Global Cat Dealer Network• More than 2,200 dealer outlets• Cat factory-trained dealer technicians service every aspect of your
Oil & Gas Engine• Caterpillar parts and labor warranty• Preventive maintenance agreements available for repair-before- failure options• S•O•SSM program matches your oil and coolant samples
against Caterpillar set standards to determine:- Internal engine component condition- Presence of unwanted fl uids- Presence of combustion by-products- Site-specifi c oil change interval
Over 80 Years of Engine Manufacturing ExperienceOver 60 years of natural gas engine production. Ownership of these manufacturing processes enables Caterpillar to produce high quality, dependable products. • Cast engine blocks, heads, cylinder liners, and fl ywheel housings• Machine critical components• Assemble complete engine
Web SiteFor all your Oil & Gas power requirements, visit www.cat.com
Cooling System CapacityTotal......................... 798 L (211 Gal)JW........................... 690 L (182 Gal)SCAC..........................108 L (29 Gal)
Lube Oil System (refi ll)1329 L (351 gal)
Oil Change Interval5000 hours
Rotation (from fl ywheel end)Counterclockwise
Flywheel Teeth255
Shown with optional equipment
STANDARD EQUIPMENT G3616 with ADEM A4 Gas Engine
Air Inlet System• Air cleaner — standard duty• Inlet air adapter
Control System• ADEM A4 control system — provides electronic governing
integrated with air/fuel ratio control and individual cylinder ignition timing control• Electrical system and instrumentation certifi ed for Class I, Division
2, Group D hazardous location. Includes entire ADEM A4 system and optional control panel
Cooling System• Compressor oil cooler connections• Jacket water pump• Jacket water thermostats and housing• Aftercooler/oil cooler pump• Aftercooler/oil cooler thermostats and housing• Two-stage aftercooler• Jacket water heater connections• Standard ANSI connections
Exhaust System• Dry exhaust manifolds• Single vertical outlet adapter• Form fi tted soft wrap insulation
Flywheels & Flywheel Housings• SAE standard rotation
Fuel System Gas admission valves — electronically controlled fuel supply pressure
Ignition System A4 control system — senses individual cylinder detonation and controls individual cylinder timing
Lube System• Crankcase breather —top mounted• Oil cooler• Oil fi lter• Oil pan drain valve - front and rear
Mounting System
Engine mounting feet (six total)
Protection System• Electronic shutoff system with purge cycle• Crankcase explosion relief valves• Gas shutoff valve
Starting System
Air starting system
General• Paint, Caterpillar yellow• Single vibration damper with guard
OPTIONAL EQUIPMENTAir Inlet System Heavy-duty air cleaner with precleaners
Charging System 35 Amp & 65 Amp charging alternators - CSA Approved
Exhaust System• Flexible bellows adapters• Exhaust expander• Weld fl anges
Fuel System• Fuel fi lter• Gas pressure regulator• Flexible connection
Instrumentation• LCD display panel• Color HMI display• Remote data monitoring and speed control• Compatible with Cat Electronic Technician (ET) and Data View• Modbus and Ethernet capable
Lube System• Air or electric motor-driven prelube• Duplex oil fi lter• RH service• Lube oil makeup system
Mounting System• Mounting plates (set of six)• Extra mounting feet (set of two)• Extra mounting plates (set of two)
Power Take-offs Front stub shafts
Starting System Air pressure reducing valve
General• Engine barring device• Dual vibration damper with guard
•
•
•
•
•
•
•
•
G3616 with ADEM A4 Gas EngineTECHNICAL DATA
Performance Number EM1426-04 EM1425-04 EM1424-04Rating °C (°F) 54 (130) 43 (110) 32 (90)Engine Power bkW (bhp) 3729 (5000) 3859 (5175) 3990 (5350)Engine Speed rpm 1000 1000 1000
Max Altitude @ Rated Torque and 38°C (100°F) m (ft) 1385 (4549) 1276 (4191) 1167 (3833)Speed Turndown @ Max Altitude, Rated Torque, and 38°C (100°F)
% 25 25 25
Aftercooler TemperatureStage 1 (JW) °C (°F) 88 (190) 88 (190) 88 (190)Stage 2 (SCAC) °C (°F) 54 (130) 43 (110) 32 (90)
Emissions (NTE)*NOx g/bkW-hr (g/bhp-hr) 0.4 (0.3) 0.4 (0.3) 0.4 (0.3)CO g/bkW-hr (g/bhp-hr) 3.35 (2.5) 3.35 (2.5) 3.35 (2.5)CO2 g/bkW-hr (g/bhp-hr) 561 (419) 561 (418) 561 (418)VOC** g/bkW-hr (g/bhp-hr) 0.36 (0.27) 0.35 (0.26) 0.34 (0.26)
Fuel Consumption ***MJ/bkW-hr (Btu/bhp-hr)
9.36 (6617) 9.33 (6598) 9.31 (6579)
Heat Balance Heat Rejection to Jacket Water bkW (Btu/min) 929 (52850) 936 (53256) 943 (53630)Heat Rejection to Oil Cooler bkW (Btu/min) 536 (30501) 559 (31771) 581 (33053)Heat Rejection to Aftercooler
Stage 1 (JW) bkW (Btu/min) 766 (43576) 798 (45368) 830 (47194)Stage 2 (SCAC) bkW (Btu/min) 204 (11603) 280 (15926) 360 (20461)
Heat Rejection to Exhaust LHV To 25°C (77°F) bkW (Btu/min) 3379 (192135) 3425 (194796) 3470 (197308)Heat Rejection to Atmosphere bkW (Btu/min) 337 (19183) 342 (19432) 343 (19497)
Exhaust System Exhaust Gas Flow Rate m3/min (scfm) 882.35 (31160) 899.73 (31774) 916.78 (32376)Exhaust Stack Temperature °C (°F) 443 (830) 438 (820) 432 (810)
Intake SystemAir Inlet Flow Rate m3/min (scfm) 343.65 (12136) 353.14 (12471) 362.62 (12806)
Gas Pressure kPag (psig) 400 - 485 (58 - 70) 400 - 485 (58 - 70) 400 - 485 (58 - 70)
All technical data is based on 100% load and speed* listed as not to exceed** Volatile organic compounds as defined in U.S. EPA 40 CFR 60, subpart JJJJ*** ISO 3046/1
To fi nd your nearest dealer, please visit: www.cat.com
Subject to change without notice. LEHW0261-01
© 2016 Caterpillar All Rights Reserved. CAT, CATERPILLAR, their respective logos, "Caterpillar Yellow" and the POWER EDGE trade dress, as well as corporate and product identity used herein, are trademarks of Caterpillar and may not be used without permission.
TECHNICAL DATA G3616 with ADEM A4 Gas Engine
DimensionsLength 5805.6 mm 228.6 inWidth 2634 mm 104 inHeight 3278 mm 129 inWeight 31,888 kg 70,301 lb
Rating Defi nitions and ConditionsEngine performance is obtained in accordance with SAE J1995, ISO3046/1, BS5514/1, and DIN6271/1 standards.
Conditions: Power for gas engines is based on fuel having an LHV of 33.74 kJ/L (905 Btu/cu ft) at 101 kPa (29.91 in Hg) and 15°C (59°F). Fuel rate is based on a cubic meter at 100 kPa (29.61 in Hg) and 15.6°C (60.1°F). Air fl ow is based on a cubic foot at 100 kPa (29.61 in Hg) and 25°C (77°F). Exhaust fl ow is based on a cubic foot at 100 kPa (29.61 in Hg) and stack temperature.
Note: General confi guration not to be used for installation
5805.6 mm228.6 in
2634 mm104 in
3278 mm129 in
For :
Catalyst Group311 Riggs Street, Bloomer, WI 54724
Tel: (715) 568-2882 • Fax: (715)568-2884E-mail : [email protected]
Via E-mail Page: 2 of 2PERFORMANCE EXPECTATION
Location : Pioneer
To Williams Our Ref. QT-117-2097-2Attn Austin Day Date: 25 May, 2017
Horsepower 5000 bhp CO 2.93 g/bhp-hr
Engine ParametersEngine Manufacturer Caterpillar Raw ExhaustEngine Model G3616 NOx 0.30 g/bhp-hr
Exhaust Flowrate 31291 acfm NMNEHC (VOC) 0.96 g/bhp-hrSpeed 1000 rpm NMHC 1.85 g/bhp-hr
Fuel Oxygen 11.10 %
Catalyst Description and Performance Expectations
Exhaust Temperature 814 ° F HCHO 0.14 g/bhp-hr
Banding CCC C-Channel Design Formulation HFX4
Warranted Performance
Substrate Type Folded Metal Foil Catalyst Dimensions 47.875 x 14.875 x 3.50"Cell Pattern 200 cpsi Herringbone Quantity Required 4 per Unit
CO 92 % ConversionNOx na % Conversion
NMNEHC (VOC) 84 % ConversionNMHC 58 % Conversion
HCHO 82 % Conversion
General Terms and Conditions of Sale and Manufacturers Warranty documents are available upon request.
This catalyst is to be installed into a converter housing produced by another manufacturer. CCC cannot verify that the housing is structurally sound and permits proper catalyst sealing. Therefore, should the catalyst not reach the catalyst outlet targets with the engine operating as listed above, then all efforts must be made to ensure that a proper catalyst seal has been obtained before questioning the performance of the catalyst.
Please contact us if you have any questions or to let us know how we can be of further help.
Best regards,
Brian WeningerMechanical Engineer, Catalyst Group
22151 East 91st Street
-Burners Broken Arrow, OK 74014 USA
-Flares Phone: 918-258-8551
-Incinerators Fax: 918-251-5519
www.zeeco.com
PRICED
Williams
Park Place Corporate Center 2
2000 Commerce Drive
Pittsburgh, PA 15275
Ph: 412-787-3132
fax:
Attention: Austin Day, Sr. Project Engr
Subject: Williams Ref.: Pioneer
Zeeco Reference: 2017-03133FL-01 -- Rev. 2
Zeeco appreciates the opportunity to propose our products to Williams.
Nikki Jenlink
Flare Application Engineer
(reach me by email at: [email protected])
July 13, 2017
Thank you for your interest in Zeeco, Inc. We look forward to the opportunity to work with you on this project. In response to your above referenced inquiry, we are pleased to provide you with our proposal for the combustion equipment designed specifically for your needs.
Zeeco's flare systems are designed to handle peak releases immediately, with no adverse effects on the flare itself or on the pilots or ignition system. Zeeco's design also offers exceptional reliability and life expectancy as well as provisions for easy maintenance and repair.
We are confident that we offer the best flaring equipment in the world at competitive prices. Should you have additional questions or require additional information, please feel free to contact us.
Best Regards,
Confidential and Proprietary
Process Conditions -- English UnitsClient: Williams Zeeco Ref.: 2017-03133FL-01 Date: 13-Jul-17Location: West Virgina Client Ref.: Pioneer Rev. 2
Pioneer Max Pioneer Min BR Max BR Min Pioneer FG BR FG
METHANE 71.47 71.47 81.34 81.34 71.61 81.19
ETHANE 17.02 17.02 11.97 11.97 17.04 12.11
PROPANE 6.67 6.67 3.64 3.64 6.67 3.69
BUTANE 2.83 2.83 1.54 1.54 2.84 1.58
PENTANE 0.87 0.87 0.50 0.50 0.87 0.51
HEXANE 0.08 0.08 0.07 0.07 0.08 0.07
HEPTANE 0.04 0.03
OCTANE 0.01 0.01
NONANE
DECANE
DODECANE
TRIDECANE
CYCLOPENTANE
ETHYLENE
PROPYLENE
BUTYLENE
ACETYLENE
BENZENE
TOLUENE
XYLENE
CARBON MONOXIDE
CARBON DIOXIDE 0.11 0.11 0.15 0.15 0.11 0.15
HYDROGEN SULFIDE
SULFUR DIOXIDE
AMMONIA
AIR
HYDROGEN
OXYGEN
NITROGEN 0.41 0.41 0.38 0.38 0.41 0.38
WATER
BUTADIENE
METHANOL
Total 99 99 100 100 100 100
Mol. Wt. 22.03 22.03 19.74 19.74 22.40 20.04
L. H. V. (BTU/SCF): 1,200 1,200 1,085 1,085 1,342 1,211.0
Temperature (Deg. F): -26.0 -73.1 -15.0
Avail. Static Pressure (psig): 35.00 35.00 35.00
Flow Rate (lbs/hr): 460,660 384,399
Smokeless Rate (lbs/hr): 460,660 384,399
Mol %
Pioneer Flare BR Flare
MJ Flare Tip
Confidential and Proprietary
Flare Tip Specification Sheet
Client: Williams Zeeco Ref.: 2017-03133FL-01 Date: 13-Jul-17Location: West Virgina Client Ref.: Rev. 2
General Information:
Tag No.: FL-7002 Pioneer
Model: MJ-16 Type: Sonic
Length: 10'- 0 ''
Weight: 1298.26444444444 lbs
No. of Pilots: 2
Design Case:
Governing Case: Pioneer Max
Molecular Weight: 22.0
L. H. V. : 1,200 BTU/SCF
Temperature: -26 Deg. F
Available Static Pressure: 35 psig
Design Flow Rate: 460,660 lbs/hr
Approximate Exit Velocity: 1129 ft/s
Mach No.: 1.00
Approx. Tip Press. Drop: 31.14 psig
Upper Section: 310 SS Windshield: NO
Lower Section: 304 SS Flame Retention Ring: n/a
Refractory: None Lifting Lugs: YES - S.S. Type
Refractory Thk: N/A
Surface Finish (Carbon Steel Surfaces):
Surface Preparation: SSPC-SP6 Primer: Inorganic Zinc
Paint (c. s. surfaces): High Heat Aluminum
Connections:
Qty. Size Type Material
N1 - Flare Gas Inlet: 1 16 '' 150# RFSO 304 SS
N2 - Pilot Gas: 1 1" 150# RFSW 304 SS
N3 - Ignition Line: 2 1 '' FNPT 304 SS
Miscellaneous Notes:
1. Includes Integral Purge Reducing Velocity Seal.
2. Required Fuel Gas Purge Rate = 760 SCFH.
Pioneer
Construction:
(Typical drawing only)
Confidential and Proprietary
Pre-Mix Flare Pilot Assembly Specification Sheet
Client: Williams Zeeco Ref.: 2017-03133FL-01 Date: 13-Jul-17Location: West Virgina Client Ref.: Rev. 2
General Information:
Tag No.: FP-1
Model: HSLF
Length: 9.135 feet
Weight: 68 lbs.
Pilot Type: Pre-Mix
Ignition Type:
Process Design Data:
Design Heat Release: 65,000 BTU/hr
Fuel Gas MW: 22.40
Fuel Gas LHV: 1,342 BTU/SCF
Fuel Gas Temperature: 100 Deg. F
Fuel Gas Inlet Pressure: 15.00 psig
Fuel Gas Flow rate: 48.4 SCFH
Design Wind Velocity: 150 mph
Design Rainfall: 50.00 inches/hr
Mounting Position: Vertical
Thermocouple Type: K Ungrounded
Construction:
Pilot Firing Tip: HK
Windshield Assembly: HK
Integral Thermowell: HK
FFG Ignition Line: 310 SS
Mounting Brackets: HK
Premix Fuel Line: 310 SS
Thermocouple Sheath: 310 SS
Thermocouple Head: 316 SS
Fuel Mixer / Spud Assembly:
Fuel Strainer Assembly: CF-8M
HEI Probe and Support: N/A
HEI Junction Head: N/A
Connections: Qty. Size Type Material
C1 - Fuel Gas Inlet: 1 1/2'' FNPT CF8M
C2 - FFG Ignition Inlet: 1 1 '' SW 310 SS
C3 - Thermocouple: 1 3/4'' Conduit Cast Iron
C4 - HEI Ignition: 0 n/a n/a n/a
Misc. Notes: (see ignition system datasheet for type applicable to this quote)
1. Upper mounting bracket is reinforced hook type for pilot removal from platform.
2. Pilot mounting brackets and thermocouple mounting brackets are investment cast assemblies.
3. Pilot mixer assembly is investment cast, high efficiency computer modeled venturi section.
4. Thermocouples are duplex fixed type. Retractable type (replaceable from grade) available upon request.
CF-3M / 18-8
High Stability
Flame Front Generator
Pioneer
Confidential and Proprietary
Client: Williams Zeeco Ref.: 2017-03133FL-01 Date: 13-Jul-17Location: West Virgina Client Ref.: Rev.: 2
General Information:
Tag No.: FL-7002 Pioneer
Overall Height: 145'- 0 ''
Design Criteria:
Wind Design Code: ASCE 7-10
Seismic Design Code: ASCE 7-10
Importance Factor: 1.25
Structural Design Code: AISC
Wind Speed (Structural): 120 mph
Seismic Zone: D
Max. Design Temperature: 150 Deg. F
Min. Design Temperature: -65 Deg. F
Design Pressure: 50 psig
Riser Corrosion Allow.: 0.000 in.
Construction:
Inner Gas Riser Material: 304 SS Ladders & Step-offs: per OSHA
Inner Gas Riser Diameter: 18" Platform at Tip: 360 deg
Outer Support Stack Material: A36CS Additional Platforms: None
Outer Support Stack Diameter:Varies Along Height (for SS Stack)
ACWL: None
Surface Finish (Carbon Steel Surfaces):
Surface Preparation: Per Spec Primer: Per Spec
Int. Coat: Per Spec Finish Paint: Per Spec
Utility Piping:
Miscellaneous Notes:
Per Attached Utility Piping Scope of Supply
Pioneer
Self-supported Flare Stack Specification Sheet
(Typical drawing only)
Confidential and Proprietary
Client: Williams Zeeco Ref.: 2017-03133FL-01 Date: 13-Jul-17Location: West Virgina Client Ref.: Rev. 2
General Information:
Tag No.: FL-7002 Pioneer
Model No.: LMC-2-DT/S
Operation: Manual/Automatic
No. of Pilots Ignited: 2
Area Classification: Class 1, Div 2, Group C&D
Fuel Gas Data:
Molecular Weight: 22.4
L. H. V.: 1,342 BTU/SCF
Temperature: 100 deg. F
Pressure: 15 psig
Utility Consumption:
Pilot Gas (Per Pilot): 48 SCFH
Pilot Gas (Total): 97 SCFH
Ignition Gas (Intermittent): 82 SCFH
Ignition Air (Intermittent): 820 SCFH
Power Available:
Ignition Line Piping: Carbon Steel Ignition Chamber: Cast Iron
Fuel Gas Piping: Carbon Steel No. Thermocouples/Pilot: 1
Mounting Rack: Carbon Steel Thermocouple Type: K
Enclosure: NEMA 4X/7 Propane Backup: No
Sun / Rain Shield: No Ignition Air PCV: YES
Pilot Gas PCV: YES Ignition Gas PCV: YES
Surface Finish (Carbon Steel Surfaces):
Surface Preparation: SSPC-SP6 First Coat:
Second Coat: Polyurethane; 1 Coat (2~3 mils) Grey - RAL7038
Connections: Qty. Size
N1 - Instrument Air Inlet: 1 3/4''
N2 - Pilot Gas Inlet: 1 1/2''
N3 - Ignition Gas Outlet: 2 1 ''
Pilot Gas Out. (Not Shown): 1 1/2''
Miscellaneous Notes:
1. Zeeco has considered relay logic. PLC can be considered upon request.
2. Piping/valves/instruments shall be CS w/ SW connections
Construction:
150# RFSW
Type
3000# Thrd. Union
Material
Galvanized C.S.
Finish Color:
Carbon Steel
Carbon Steel
150# RFSW
150# RFSW
Carbon Steel
120 Volt, 1 Phase, 60 Hertz
Pioneer
Flame Front Generator Specification Sheet
(Typical drawing only)
High Build Epoxy; 1 Coat (4~6 mils)
Confidential and Proprietary
CHARACTERISTIC SPECIFICATION
ELECTRICAL PERFORMANCE*
FLEX TURBINE® GT1300S
FlexEnergy 1.3 Megawatt Highly E�cient Ultra Low Emission Power Package
Electrical e�ciency
Electrical power
33% LHV
1300 kW
* At ISO Conditions (59°F [15°C], sea level, 60% RH); high pressure natural gasElectrical e�ciency tolerance: +1/-2.5 ptsElectrical power tolerance: ± 50kWElevation derate of approximately 3.5% per 1000 ft (305 m)
Nominal Heat Rate (LHV)
Nominal Heat Rate (HHV)
10,490 Btu/kWh (11.1 MJ/kWh)
11,540 Btu/kWh (12.1 MJ/kWh)
Voltage
Frequency
480 VAC / 400 VAC
60 Hz / 50 Hz
Type of Service 3 phase, wye, 4 wire
HEAT RECOVERY*CHARACTERISTIC SPECIFICATION
Exhaust temp 507°F (264°C)
19.8 lb/s (9.2 kg/s)
* At ISO conditions; four drivetrains operating at full powerAvailable heat based on exhaust recovery down to 59°F (15°C)
Engine air �ow 15,560 scfm (25,000 Nm3/h)
7.6 MMBtu/h (2,224 kW)Max available heat
FUEL REQUIREMENTS*
CHARACTERISTIC SPECIFICATION
Inlet pressure 75 to 140 psig (517 to 965 kPag)
325 to 1900 WI Btu/ft3
12.1 to 70.7 WI MJ/m3
* Consumption at ISO conditions; four drivetrains operating at full powerWI - Wobbe Index Lower heating value (LHV)
Fuel Consumption (LHV) 13.6 MMBtu/h (3,996 kW)
Acceptable Fuel Range (LHV)
©2016 FlexEnergy Inc. and/or its a�liates (“FlexEnergy”). This document comprises a general overview of the products or services described herein. It is solely for informational purposes, does not represent a warranty of the information constrained herein and is not to be construed as an o�er to sell or solicitation to buy. Contact FlexEnergy for detailed product, design, and engineering information suitable to your speci�c applications. FlexEnergy reserves the right to modify its products and related product information at any time without prior notice.
PHYSICAL SPECIFICATIONS
TurbinePackage
WIDTH LENGTH HEIGHT WEIGHT
96 in 480 in 124 in 48,000 lb 244 cm 1219 cm 315 cm 21,818 kg
GBR - One perDrivetrain
43 in 63 in 21 in 595 lb 110 cm 160 cm 78 cm 270 kg
Ambient Temperature Range -20° to 115°F (-29° to 46°C)
69 dB(A) @ 10 mTurbine PackageGBRs
SOUND LEVELS
65 dB(A) @ 10 m
EMISSIONS AT 100% LOAD*NOx <9 ppmv @ 15% O2CO <9 ppmv @ 15% O2VOC <9 ppmv @ 15% O2* Pipeline natural gas only at ISO conditions
www.flexenergy.com
• High electrical efficiency over a wideoperating range
• Part load redundancy and demand responsecontrol
• Built with the same proven technology as the GT333S
• Integrated Utility synchronization andprotection
• Remote Monitoring and FlexCare fixedmaintenance plans available
0%
5%
10%
15%
20%
25%
30%
35%
0 163 325 488 650 813 975 1,138 1,300
LHV
E�ci
ency
Power Output (kW)
GT1300S Part Load E�cieny
Typical Turbine E�ciency
July 20, 2017 Williams - NE G&P 2000 Commerce Drive Pittsburgh, PA 15275 Attention: Ignacio Russo [email protected] Reference: Pioneer and Blake Ridge Thermal Oxidizers Zeeco Proposal No. 2017-02645IN-01 Rev 4 Dear Mr. Russo: Thank you for your inquiry. We appreciate this opportunity to provide our revised proposal to include Waste Stream 5 & 6 as shown in the updated process data provided on July 18, 2017, for the following equipment:
Two (2) Zeeco Standard, Direct Fired Horizontal Thermal Oxidizer Packages The attached proposal describes specific features and performance of Zeeco’s standard thermal oxidizer system. Our design incorporates a proven thermal process to effectively treat the waste gas stream from your process. The design and materials of construction have been chosen to maximize on-line time and operational life. Please note that the base of the thermal oxidizer is mounted on a pre-wired and pre-piped rectangular structural steel skid that will also house the fuel rack and control panel. This is intended to reduce installation time associated with interconnecting piping and wiring between the fuel rack/control panel and the thermal oxidizer. Furthermore, the unit is NFPA 86 compliant to ensure personnel and equipment safety. Again, we appreciate the opportunity to quote on your combustion equipment requirements. After you have had an opportunity to review our proposal, should you have any questions or require additional information, please contact me at (918)893-8416 or email me at [email protected]. Best regards,
Sydney Levine Applications Engineer Cc: Ryan B. Tate, Zeeco- Broken Arrow
4.0 DESIGN BASIS
4.1 Site Conditions
Elevation, feet Blake Ridge: 1,450 Pioneer: 1,250
Barometric Pressure, psia 13.9
Temperature, oF (Min/Max) -20* / 100
Design Relative Humidity 90% (assumed)
Wind Design ASCE 7-10, 120MPH
*Note: The Thermal Oxidizer package is acceptable to -20°F with the exception of the HMI, which is guaranteed to 32°F.
4.2 Waste Stream Summary
PIONEER
Waste Gas 1
Waste Gas 2
Waste Gas 3
Waste Gas 4
Waste Gas 5
Waste Gas 6
Mol % Mol % Mol % Mol % Mol % Mol %
Water 85.80192 85.80192 0.1649743 0.1649743 0 0
TEG 0.0001174 0.0001174 0.0001382 0.0001382 0 0
Nitrogen 0.00054 0.00054 0.0896987 0.0896987 0 0
Methane 1.3688041 1.3688041 51.344687 51.344687 0 0
CO2 0.1482647 0.1482647 0.5000099 0.5000099 0 0
Ethane 2.7699719 2.7699719 26.727424 26.727424 0 0
Propane 2.8329436 2.8329436 13.104553 13.104553 20.986107 20.983331
i-Butane 0.3045151 0.3045151 1.1240846 1.1240846 11.165111 11.16968
n-Butane 1.7903509 1.7903509 4.4060352 4.4060352 41.265849 41.265083
i-Pentane 0.4968271 0.4968271 0.6435775 0.6435775 6.8906596 6.891371
n-Pentane 1.0508567 1.0508567 1.1111151 1.1111151 10.954713 10.953998
2,3-Dimethylbutane 0.3533435 0.3533435 0.2251448 0.2251448 2.4705339 2.4699713
3-Methylpentane 0.2620526 0.2620526 0.1449929 0.1449929 1.5553963 1.5556149
Hexane 0.2724999 0.2724999 0.1442947 0.1442947 1.7404499 1.7402445
2,2-Dimethylpentane 0.0025424 0.0025424 0.0011917 0.0011917 0.0151192 0.0151176
Methylcyclopentane 0.1080608 0.1080608 0.0169657 0.0169657 0.1282144 0.1282291
Benzene 0.1038125 0.1038125 0.0027162 0.0027162 0.0118769 0.0118758
3,3-Dimethylpentane 0.0034755 0.0034755 0.0010277 0.0010277 0.0124009 0.0124003
Cyclohexane 0.131173 0.131173 0.0224721 0.0224721 0.167149 0.1671086
2-Methylhexane 0.1065749 0.1065749 0.0363433 0.0363433 0.1272613 0.127264
2,3-Dimethylpentane 0.0047007 0.0047007 0.0012513 0.0012513 0.0152063 0.0152027
3-Methylhexane 0.1157544 0.1157544 0.0319648 0.0319648 0.4129168 0.4128873
Heptane 0.2365455 0.2365455 0.0588878 0.0588878 0.8027164 0.8024295
Toluene 0.4661113 0.4661113 0.0063571 0.0063571 0.0374895 0.0374861
Octane 0.0781148 0.0781148 0.0112213 0.0112213 0.1909147 0.1908976
Ethylbenzene 0.2614509 0.2614509 0.0023632 0.0023632 0.021013 0.021008
o-Xylene 0.0583867 0.0583867 0.0003829 0.0003829 0.002905 0.0029045
2-Methylheptane 0.0569704 0.0569704 0.0108261 0.0108261 0.1766993 0.1767202
Methylcyclohexane 0.2703071 0.2703071 0.0339189 0.0339189 0.3790713 0.3790206
2,5-Dimethylhexane 0.0086627 0.0086627 0.0024037 0.0024037 0.0391255 0.0391205
1,t-3-Dimethylcyclohexane 0.0103362 0.0103362 0.0007206 0.0007206 0.0109802 0.0109802
Nonane 0.024489 0.024489 0.0018243 0.0018243 0.043396 0.0433819
n-Undecane 0.000775 0.000775 1.57E-05 1.57E-05 5.70E-04 5.70E-04
n-Decane 0.0060499 0.0060499 0.0002399 0.0002399 0.0076207 0.007618
Dodecane 0.0001128 0.0001128 1.19E-06 1.19E-06 5.64E-05 5.64E-05
Tridecane 1.54E-05 1.54E-05 9.25E-08 9.25E-08 5.43E-06 5.42E-06
Tetradecane 1.82E-06 1.82E-06 7.74E-09 7.74E-09 5.72E-07 5.73E-07
Pentadecane 4.66E-07 4.66E-07 1.65E-09 1.65E-09 1.56E-07 1.56E-07
Hexadecane 3.63E-07 3.63E-07 1.22E-09 1.22E-09 1.24E-07 1.24E-07
Heptadecane 7.27E-08 7.27E-08 2.40E-10 2.40E-10 2.76E-08 2.76E-08
Octadecane 2.96E-08 2.96E-08 8.59E-11 8.59E-11 1.08E-08 1.08E-08
Nonadecane 7.95E-09 7.95E-09 1.99E-11 1.99E-11 2.49E-09 2.50E-09
Eicosane 2.53E-09 2.53E-09 4.46E-12 4.46E-12 9.04E-10 9.05E-10
C21 2.31E-09 2.31E-09 4.13E-12 4.13E-12 1.05E-09 1.05E-09
C22 2.03E-09 2.03E-09 3.57E-12 3.57E-12 8.08E-10 8.08E-10
C23 8.64E-10 8.64E-10 1.47E-12 1.47E-12 4.00E-10 4.00E-10
C24 1.92E-11 1.92E-11 0 0 2.17E-11 2.17E-11
m-Xylene 0.1335432 0.1335432 0.0011677 0.0011677 0.0139191 0.0139206
p-Xylene 0.1275405 0.1275405 0.0012043 0.0012043 0.0102296 0.0102275
2,2,4-Trimethylpentane 0.0100727 0.0100727 0.002629 0.002629 0.0369041 0.0368986
2,4-Dimethylpentane 0.0009178 0.0009178 0.0004242 0.0004242 0.0055755 0.0055764
3-Ethylpentane 0.0196507 0.0196507 0.0046713 0.0046713 0.057195 0.0571814
2,4-Dimethylhexane 0.0104157 0.0104157 0.0025313 0.0025313 0.0382339 0.0382293
trans-1,2-Dimethylcyclohexane 0.1165761 0.1165761 0.0088281 0.0088281 0.1352164 0.135206
cis-1,2-Dimethylcyclohexane 0.0566796 0.0566796 0.0032722 0.0032722 0.0511976 0.0511875
cis-1,3-Dimethylcyclohexane 0.0171711 0.0171711 0.0014461 0.0014461 0.0199998 0.0199939
PRESSURE 0.1 psig 0.1 psig 57 psig 57 psig 1 psig 1 psig
TEMPERATURE 205 F 205 F 108 F 108 F 100 F 100 F
MW 23.5 23.5 27.6 27.6 60.6 60.6
FLOW RATE 230 lb/hr 230 lb/hr 104 lb/hr 104 lb/hr 23 lb/hr 3 lb/hr
BLAKE RIDGE
Waste Gas 1
Waste Gas 2
Waste Gas 3
Waste Gas 4
Waste Gas 5
Waste Gas 6
Mol % Mol % Mol % Mol % Mol % Mol %
Water 90.708664 90.708664 0.2017609 0.2017609 0 0
TEG 0.0001122 0.0001122 0.0001397 0.0001397 0 0
Nitrogen 0.0004032 0.0004032 0.0852151 0.0852151 0 0
Methane 1.3278677 1.3278677 63.75814 63.75814 0 0
CO2 0.163891 0.163891 0.7111178 0.7111178 0 0
Ethane 1.7101505 1.7101505 21.237356 21.237356 0 0
Propane 1.396036 1.396036 8.3472711 8.3472711 38.323047 38.323876
i-Butane 0.2289641 0.2289641 1.0938283 1.0938283 12.777954 12.779927
n-Butane 0.7701528 0.7701528 2.4546063 2.4546063 26.131425 26.134075
i-Pentane 0.363147 0.363147 0.6120734 0.6120734 6.9368491 6.9331473
n-Pentane 0.4541709 0.4541709 0.6269606 0.6269606 6.4849562 6.481844
2,3-Dimethylbutane 0.3026362 0.3026362 0.2514102 0.2514102 2.7623678 2.7629963
3-Methylpentane 0.2249217 0.2249217 0.1619479 0.1619479 1.7231632 1.7234484
Hexane 0.2326474 0.2326474 0.1614611 0.1614611 1.8912048 1.8915898
2,2-Dimethylpentane 0.0021887 0.0021887 0.0013412 0.0013412 0.0160914 0.0160933
Methylcyclopentane 0.089903 0.089903 0.0185289 0.0185289 0.1400683 0.1401048
Benzene 0.0844365 0.0844365 0.0028887 0.0028887 0.0131832 0.0131829
3,3-Dimethylpentane 0.0029518 0.0029518 0.0011436 0.0011436 0.0130236 0.0130266
Cyclohexane 0.107881 0.107881 0.0241539 0.0241539 0.18067 0.1806805
2-Methylhexane 0.0909396 0.0909396 0.0406738 0.0406738 0.1313767 0.1314031
2,3-Dimethylpentane 0.003982 0.003982 0.0013899 0.0013899 0.0157618 0.0157643
3-Methylhexane 0.0980455 0.0980455 0.0355655 0.0355655 0.4234141 0.4236583
Heptane 0.199117 0.199117 0.0652781 0.0652781 0.8041488 0.803854
Toluene 0.3817306 0.3817306 0.0068002 0.0068002 0.0378072 0.0378085
Octane 0.0655045 0.0655045 0.0124363 0.0124363 0.1754799 0.1754847
Ethylbenzene 0.2156914 0.2156914 0.0025333 0.0025333 0.0193993 0.0193989
o-Xylene 0.0487716 0.0487716 0.0004097 0.0004097 0.0026479 0.002648
2-Methylheptane 0.0482573 0.0482573 0.0120698 0.0120698 0.1662129 0.1662205
Methylcyclohexane 0.2229197 0.2229197 0.0366772 0.0366772 0.3825573 0.3825713
2,5-Dimethylhexane 0.0073056 0.0073056 0.002683 0.002683 0.0378094 0.0378049
1,t-3-Dimethylcyclohexane 0.0085951 0.0085951 0.0007932 0.0007932 0.0102749 0.0102757
Nonane 0.0216021 0.0216021 0.0021341 0.0021341 0.0377681 0.0377642
n-Undecane 0.0007895 0.0007895 2.13E-05 2.13E-05 4.84E-04 4.84E-04
n-Decane 0.0056354 0.0056354 0.0002983 0.0002983 0.0065143 0.0065136
Dodecane 0.0001279 0.0001279 1.79E-06 1.79E-06 4.80E-05 4.80E-05
Tridecane 1.94E-05 1.94E-05 1.51E-07 1.51E-07 4.62E-06 4.61E-06
Tetradecane 2.67E-06 2.67E-06 1.38E-08 1.38E-08 4.87E-07 4.86E-07
Pentadecane 7.98E-07 7.98E-07 3.16E-09 3.16E-09 1.32E-07 1.32E-07
Hexadecane 7.03E-07 7.03E-07 2.55E-09 2.55E-09 1.05E-07 1.05E-07
Heptadecane 1.56E-07 1.56E-07 5.45E-10 5.45E-10 2.34E-08 2.34E-08
Octadecane 6.79E-08 6.79E-08 2.09E-10 2.09E-10 9.12E-09 9.12E-09
Nonadecane 1.99E-08 1.99E-08 5.22E-11 5.22E-11 2.13E-09 2.12E-09
Eicosane 6.78E-09 6.78E-09 1.24E-11 1.24E-11 7.67E-10 7.68E-10
C21 6.60E-09 6.60E-09 1.20E-11 1.20E-11 8.88E-10 8.88E-10
C22 6.16E-09 6.16E-09 1.06E-11 1.06E-11 6.86E-10 6.85E-10
C23 2.49E-09 2.49E-09 3.87E-12 3.87E-12 3.39E-10 3.40E-10
C24 4.45E-11 4.45E-11 7.76E-14 7.76E-14 1.85E-11 1.85E-11
m-Xylene 0.1106692 0.1106692 0.0012565 0.0012565 0.0127826 0.0127818
p-Xylene 0.1057971 0.1057971 0.0012974 0.0012974 0.0094165 0.0094196
2,2,4-Trimethylpentane 0.0086311 0.0086311 0.002963 0.002963 0.0370198 0.037021
2,4-Dimethylpentane 0.0007906 0.0007906 0.0004778 0.0004778 0.0058991 0.0058979
3-Ethylpentane 0.0165798 0.0165798 0.0051684 0.0051684 0.0585258 0.0585323
2,4-Dimethylhexane 0.0087772 0.0087772 0.0028154 0.0028154 0.0371051 0.0370923
trans-1,2-Dimethylcyclohexane 0.0971593 0.0971593 0.0097175 0.0097175 0.1272388 0.1272405
cis-1,2-Dimethylcyclohexane 0.0471172 0.0471172 0.0036043 0.0036043 0.0473183 0.0473343
cis-1,3-Dimethylcyclohexane 0.0143137 0.0143137 0.0015894 0.0015894 0.0189802 0.0189809
PRESSURE 0.1 psig 0.1 psig 57 psig 57 psig 1 psig 1 psig
TEMPERATURE 205 F 205 F 108 F 108 F 100 F 100 F
MW 23.7 23.7 24.6 24.6 57.7 57.7
FLOW RATE 267 lb/hr 267 lb/hr 108 lb/hr 108 lb/hr 30 lb/hr 3.3 lb/hr
Waste streams for both locations are assumed to be in vapor phase, no liquid has been considered within this design. For both locations, it has been assumed that Waste Streams 1 and 2 are together in one pipe coming to the thermal oxidizer, Waste 3 and 4 are in together in one pipe and Wastes 5 & 6 are combined into one pipe.
4.3 Utilities
Electrical Power 460V / 3 Phase / 60 Hz
Instrument Air, SCFH 2000
Maximum Fuel Gas Required, MMBtu/Hr
1
4.4 Flue Gas Summary
PIONEER at 1800F Operating Temperature
Waste Gas 1, 2, 3, 4, 5 & 6
Waste Gas 1, 2, 3, 4 & 6
Waste Gas 1, 3, 5 & 6
Waste Gas 1, 3 & 6
Mol % Mol % Mol % Mol %
Carbon Dioxide 4.81 4.81 4.84 4.82
Water 15.89 16.06 15.64 15.92
Nitrogen 69.17 69.05 69.41 69.22
Oxygen 10.12 10.08 10.11 10.04
Total, lb/hr 16,972 16,079 9,858 8,976
Mol. Wt. 27.6 27.6 27.6 27.6
BLAKE RIDGE at 1800F Operating Temperature
Waste Gas 1, 2, 3, 4, 5 & 6
Waste Gas 1, 2, 3, 4 & 6
Waste Gas 1, 3, 5 & 6
Waste Gas 1, 3 & 6
Mol % Mol % Mol % Mol %
Carbon Dioxide 4.76 4.75 4.78 4.75
Water 16.97 17.28 16.53 17.02
Nitrogen 68.38 68.16 68.77 68.42
Oxygen 9.89 9.81 9.92 9.80
Total, lb/hr 16,480 15,313 9,755 8,601
Mol. Wt. 27.5 27.4 27.5 27.5
4.5 System Performance
Stack Parameter Guaranteed Values
VOC Destruction Efficiency 99.5 %
These values are understood to apply only when the system is operated in accordance with the operating conditions stipulated in the design summary and for the waste(s) stipulated in the design basis sections of this proposal.
Appalachia Midstream Services, LLC (AMS) Threedubs Compressor Station (3WCS) Application for G35-D General Permit Registration
Appendix S5
Emission Programs
• GRI-GLYCalc – TEG Dehydrator (DHY - DFT and DSV)
• EPA TANKS 4.0.9d – Stabilized Condensate Tanks (TK-01 thru TK-06)
• EPA TANKS 4.0.9d – Produced Water Storage Tanks (TK-07 and TK-08)
Page: 1GRI-GLYCalc VERSION 4.0 - SUMMARY OF INPUT VALUES
Case Name: 3WCS-G35-D Gen Permit-S5-200.0 MMscfd Dehy-041618File Name: C:\Users\Clyde\Documents\Documents\04.16 - Ecologic\07 - AMS - ThreedubsCS\3WCS-G35-D-Gen Permit-O-200 MMscfd Dehy-041618.ddf Date: April 15, 2018
DESCRIPTION: -------------------------------------------------------------------
Description: Wet Gas: 80 oF, 1000 psigPump: Electric, 24.0 gpmFlash Tank: 110.0 oF, 60 psigFlash Tank/Still Vent Controlled by 98% T-Ox
Annual Hours of Operation: 8760.0 hours/yr
WET GAS: -------------------------------------------------------------------
Temperature: 80.00 deg. F Pressure: 1000.00 psig
Wet Gas Water Content: Saturated
Component Conc. (vol %)
------------------------------- -----------Carbon Dioxide 0.1098
Nitrogen 0.4144Methane 71.6162Ethane 17.0404Propane 6.6780
Isobutane 0.6673n-Butane 2.1619
Isopentane 0.3376n-Pentane 0.5333n-Hexane 0.0796
Cyclohexane 0.0162Other Hexanes 0.1863
Heptanes 0.0934Methylcyclohexane 0.0191
2,2,4-Trimethylpentane 0.0018
Benzene 0.0008Toluene 0.0024
Ethylbenzene 0.0013Xylenes 0.0016
C8+ Heavies 0.0386
DRY GAS: -------------------------------------------------------------------
Flow Rate: 200.0 MMSCF/dayWater Content: 7.0 lbs. H2O/MMSCF
LEAN GLYCOL: -------------------------------------------------------------------
Glycol Type: TEGWater Content: 1.5 wt% H2O
Flow Rate: 24.0 gpm
Page: 2 PUMP: -------------------------------------------------------------------
Glycol Pump Type: Electric/Pneumatic
FLASH TANK: -------------------------------------------------------------------
Flash Control: Combustion device Flash Control Efficiency: 98.00 % Temperature: 110.0 deg. F Pressure: 60.0 psig
REGENERATOR OVERHEADS CONTROL DEVICE: -------------------------------------------------------------------
Control Device: Combustion Device Destruction Efficiency: 98.0 % Excess Oxygen: 5.0 % Ambient Air Temperature: 50.0 deg. F
Page: 1GRI-GLYCalc VERSION 4.0 - AGGREGATE CALCULATIONS REPORT
Case Name: 3WCS-G35-D Gen Permit-S5-200.0 MMscfd Dehy-041618File Name: C:\Users\Clyde\Documents\Documents\04.16 - Ecologic\07 - AMS - ThreedubsCS\3WCS-G35-D-Gen Permit-O-200 MMscfd Dehy-041618.ddf Date: April 15, 2018
DESCRIPTION:
Description: Wet Gas: 80 oF, 1000 psigPump: Electric, 24.0 gpmFlash Tank: 110.0 oF, 60 psigFlash Tank/Still Vent Controlled by 98% T-Ox
Annual Hours of Operation: 8760.0 hours/yr
EMISSIONS REPORTS: -------------------------------------------------------------------
CONTROLLED REGENERATOR EMISSIONS -------------------------------------------------------------------
Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- -----------
Methane 0.0373 0.894 0.1632Ethane 0.1471 3.531 0.6444Propane 0.2151 5.162 0.9420
Isobutane 0.0472 1.133 0.2068n-Butane 0.2337 5.609 1.0236
Isopentane 0.0441 1.058 0.1931n-Pentane 0.0995 2.389 0.4359n-Hexane 0.0311 0.746 0.1361
Cyclohexane 0.0370 0.888 0.1621Other Hexanes 0.0520 1.247 0.2276
Heptanes 0.0808 1.940 0.3540Methylcyclohexane 0.0503 1.208 0.2205
2,2,4-Trimethylpentane 0.0006 0.015 0.0027Benzene 0.0187 0.448 0.0818Toluene 0.0841 2.018 0.3683
Ethylbenzene 0.0604 1.449 0.2644Xylenes 0.1035 2.485 0.4535
C8+ Heavies 0.0709 1.702 0.3106 ------------------------------- ----------- ----------- -----------
Total Emissions 1.4134 33.921 6.1907
Total Hydrocarbon Emissions 1.4134 33.921 6.1907Total VOC Emissions 1.2290 29.496 5.3830Total HAP Emissions 0.2984 7.160 1.3068Total BTEX Emissions 0.2667 6.400 1.1680
UNCONTROLLED REGENERATOR EMISSIONS -------------------------------------------------------------------
Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- -----------
Methane 1.8633 44.720 8.1614Ethane 7.3560 176.545 32.2195Propane 10.7537 258.089 47.1012
Isobutane 2.3606 56.653 10.3392n-Butane 11.6848 280.435 51.1793
Isopentane 2.2043 52.903 9.6548n-Pentane 4.9761 119.427 21.7954
Page: 2 n-Hexane 1.5540 37.296 6.8065 Cyclohexane 1.8509 44.421 8.1069 Other Hexanes 2.5985 62.363 11.3813
Heptanes 4.0413 96.991 17.7009 Methylcyclohexane 2.5168 60.402 11.0234 2,2,4-Trimethylpentane 0.0306 0.733 0.1338 Benzene 0.9338 22.411 4.0901 Toluene 4.2043 100.904 18.4150
Ethylbenzene 3.0185 72.444 13.2211 Xylenes 5.1764 124.233 22.6726 C8+ Heavies 3.5458 85.100 15.5307 ------------------------------- ----------- ----------- ----------- Total Emissions 70.6696 1696.071 309.5330
Total Hydrocarbon Emissions 70.6696 1696.071 309.5330 Total VOC Emissions 61.4503 1474.806 269.1521 Total HAP Emissions 14.9176 358.022 65.3390 Total BTEX Emissions 13.3330 319.993 58.3987
FLASH GAS EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 0.6637 15.929 2.9070 Ethane 0.7042 16.901 3.0845 Propane 0.4617 11.081 2.0224 Isobutane 0.0644 1.546 0.2822 n-Butane 0.2386 5.727 1.0452
Isopentane 0.0381 0.915 0.1670 n-Pentane 0.0676 1.622 0.2960 n-Hexane 0.0112 0.269 0.0491 Cyclohexane 0.0033 0.079 0.0145 Other Hexanes 0.0252 0.604 0.1102
Heptanes 0.0136 0.326 0.0595 Methylcyclohexane 0.0034 0.082 0.0149 2,2,4-Trimethylpentane 0.0002 0.005 0.0009 Benzene 0.0002 0.005 0.0009 Toluene 0.0006 0.014 0.0026
Ethylbenzene 0.0002 0.006 0.0010 Xylenes 0.0003 0.007 0.0012 C8+ Heavies 0.0011 0.025 0.0046 ------------------------------- ----------- ----------- ----------- Total Emissions 2.2976 55.143 10.0637
Total Hydrocarbon Emissions 2.2976 55.143 10.0637 Total VOC Emissions 0.9297 22.314 4.0722 Total HAP Emissions 0.0127 0.306 0.0558 Total BTEX Emissions 0.0013 0.031 0.0057
FLASH TANK OFF GAS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 33.1846 796.431 145.3486 Ethane 35.2108 845.059 154.2233 Propane 23.0862 554.069 101.1175 Isobutane 3.2216 77.318 14.1105 n-Butane 11.9309 286.343 52.2575
Isopentane 1.9066 45.758 8.3508 n-Pentane 3.3789 81.095 14.7998
Page: 3 n-Hexane 0.5610 13.464 2.4572 Cyclohexane 0.1655 3.973 0.7251 Other Hexanes 1.2578 30.187 5.5091
Heptanes 0.6791 16.299 2.9747 Methylcyclohexane 0.1699 4.077 0.7441 2,2,4-Trimethylpentane 0.0105 0.253 0.0461 Benzene 0.0106 0.255 0.0466 Toluene 0.0295 0.709 0.1294
Ethylbenzene 0.0117 0.282 0.0514 Xylenes 0.0137 0.328 0.0599 C8+ Heavies 0.0530 1.271 0.2320 ------------------------------- ----------- ----------- ----------- Total Emissions 114.8821 2757.171 503.1837
Total Hydrocarbon Emissions 114.8821 2757.171 503.1837 Total VOC Emissions 46.4867 1115.681 203.6117 Total HAP Emissions 0.6371 15.291 2.7906 Total BTEX Emissions 0.0656 1.574 0.2873
COMBINED REGENERATOR VENT/FLASH GAS EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 0.7010 16.823 3.0702 Ethane 0.8513 20.432 3.7289 Propane 0.6768 16.243 2.9644 Isobutane 0.1116 2.679 0.4890 n-Butane 0.4723 11.336 2.0687
Isopentane 0.0822 1.973 0.3601 n-Pentane 0.1671 4.010 0.7319 n-Hexane 0.0423 1.015 0.1853 Cyclohexane 0.0403 0.968 0.1766 Other Hexanes 0.0771 1.851 0.3378
Heptanes 0.0944 2.266 0.4135 Methylcyclohexane 0.0537 1.290 0.2353 2,2,4-Trimethylpentane 0.0008 0.020 0.0036 Benzene 0.0189 0.453 0.0827 Toluene 0.0847 2.032 0.3709
Ethylbenzene 0.0606 1.455 0.2655 Xylenes 0.1038 2.491 0.4546 C8+ Heavies 0.0720 1.727 0.3153 ------------------------------- ----------- ----------- ----------- Total Emissions 3.7110 89.065 16.2543
Total Hydrocarbon Emissions 3.7110 89.065 16.2543 Total VOC Emissions 2.1587 51.810 9.4553 Total HAP Emissions 0.3111 7.466 1.3626 Total BTEX Emissions 0.2680 6.431 1.1737
COMBINED REGENERATOR VENT/FLASH GAS EMISSION CONTROL REPORT: -------------------------------------------------------------------
Component Uncontrolled Controlled % Reduction tons/yr tons/yr ------------------------------- ------------ ------------ ------------ Methane 153.5100 3.0702 98.00 Ethane 186.4428 3.7289 98.00 Propane 148.2187 2.9644 98.00 Isobutane 24.4497 0.4890 98.00 n-Butane 103.4369 2.0687 98.00
Page: 4
Isopentane 18.0056 0.3601 98.00 n-Pentane 36.5952 0.7319 98.00 n-Hexane 9.2637 0.1853 98.00 Cyclohexane 8.8319 0.1766 98.00 Other Hexanes 16.8904 0.3378 98.00
Heptanes 20.6756 0.4135 98.00 Methylcyclohexane 11.7675 0.2353 98.00 2,2,4-Trimethylpentane 0.1799 0.0036 98.00 Benzene 4.1367 0.0827 98.00 Toluene 18.5444 0.3709 98.00
Ethylbenzene 13.2725 0.2655 98.00 Xylenes 22.7325 0.4546 98.00 C8+ Heavies 15.7627 0.3153 98.00 ------------------------------- ------------ ------------ ------------ Total Emissions 812.7166 16.2543 98.00
Total Hydrocarbon Emissions 812.7166 16.2543 98.00 Total VOC Emissions 472.7639 9.4553 98.00 Total HAP Emissions 68.1296 1.3626 98.00 Total BTEX Emissions 58.6860 1.1737 98.00
EQUIPMENT REPORTS: -------------------------------------------------------------------
COMBUSTION DEVICE -------------------------------------------------------------------
Ambient Temperature: 50.00 deg. F Excess Oxygen: 5.00 % Combustion Efficiency: 98.00 % Supplemental Fuel Requirement: 3.95e-001 MM BTU/hr
Component Emitted Destroyed ------------------------------- ----------- ----------- Methane 2.00% 98.00% Ethane 2.00% 98.00% Propane 2.00% 98.00% Isobutane 2.00% 98.00% n-Butane 2.00% 98.00%
Isopentane 2.00% 98.00% n-Pentane 2.00% 98.00% n-Hexane 2.00% 98.00% Cyclohexane 2.00% 98.00% Other Hexanes 2.00% 98.00%
Heptanes 2.00% 98.00% Methylcyclohexane 2.00% 98.00% 2,2,4-Trimethylpentane 2.00% 98.00% Benzene 2.00% 98.00% Toluene 2.00% 98.00%
Ethylbenzene 2.00% 98.00% Xylenes 2.00% 98.00% C8+ Heavies 2.00% 98.00%
ABSORBER -------------------------------------------------------------------
Page: 5NOTE: Because the Calculated Absorber Stages was below the minimumallowed, GRI-GLYCalc has set the number of Absorber Stages to 1.25and has calculated a revised Dry Gas Dew Point.
Calculated Absorber Stages: 1.25 Calculated Dry Gas Dew Point: 1.59 lbs. H2O/MMSCF
Temperature: 80.0 deg. F Pressure: 1000.0 psig Dry Gas Flow Rate: 200.0000 MMSCF/day Glycol Losses with Dry Gas: 3.8589 lb/hr Wet Gas Water Content: Saturated Calculated Wet Gas Water Content: 32.36 lbs. H2O/MMSCF Calculated Lean Glycol Recirc. Ratio: 5.61 gal/lb H2O
Remaining Absorbed Component in Dry Gas in Glycol ------------------------------- ----------- ----------- Water 4.90% 95.10% Carbon Dioxide 99.81% 0.19% Nitrogen 99.98% 0.02% Methane 99.99% 0.01% Ethane 99.96% 0.04%
Propane 99.95% 0.05% Isobutane 99.93% 0.07% n-Butane 99.91% 0.09% Isopentane 99.92% 0.08% n-Pentane 99.90% 0.10%
n-Hexane 99.86% 0.14% Cyclohexane 99.33% 0.67% Other Hexanes 99.89% 0.11% Heptanes 99.77% 0.23% Methylcyclohexane 99.35% 0.65%
2,2,4-Trimethylpentane 99.91% 0.09% Benzene 93.12% 6.88% Toluene 91.28% 8.72% Ethylbenzene 90.00% 10.00% Xylenes 86.09% 13.91%
C8+ Heavies 99.75% 0.25%
FLASH TANK -------------------------------------------------------------------
Flash Control: Combustion device Flash Control Efficiency: 98.00 % Flash Temperature: 110.0 deg. F Flash Pressure: 60.0 psig
Left in Removed in Component Glycol Flash Gas ------------------------------- ----------- ----------- Water 99.98% 0.02% Carbon Dioxide 43.07% 56.93% Nitrogen 5.14% 94.86% Methane 5.32% 94.68% Ethane 17.28% 82.72%
Propane 31.78% 68.22% Isobutane 42.29% 57.71% n-Butane 49.48% 50.52% Isopentane 53.85% 46.15% n-Pentane 59.76% 40.24%
n-Hexane 73.61% 26.39%
Page: 6Cyclohexane 92.05% 7.95%
Other Hexanes 67.71% 32.29%Heptanes 85.68% 14.32%
Methylcyclohexane 93.93% 6.07%
2,2,4-Trimethylpentane 74.75% 25.25%Benzene 98.93% 1.07%Toluene 99.36% 0.64%
Ethylbenzene 99.65% 0.35%Xylenes 99.77% 0.23%
C8+ Heavies 98.70% 1.30%
REGENERATOR -------------------------------------------------------------------
No Stripping Gas used in regenerator.
Remaining Distilled Component in Glycol Overhead
------------------------------- ----------- -----------Water 44.12% 55.88%
Carbon Dioxide 0.00% 100.00%Nitrogen 0.00% 100.00%Methane 0.00% 100.00%Ethane 0.00% 100.00%
Propane 0.00% 100.00%Isobutane 0.00% 100.00%n-Butane 0.00% 100.00%
Isopentane 0.93% 99.07%n-Pentane 0.84% 99.16%
n-Hexane 0.68% 99.32%Cyclohexane 3.48% 96.52%
Other Hexanes 1.48% 98.52%Heptanes 0.58% 99.42%
Methylcyclohexane 4.26% 95.74%
2,2,4-Trimethylpentane 2.01% 97.99%Benzene 5.05% 94.95%Toluene 7.96% 92.04%
Ethylbenzene 10.45% 89.55%Xylenes 12.97% 87.03%
C8+ Heavies 12.18% 87.82%
STREAM REPORTS: -------------------------------------------------------------------
WET GAS STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 8.34e+006 scfh
Component Conc. Loading (vol%) (lb/hr)
------------------------------- --------- ---------Water 6.82e-002 2.70e+002
Carbon Dioxide 1.10e-001 1.06e+003Nitrogen 4.14e-001 2.55e+003Methane 7.16e+001 2.52e+005
Page: 7 Ethane 1.70e+001 1.13e+005
Propane 6.67e+000 6.47e+004 Isobutane 6.67e-001 8.52e+003 n-Butane 2.16e+000 2.76e+004 Isopentane 3.37e-001 5.35e+003 n-Pentane 5.33e-001 8.45e+003
n-Hexane 7.95e-002 1.51e+003 Cyclohexane 1.62e-002 3.00e+002 Other Hexanes 1.86e-001 3.53e+003 Heptanes 9.33e-002 2.06e+003 Methylcyclohexane 1.91e-002 4.12e+002
2,2,4-Trimethylpentane 1.80e-003 4.52e+001 Benzene 7.99e-004 1.37e+001 Toluene 2.40e-003 4.86e+001 Ethylbenzene 1.30e-003 3.03e+001 Xylenes 1.60e-003 3.73e+001
C8+ Heavies 3.86e-002 1.44e+003 ------------------------------- --------- --------- Total Components 100.00 4.93e+005
DRY GAS STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 8.33e+006 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 3.35e-003 1.32e+001 Carbon Dioxide 1.10e-001 1.06e+003 Nitrogen 4.14e-001 2.55e+003 Methane 7.16e+001 2.52e+005 Ethane 1.70e+001 1.13e+005
Propane 6.68e+000 6.47e+004 Isobutane 6.67e-001 8.51e+003 n-Butane 2.16e+000 2.76e+004 Isopentane 3.37e-001 5.35e+003 n-Pentane 5.33e-001 8.44e+003
n-Hexane 7.95e-002 1.50e+003 Cyclohexane 1.61e-002 2.97e+002 Other Hexanes 1.86e-001 3.52e+003 Heptanes 9.32e-002 2.05e+003 Methylcyclohexane 1.90e-002 4.09e+002
2,2,4-Trimethylpentane 1.80e-003 4.51e+001 Benzene 7.45e-004 1.28e+001 Toluene 2.19e-003 4.43e+001 Ethylbenzene 1.17e-003 2.73e+001 Xylenes 1.38e-003 3.21e+001
C8+ Heavies 3.85e-002 1.44e+003 ------------------------------- --------- --------- Total Components 100.00 4.92e+005
LEAN GLYCOL STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Flow Rate: 2.40e+001 gpm
Page: 8Component Conc. Loading
(wt%) (lb/hr) ------------------------------- --------- ---------
TEG 9.85e+001 1.33e+004Water 1.50e+000 2.03e+002
Carbon Dioxide 1.53e-012 2.07e-010Nitrogen 3.25e-013 4.39e-011Methane 8.72e-018 1.18e-015
Ethane 1.49e-007 2.01e-005Propane 1.02e-008 1.38e-006
Isobutane 1.24e-009 1.67e-007n-Butane 4.34e-009 5.86e-007
Isopentane 1.53e-004 2.07e-002
n-Pentane 3.11e-004 4.20e-002n-Hexane 7.87e-005 1.06e-002
Cyclohexane 4.93e-004 6.67e-002Other Hexanes 2.88e-004 3.90e-002
Heptanes 1.76e-004 2.37e-002
Methylcyclohexane 8.29e-004 1.12e-0012,2,4-Trimethylpentane 4.63e-006 6.26e-004
Benzene 3.68e-004 4.97e-002Toluene 2.69e-003 3.63e-001
Ethylbenzene 2.61e-003 3.52e-001
Xylenes 5.71e-003 7.71e-001C8+ Heavies 3.64e-003 4.92e-001
------------------------------- --------- ---------Total Components 100.00 1.35e+004
RICH GLYCOL STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 2.49e+001 gpm NOTE: Stream has more than one phase.
Component Conc. Loading (wt%) (lb/hr)
------------------------------- --------- ---------TEG 9.53e+001 1.33e+004
Water 3.29e+000 4.59e+002Carbon Dioxide 1.48e-002 2.07e+000
Nitrogen 3.15e-003 4.39e-001Methane 2.51e-001 3.50e+001
Ethane 3.05e-001 4.26e+001Propane 2.43e-001 3.38e+001
Isobutane 4.00e-002 5.58e+000n-Butane 1.69e-001 2.36e+001
Isopentane 2.96e-002 4.13e+000
n-Pentane 6.02e-002 8.40e+000n-Hexane 1.52e-002 2.13e+000
Cyclohexane 1.49e-002 2.08e+000Other Hexanes 2.79e-002 3.90e+000
Heptanes 3.40e-002 4.74e+000
Methylcyclohexane 2.01e-002 2.80e+0002,2,4-Trimethylpentane 2.99e-004 4.17e-002
Benzene 7.13e-003 9.94e-001Toluene 3.29e-002 4.60e+000
Ethylbenzene 2.42e-002 3.38e+000
Xylenes 4.27e-002 5.96e+000C8+ Heavies 2.93e-002 4.09e+000
Page: 9 ------------------------------- --------- --------- Total Components 100.00 1.40e+004
FLASH TANK OFF GAS STREAM ------------------------------------------------------------- Temperature: 110.00 deg. F Pressure: 74.70 psia Flow Rate: 1.58e+003 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 1.33e-001 1.00e-001 Carbon Dioxide 6.41e-001 1.18e+000 Nitrogen 3.56e-001 4.17e-001 Methane 4.95e+001 3.32e+001 Ethane 2.80e+001 3.52e+001
Propane 1.25e+001 2.31e+001 Isobutane 1.33e+000 3.22e+000 n-Butane 4.91e+000 1.19e+001 Isopentane 6.33e-001 1.91e+000 n-Pentane 1.12e+000 3.38e+000
n-Hexane 1.56e-001 5.61e-001 Cyclohexane 4.71e-002 1.66e-001 Other Hexanes 3.49e-001 1.26e+000 Heptanes 1.62e-001 6.79e-001 Methylcyclohexane 4.14e-002 1.70e-001
2,2,4-Trimethylpentane 2.21e-003 1.05e-002 Benzene 3.26e-003 1.06e-002 Toluene 7.67e-003 2.95e-002 Ethylbenzene 2.65e-003 1.17e-002 Xylenes 3.08e-003 1.37e-002
C8+ Heavies 7.45e-003 5.30e-002 ------------------------------- --------- --------- Total Components 100.00 1.17e+002
FLASH TANK GLYCOL STREAM ------------------------------------------------------------- Temperature: 110.00 deg. F Flow Rate: 2.47e+001 gpm
Component Conc. Loading (wt%) (lb/hr) ------------------------------- --------- --------- TEG 9.61e+001 1.33e+004 Water 3.32e+000 4.59e+002 Carbon Dioxide 6.44e-003 8.92e-001 Nitrogen 1.63e-004 2.26e-002 Methane 1.35e-002 1.86e+000
Ethane 5.32e-002 7.36e+000 Propane 7.77e-002 1.08e+001 Isobutane 1.71e-002 2.36e+000 n-Butane 8.45e-002 1.17e+001 Isopentane 1.61e-002 2.22e+000
n-Pentane 3.63e-002 5.02e+000 n-Hexane 1.13e-002 1.56e+000 Cyclohexane 1.39e-002 1.92e+000 Other Hexanes 1.91e-002 2.64e+000 Heptanes 2.94e-002 4.06e+000
Page: 10Methylcyclohexane 1.90e-002 2.63e+000
2,2,4-Trimethylpentane 2.25e-004 3.12e-002Benzene 7.11e-003 9.84e-001Toluene 3.30e-002 4.57e+000
Ethylbenzene 2.44e-002 3.37e+000
Xylenes 4.30e-002 5.95e+000C8+ Heavies 2.92e-002 4.04e+000
------------------------------- --------- ---------Total Components 100.00 1.38e+004
FLASH GAS EMISSIONS ------------------------------------------------------------- Flow Rate: 7.23e+003 scfh Control Method: Combustion Device Control Efficiency: 98.00
Component Conc. Loading (vol%) (lb/hr)
------------------------------- --------- ---------Water 6.03e+001 2.07e+002
Carbon Dioxide 3.92e+001 3.29e+002Nitrogen 7.80e-002 4.17e-001Methane 2.17e-001 6.64e-001Ethane 1.23e-001 7.04e-001
Propane 5.49e-002 4.62e-001Isobutane 5.82e-003 6.44e-002n-Butane 2.15e-002 2.39e-001
Isopentane 2.77e-003 3.81e-002n-Pentane 4.91e-003 6.76e-002
n-Hexane 6.83e-004 1.12e-002Cyclohexane 2.06e-004 3.31e-003
Other Hexanes 1.53e-003 2.52e-002Heptanes 7.11e-004 1.36e-002
Methylcyclohexane 1.82e-004 3.40e-003
2,2,4-Trimethylpentane 9.67e-006 2.11e-004Benzene 1.43e-005 2.13e-004Toluene 3.36e-005 5.91e-004
Ethylbenzene 1.16e-005 2.35e-004Xylenes 1.35e-005 2.73e-004
C8+ Heavies 3.26e-005 1.06e-003 ------------------------------- --------- ---------
Total Components 100.00 5.39e+002
REGENERATOR OVERHEADS STREAM ------------------------------------------------------------- Temperature: 212.00 deg. F Pressure: 14.70 psia Flow Rate: 5.88e+003 scfh
Component Conc. Loading (vol%) (lb/hr)
------------------------------- --------- ---------Water 9.19e+001 2.57e+002
Carbon Dioxide 1.31e-001 8.92e-001Nitrogen 5.20e-003 2.26e-002Methane 7.49e-001 1.86e+000Ethane 1.58e+000 7.36e+000
Propane 1.57e+000 1.08e+001Isobutane 2.62e-001 2.36e+000n-Butane 1.30e+000 1.17e+001
Page: 11Isopentane 1.97e-001 2.20e+000n-Pentane 4.45e-001 4.98e+000
n-Hexane 1.16e-001 1.55e+000Cyclohexane 1.42e-001 1.85e+000
Other Hexanes 1.94e-001 2.60e+000Heptanes 2.60e-001 4.04e+000
Methylcyclohexane 1.65e-001 2.52e+000
2,2,4-Trimethylpentane 1.72e-003 3.06e-002Benzene 7.71e-002 9.34e-001Toluene 2.94e-001 4.20e+000
Ethylbenzene 1.83e-001 3.02e+000Xylenes 3.14e-001 5.18e+000
C8+ Heavies 1.34e-001 3.55e+000 ------------------------------- --------- ---------
Total Components 100.00 3.28e+002
COMBUSTION DEVICE OFF GAS STREAM ------------------------------------------------------------- Temperature: 1000.00 deg. F Pressure: 14.70 psia Flow Rate: 9.39e+000 scfh
Component Conc. Loading (vol%) (lb/hr)
------------------------------- --------- ---------Methane 9.38e+000 3.73e-002Ethane 1.98e+001 1.47e-001Propane 1.97e+001 2.15e-001
Isobutane 3.28e+000 4.72e-002n-Butane 1.62e+001 2.34e-001
Isopentane 2.47e+000 4.41e-002n-Pentane 5.57e+000 9.95e-002n-Hexane 1.46e+000 3.11e-002
Cyclohexane 1.78e+000 3.70e-002Other Hexanes 2.44e+000 5.20e-002
Heptanes 3.26e+000 8.08e-002Methylcyclohexane 2.07e+000 5.03e-002
2,2,4-Trimethylpentane 2.16e-002 6.11e-004Benzene 9.66e-001 1.87e-002Toluene 3.69e+000 8.41e-002
Ethylbenzene 2.30e+000 6.04e-002Xylenes 3.94e+000 1.04e-001
C8+ Heavies 1.68e+000 7.09e-002 ------------------------------- --------- ---------
Total Components 100.00 1.41e+000
Page: 1GRI-GLYCalc VERSION 4.0 - SUMMARY OF INPUT VALUES
Case Name: 3WCS-G35-D Gen Permit-S5-200 MMscfd Dehy-043018File Name: D:\Projects2\wfs\AMS\Threedubs\3WCS-G35-D Gen Permit-S5a-200 MMscfdDHY-01-043018 (Backup Pump).ddf Date: April 30, 2018
DESCRIPTION: -------------------------------------------------------------------
Description: Wet Gas: 80 oF, 1000 psig Pump: Gas-Assist, 7.5 gpm (BACKUP) Flash Tank: 110.0 oF, 60 psig Flash Tank/Still Vent Controlled by 98% T-Ox
Annual Hours of Operation: 8760.0 hours/yr
WET GAS: -------------------------------------------------------------------
Temperature: 80.00 deg. F Pressure: 1000.00 psig Wet Gas Water Content: Saturated
Component Conc. (vol %) ------------------------------- ----------- Carbon Dioxide 0.1098 Nitrogen 0.4144 Methane 71.6162 Ethane 17.0404 Propane 6.6780
Isobutane 0.6673 n-Butane 2.1619 Isopentane 0.3376 n-Pentane 0.5333 n-Hexane 0.0796
Cyclohexane 0.0162 Other Hexanes 0.1863 Heptanes 0.0934 Methylcyclohexane 0.0191 2,2,4-Trimethylpentane 0.0018
Benzene 0.0008 Toluene 0.0024 Ethylbenzene 0.0013 Xylenes 0.0016 C8+ Heavies 0.0386
DRY GAS: -------------------------------------------------------------------
Flow Rate: 200.0 MMSCF/day Water Content: 7.0 lbs. H2O/MMSCF
LEAN GLYCOL: -------------------------------------------------------------------
Glycol Type: TEG Water Content: 1.5 wt% H2O Flow Rate: 7.5 gpm
Page: 2 PUMP: -------------------------------------------------------------------
Glycol Pump Type: Gas Injection Gas Injection Pump Volume Ratio: 0.080 acfm gas/gpm glycol
FLASH TANK: -------------------------------------------------------------------
Flash Control: Combustion device Flash Control Efficiency: 98.00 % Temperature: 110.0 deg. F Pressure: 60.0 psig
REGENERATOR OVERHEADS CONTROL DEVICE: -------------------------------------------------------------------
Control Device: Combustion Device Destruction Efficiency: 98.0 % Excess Oxygen: 5.0 % Ambient Air Temperature: 50.0 deg. F
Page: 1GRI-GLYCalc VERSION 4.0 - AGGREGATE CALCULATIONS REPORT
Case Name: 3WCS-G35-D Gen Permit-S5-200 MMscfd Dehy-043018File Name: D:\Projects2\wfs\AMS\Threedubs\3WCS-G35-D Gen Permit-S5a-200 MMscfdDHY-01-043018 (Backup Pump).ddf Date: April 30, 2018
DESCRIPTION:
Description: Wet Gas: 80 oF, 1000 psig Pump: Gas-Assist, 7.5 gpm (BACKUP) Flash Tank: 110.0 oF, 60 psig Flash Tank/Still Vent Controlled by 98% T-Ox
Annual Hours of Operation: 8760.0 hours/yr
EMISSIONS REPORTS: -------------------------------------------------------------------
CONTROLLED REGENERATOR EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 0.0147 0.354 0.0645 Ethane 0.0255 0.612 0.1117 Propane 0.0393 0.942 0.1719 Isobutane 0.0082 0.197 0.0360 n-Butane 0.0381 0.914 0.1667
Isopentane 0.0080 0.192 0.0350 n-Pentane 0.0171 0.411 0.0750 n-Hexane 0.0058 0.140 0.0255 Cyclohexane 0.0072 0.173 0.0316 Other Hexanes 0.0096 0.230 0.0419
Heptanes 0.0169 0.406 0.0742 Methylcyclohexane 0.0109 0.261 0.0477 2,2,4-Trimethylpentane 0.0001 0.003 0.0006 Benzene 0.0054 0.129 0.0235 Toluene 0.0246 0.591 0.1079
Ethylbenzene 0.0180 0.431 0.0787 Xylenes 0.0324 0.776 0.1417 C8+ Heavies 0.0274 0.657 0.1200 ------------------------------- ----------- ----------- ----------- Total Emissions 0.3092 7.420 1.3542
Total Hydrocarbon Emissions 0.3092 7.420 1.3542 Total VOC Emissions 0.2689 6.454 1.1779 Total HAP Emissions 0.0863 2.071 0.3779 Total BTEX Emissions 0.0803 1.928 0.3518
UNCONTROLLED REGENERATOR EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 0.7368 17.684 3.2273 Ethane 1.2756 30.614 5.5870 Propane 1.9627 47.106 8.5968 Isobutane 0.4105 9.851 1.7979 n-Butane 1.9034 45.680 8.3367
Isopentane 0.3993 9.584 1.7490 n-Pentane 0.8564 20.555 3.7512
Page: 2 n-Hexane 0.2907 6.977 1.2733 Cyclohexane 0.3610 8.665 1.5813 Other Hexanes 0.4784 11.481 2.0952
Heptanes 0.8469 20.325 3.7092 Methylcyclohexane 0.5447 13.074 2.3859 2,2,4-Trimethylpentane 0.0071 0.170 0.0310 Benzene 0.2684 6.443 1.1758 Toluene 1.2317 29.561 5.3949
Ethylbenzene 0.8982 21.557 3.9342 Xylenes 1.6175 38.820 7.0847 C8+ Heavies 1.3694 32.865 5.9979 ------------------------------- ----------- ----------- ----------- Total Emissions 15.4587 371.010 67.7093
Total Hydrocarbon Emissions 15.4587 371.010 67.7093 Total VOC Emissions 13.4463 322.712 58.8950 Total HAP Emissions 4.3137 103.528 18.8938 Total BTEX Emissions 4.0159 96.381 17.5895
FLASH GAS EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 2.2744 54.585 9.9617 Ethane 1.1480 27.553 5.0284 Propane 0.6997 16.792 3.0645 Isobutane 0.0955 2.291 0.4181 n-Butane 0.3311 7.945 1.4500
Isopentane 0.0605 1.451 0.2649 n-Pentane 0.1020 2.448 0.4468 n-Hexane 0.0189 0.454 0.0829 Cyclohexane 0.0065 0.156 0.0285 Other Hexanes 0.0420 1.007 0.1838
Heptanes 0.0268 0.644 0.1175 Methylcyclohexane 0.0074 0.178 0.0325 2,2,4-Trimethylpentane 0.0005 0.011 0.0020 Benzene 0.0005 0.013 0.0023 Toluene 0.0015 0.037 0.0068
Ethylbenzene 0.0006 0.015 0.0028 Xylenes 0.0008 0.018 0.0033 C8+ Heavies 0.0041 0.099 0.0180 ------------------------------- ----------- ----------- ----------- Total Emissions 4.8207 115.697 21.1147
Total Hydrocarbon Emissions 4.8207 115.697 21.1147 Total VOC Emissions 1.3983 33.559 6.1246 Total HAP Emissions 0.0229 0.548 0.1001 Total BTEX Emissions 0.0035 0.083 0.0152
FLASH TANK OFF GAS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 113.7177 2729.225 498.0836 Ethane 57.4021 1377.649 251.4210 Propane 34.9827 839.586 153.2244 Isobutane 4.7728 114.546 20.9047 n-Butane 16.5527 397.264 72.5006
Isopentane 3.0235 72.563 13.2428 n-Pentane 5.1001 122.403 22.3386
Page: 3 n-Hexane 0.9459 22.703 4.1432 Cyclohexane 0.3248 7.796 1.4228 Other Hexanes 2.0978 50.348 9.1884
Heptanes 1.3417 32.201 5.8767 Methylcyclohexane 0.3711 8.906 1.6254 2,2,4-Trimethylpentane 0.0232 0.556 0.1015 Benzene 0.0265 0.636 0.1160 Toluene 0.0773 1.855 0.3385
Ethylbenzene 0.0321 0.769 0.1404 Xylenes 0.0377 0.906 0.1653 C8+ Heavies 0.2056 4.936 0.9007 ------------------------------- ----------- ----------- ----------- Total Emissions 241.0353 5784.847 1055.7346
Total Hydrocarbon Emissions 241.0353 5784.847 1055.7346 Total VOC Emissions 69.9155 1677.973 306.2300 Total HAP Emissions 1.1427 27.424 5.0049 Total BTEX Emissions 0.1736 4.165 0.7602
COMBINED REGENERATOR VENT/FLASH GAS EMISSIONS ------------------------------------------------------------------- Component lbs/hr lbs/day tons/yr ------------------------------- ----------- ----------- ----------- Methane 2.2891 54.938 10.0262 Ethane 1.1736 28.165 5.1402 Propane 0.7389 17.734 3.2364 Isobutane 0.1037 2.488 0.4541 n-Butane 0.3691 8.859 1.6167
Isopentane 0.0685 1.643 0.2998 n-Pentane 0.1191 2.859 0.5218 n-Hexane 0.0247 0.594 0.1083 Cyclohexane 0.0137 0.329 0.0601 Other Hexanes 0.0515 1.237 0.2257
Heptanes 0.0438 1.051 0.1917 Methylcyclohexane 0.0183 0.440 0.0802 2,2,4-Trimethylpentane 0.0006 0.015 0.0026 Benzene 0.0059 0.142 0.0258 Toluene 0.0262 0.628 0.1147
Ethylbenzene 0.0186 0.447 0.0815 Xylenes 0.0331 0.795 0.1450 C8+ Heavies 0.0315 0.756 0.1380 ------------------------------- ----------- ----------- ----------- Total Emissions 5.1299 123.117 22.4689
Total Hydrocarbon Emissions 5.1299 123.117 22.4689 Total VOC Emissions 1.6672 40.014 7.3025 Total HAP Emissions 0.1091 2.619 0.4780 Total BTEX Emissions 0.0838 2.011 0.3670
COMBINED REGENERATOR VENT/FLASH GAS EMISSION CONTROL REPORT: -------------------------------------------------------------------
Component Uncontrolled Controlled % Reduction tons/yr tons/yr ------------------------------- ------------ ------------ ------------ Methane 501.3109 10.0262 98.00 Ethane 257.0080 5.1402 98.00 Propane 161.8212 3.2364 98.00 Isobutane 22.7026 0.4541 98.00 n-Butane 80.8373 1.6167 98.00
Page: 4
Isopentane 14.9918 0.2998 98.00 n-Pentane 26.0898 0.5218 98.00 n-Hexane 5.4165 0.1083 98.00 Cyclohexane 3.0041 0.0601 98.00 Other Hexanes 11.2837 0.2257 98.00
Heptanes 9.5859 0.1917 98.00 Methylcyclohexane 4.0113 0.0802 98.00 2,2,4-Trimethylpentane 0.1324 0.0026 98.00 Benzene 1.2918 0.0258 98.00 Toluene 5.7333 0.1147 98.00
Ethylbenzene 4.0746 0.0815 98.00 Xylenes 7.2499 0.1450 98.00 C8+ Heavies 6.8986 0.1380 98.00 ------------------------------- ------------ ------------ ------------ Total Emissions 1123.4439 22.4689 98.00
Total Hydrocarbon Emissions 1123.4439 22.4689 98.00 Total VOC Emissions 365.1250 7.3025 98.00 Total HAP Emissions 23.8987 0.4780 98.00 Total BTEX Emissions 18.3497 0.3670 98.00
EQUIPMENT REPORTS: -------------------------------------------------------------------
COMBUSTION DEVICE -------------------------------------------------------------------
Ambient Temperature: 50.00 deg. F Excess Oxygen: 5.00 % Combustion Efficiency: 98.00 % Supplemental Fuel Requirement: 1.57e-001 MM BTU/hr
Component Emitted Destroyed ------------------------------- ----------- ----------- Methane 2.00% 98.00% Ethane 2.00% 98.00% Propane 2.00% 98.00% Isobutane 2.00% 98.00% n-Butane 2.00% 98.00%
Isopentane 2.00% 98.00% n-Pentane 2.00% 98.00% n-Hexane 2.00% 98.00% Cyclohexane 2.00% 98.00% Other Hexanes 2.00% 98.00%
Heptanes 2.00% 98.00% Methylcyclohexane 2.00% 98.00% 2,2,4-Trimethylpentane 2.00% 98.00% Benzene 2.00% 98.00% Toluene 2.00% 98.00%
Ethylbenzene 2.00% 98.00% Xylenes 2.00% 98.00% C8+ Heavies 2.00% 98.00%
ABSORBER -------------------------------------------------------------------
Page: 5NOTE: Because the Calculated Absorber Stages was below the minimumallowed, GRI-GLYCalc has set the number of Absorber Stages to 1.25and has calculated a revised Dry Gas Dew Point.
Calculated Absorber Stages: 1.25 Calculated Dry Gas Dew Point: 3.28 lbs. H2O/MMSCF
Temperature: 80.0 deg. F Pressure: 1000.0 psig Dry Gas Flow Rate: 200.0000 MMSCF/day Glycol Losses with Dry Gas: 3.8621 lb/hr Wet Gas Water Content: Saturated Calculated Wet Gas Water Content: 32.36 lbs. H2O/MMSCF Calculated Lean Glycol Recirc. Ratio: 1.86 gal/lb H2O
Remaining Absorbed Component in Dry Gas in Glycol ------------------------------- ----------- ----------- Water 10.14% 89.86% Carbon Dioxide 99.94% 0.06% Nitrogen 100.00% 0.00% Methane 100.00% 0.00% Ethane 99.99% 0.01%
Propane 99.98% 0.02% Isobutane 99.98% 0.02% n-Butane 99.97% 0.03% Isopentane 99.98% 0.02% n-Pentane 99.97% 0.03%
n-Hexane 99.96% 0.04% Cyclohexane 99.81% 0.19% Other Hexanes 99.97% 0.03% Heptanes 99.93% 0.07% Methylcyclohexane 99.82% 0.18%
2,2,4-Trimethylpentane 99.97% 0.03% Benzene 97.89% 2.11% Toluene 97.35% 2.65% Ethylbenzene 96.97% 3.03% Xylenes 95.61% 4.39%
C8+ Heavies 99.93% 0.07%
FLASH TANK -------------------------------------------------------------------
Flash Control: Combustion device Flash Control Efficiency: 98.00 % Flash Temperature: 110.0 deg. F Flash Pressure: 60.0 psig
Left in Removed in Component Glycol Flash Gas ------------------------------- ----------- ----------- Water 99.83% 0.17% Carbon Dioxide 8.29% 91.71% Nitrogen 0.59% 99.41% Methane 0.64% 99.36% Ethane 2.17% 97.83%
Propane 5.31% 94.69% Isobutane 7.92% 92.08% n-Butane 10.31% 89.69% Isopentane 11.82% 88.18% n-Pentane 14.56% 85.44%
n-Hexane 23.70% 76.30%
Page: 6 Cyclohexane 53.89% 46.11% Other Hexanes 18.93% 81.07% Heptanes 38.88% 61.12% Methylcyclohexane 60.81% 39.19%
2,2,4-Trimethylpentane 23.83% 76.17% Benzene 91.46% 8.54% Toluene 94.56% 5.44% Ethylbenzene 96.91% 3.09% Xylenes 98.01% 1.99%
C8+ Heavies 87.96% 12.04%
REGENERATOR -------------------------------------------------------------------
No Stripping Gas used in regenerator.
Remaining Distilled Component in Glycol Overhead ------------------------------- ----------- ----------- Water 20.73% 79.27% Carbon Dioxide 0.00% 100.00% Nitrogen 0.00% 100.00% Methane 0.00% 100.00% Ethane 0.00% 100.00%
Propane 0.00% 100.00% Isobutane 0.00% 100.00% n-Butane 0.00% 100.00% Isopentane 1.51% 98.49% n-Pentane 1.43% 98.57%
n-Hexane 1.05% 98.95% Cyclohexane 4.90% 95.10% Other Hexanes 2.31% 97.69% Heptanes 0.79% 99.21% Methylcyclohexane 5.40% 94.60%
2,2,4-Trimethylpentane 2.44% 97.56% Benzene 5.37% 94.63% Toluene 8.24% 91.76% Ethylbenzene 10.60% 89.40% Xylenes 13.04% 86.96%
C8+ Heavies 8.88% 91.12%
STREAM REPORTS: -------------------------------------------------------------------
WET GAS STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 8.34e+006 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 6.82e-002 2.70e+002 Carbon Dioxide 1.10e-001 1.06e+003 Nitrogen 4.14e-001 2.55e+003 Methane 7.16e+001 2.52e+005
Page: 7 Ethane 1.70e+001 1.13e+005
Propane 6.67e+000 6.47e+004 Isobutane 6.67e-001 8.52e+003 n-Butane 2.16e+000 2.76e+004 Isopentane 3.37e-001 5.35e+003 n-Pentane 5.33e-001 8.45e+003
n-Hexane 7.95e-002 1.51e+003 Cyclohexane 1.62e-002 2.99e+002 Other Hexanes 1.86e-001 3.53e+003 Heptanes 9.33e-002 2.06e+003 Methylcyclohexane 1.91e-002 4.12e+002
2,2,4-Trimethylpentane 1.80e-003 4.52e+001 Benzene 7.99e-004 1.37e+001 Toluene 2.40e-003 4.86e+001 Ethylbenzene 1.30e-003 3.03e+001 Xylenes 1.60e-003 3.73e+001
C8+ Heavies 3.86e-002 1.44e+003 ------------------------------- --------- --------- Total Components 100.00 4.93e+005
DRY GAS STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 8.33e+006 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 6.92e-003 2.74e+001 Carbon Dioxide 1.10e-001 1.06e+003 Nitrogen 4.14e-001 2.55e+003 Methane 7.16e+001 2.52e+005 Ethane 1.70e+001 1.13e+005
Propane 6.68e+000 6.47e+004 Isobutane 6.67e-001 8.52e+003 n-Butane 2.16e+000 2.76e+004 Isopentane 3.38e-001 5.35e+003 n-Pentane 5.33e-001 8.45e+003
n-Hexane 7.96e-002 1.51e+003 Cyclohexane 1.62e-002 2.99e+002 Other Hexanes 1.86e-001 3.53e+003 Heptanes 9.33e-002 2.05e+003 Methylcyclohexane 1.91e-002 4.11e+002
2,2,4-Trimethylpentane 1.80e-003 4.51e+001 Benzene 7.83e-004 1.34e+001 Toluene 2.34e-003 4.73e+001 Ethylbenzene 1.26e-003 2.94e+001 Xylenes 1.53e-003 3.57e+001
C8+ Heavies 3.86e-002 1.44e+003 ------------------------------- --------- --------- Total Components 100.00 4.92e+005
LEAN GLYCOL STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Flow Rate: 7.50e+000 gpm
Page: 8 Component Conc. Loading (wt%) (lb/hr) ------------------------------- --------- --------- TEG 9.85e+001 4.16e+003 Water 1.50e+000 6.33e+001 Carbon Dioxide 1.50e-012 6.34e-011 Nitrogen 3.01e-013 1.27e-011 Methane 8.21e-018 3.47e-016
Ethane 1.37e-007 5.77e-006 Propane 9.88e-009 4.17e-007 Isobutane 1.18e-009 5.00e-008 n-Butane 4.15e-009 1.75e-007 Isopentane 1.45e-004 6.10e-003
n-Pentane 2.94e-004 1.24e-002 n-Hexane 7.32e-005 3.09e-003 Cyclohexane 4.40e-004 1.86e-002 Other Hexanes 2.68e-004 1.13e-002 Heptanes 1.60e-004 6.73e-003
Methylcyclohexane 7.36e-004 3.11e-002 2,2,4-Trimethylpentane 4.18e-006 1.77e-004 Benzene 3.61e-004 1.52e-002 Toluene 2.62e-003 1.11e-001 Ethylbenzene 2.52e-003 1.06e-001
Xylenes 5.75e-003 2.43e-001 C8+ Heavies 3.16e-003 1.33e-001 ------------------------------- --------- --------- Total Components 100.00 4.22e+003
RICH GLYCOL AND PUMP GAS STREAM ------------------------------------------------------------- Temperature: 80.00 deg. F Pressure: 1014.70 psia Flow Rate: 8.55e+000 gpm NOTE: Stream has more than one phase.
Component Conc. Loading (wt%) (lb/hr) ------------------------------- --------- --------- TEG 8.80e+001 4.16e+003 Water 6.48e+000 3.06e+002 Carbon Dioxide 2.27e-002 1.07e+000 Nitrogen 2.50e-002 1.18e+000 Methane 2.42e+000 1.14e+002
Ethane 1.24e+000 5.87e+001 Propane 7.82e-001 3.69e+001 Isobutane 1.10e-001 5.18e+000 n-Butane 3.91e-001 1.85e+001 Isopentane 7.26e-002 3.43e+000
n-Pentane 1.26e-001 5.97e+000 n-Hexane 2.63e-002 1.24e+000 Cyclohexane 1.49e-002 7.04e-001 Other Hexanes 5.48e-002 2.59e+000 Heptanes 4.65e-002 2.20e+000
Methylcyclohexane 2.01e-002 9.47e-001 2,2,4-Trimethylpentane 6.44e-004 3.04e-002 Benzene 6.57e-003 3.10e-001 Toluene 3.01e-002 1.42e+000 Ethylbenzene 2.20e-002 1.04e+000
Xylenes 4.02e-002 1.90e+000 C8+ Heavies 3.62e-002 1.71e+000
Page: 9 ------------------------------- --------- --------- Total Components 100.00 4.72e+003
FLASH TANK OFF GAS STREAM ------------------------------------------------------------- Temperature: 110.00 deg. F Pressure: 74.70 psia Flow Rate: 3.96e+003 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 2.84e-001 5.33e-001 Carbon Dioxide 2.14e-001 9.83e-001 Nitrogen 4.01e-001 1.17e+000 Methane 6.80e+001 1.14e+002 Ethane 1.83e+001 5.74e+001
Propane 7.61e+000 3.50e+001 Isobutane 7.88e-001 4.77e+000 n-Butane 2.73e+000 1.66e+001 Isopentane 4.02e-001 3.02e+000 n-Pentane 6.78e-001 5.10e+000
n-Hexane 1.05e-001 9.46e-001 Cyclohexane 3.70e-002 3.25e-001 Other Hexanes 2.34e-001 2.10e+000 Heptanes 1.28e-001 1.34e+000 Methylcyclohexane 3.63e-002 3.71e-001
2,2,4-Trimethylpentane 1.95e-003 2.32e-002 Benzene 3.25e-003 2.65e-002 Toluene 8.05e-003 7.73e-002 Ethylbenzene 2.90e-003 3.21e-002 Xylenes 3.41e-003 3.77e-002
C8+ Heavies 1.16e-002 2.06e-001 ------------------------------- --------- --------- Total Components 100.00 2.44e+002
FLASH TANK GLYCOL STREAM ------------------------------------------------------------- Temperature: 110.00 deg. F Flow Rate: 8.01e+000 gpm
Component Conc. Loading (wt%) (lb/hr) ------------------------------- --------- --------- TEG 9.28e+001 4.16e+003 Water 6.82e+000 3.05e+002 Carbon Dioxide 1.98e-003 8.88e-002 Nitrogen 1.57e-004 7.01e-003 Methane 1.65e-002 7.37e-001
Ethane 2.85e-002 1.28e+000 Propane 4.38e-002 1.96e+000 Isobutane 9.17e-003 4.10e-001 n-Butane 4.25e-002 1.90e+000 Isopentane 9.05e-003 4.05e-001
n-Pentane 1.94e-002 8.69e-001 n-Hexane 6.56e-003 2.94e-001 Cyclohexane 8.48e-003 3.80e-001 Other Hexanes 1.09e-002 4.90e-001 Heptanes 1.91e-002 8.54e-001
Page: 10 Methylcyclohexane 1.29e-002 5.76e-001 2,2,4-Trimethylpentane 1.62e-004 7.25e-003 Benzene 6.34e-003 2.84e-001 Toluene 3.00e-002 1.34e+000 Ethylbenzene 2.24e-002 1.00e+000
Xylenes 4.15e-002 1.86e+000 C8+ Heavies 3.36e-002 1.50e+000 ------------------------------- --------- --------- Total Components 100.00 4.48e+003
FLASH GAS EMISSIONS ------------------------------------------------------------- Flow Rate: 1.56e+004 scfh Control Method: Combustion Device Control Efficiency: 98.00
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 6.20e+001 4.60e+002 Carbon Dioxide 3.74e+001 6.78e+002 Nitrogen 1.02e-001 1.17e+000 Methane 3.44e-001 2.27e+000 Ethane 9.27e-002 1.15e+000
Propane 3.85e-002 7.00e-001 Isobutane 3.99e-003 9.55e-002 n-Butane 1.38e-002 3.31e-001 Isopentane 2.03e-003 6.05e-002 n-Pentane 3.43e-003 1.02e-001
n-Hexane 5.33e-004 1.89e-002 Cyclohexane 1.87e-004 6.50e-003 Other Hexanes 1.18e-003 4.20e-002 Heptanes 6.50e-004 2.68e-002 Methylcyclohexane 1.84e-004 7.42e-003
2,2,4-Trimethylpentane 9.85e-006 4.63e-004 Benzene 1.65e-005 5.30e-004 Toluene 4.07e-005 1.55e-003 Ethylbenzene 1.47e-005 6.41e-004 Xylenes 1.73e-005 7.55e-004
C8+ Heavies 5.86e-005 4.11e-003 ------------------------------- --------- --------- Total Components 100.00 1.14e+003
REGENERATOR OVERHEADS STREAM ------------------------------------------------------------- Temperature: 212.00 deg. F Pressure: 14.70 psia Flow Rate: 5.20e+003 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Water 9.80e+001 2.42e+002 Carbon Dioxide 1.47e-002 8.88e-002 Nitrogen 1.83e-003 7.01e-003 Methane 3.35e-001 7.37e-001 Ethane 3.09e-001 1.28e+000
Propane 3.25e-001 1.96e+000 Isobutane 5.15e-002 4.10e-001 n-Butane 2.39e-001 1.90e+000
Page: 11 Isopentane 4.04e-002 3.99e-001 n-Pentane 8.66e-002 8.56e-001
n-Hexane 2.46e-002 2.91e-001 Cyclohexane 3.13e-002 3.61e-001 Other Hexanes 4.05e-002 4.78e-001 Heptanes 6.16e-002 8.47e-001 Methylcyclohexane 4.05e-002 5.45e-001
2,2,4-Trimethylpentane 4.51e-004 7.07e-003 Benzene 2.51e-002 2.68e-001 Toluene 9.75e-002 1.23e+000 Ethylbenzene 6.17e-002 8.98e-001 Xylenes 1.11e-001 1.62e+000
C8+ Heavies 5.86e-002 1.37e+000 ------------------------------- --------- --------- Total Components 100.00 2.58e+002
COMBUSTION DEVICE OFF GAS STREAM ------------------------------------------------------------- Temperature: 1000.00 deg. F Pressure: 14.70 psia Flow Rate: 2.02e+000 scfh
Component Conc. Loading (vol%) (lb/hr) ------------------------------- --------- --------- Methane 1.73e+001 1.47e-002 Ethane 1.60e+001 2.55e-002 Propane 1.67e+001 3.93e-002 Isobutane 2.66e+000 8.21e-003 n-Butane 1.23e+001 3.81e-002
Isopentane 2.08e+000 7.99e-003 n-Pentane 4.46e+000 1.71e-002 n-Hexane 1.27e+000 5.81e-003 Cyclohexane 1.61e+000 7.22e-003 Other Hexanes 2.09e+000 9.57e-003
Heptanes 3.18e+000 1.69e-002 Methylcyclohexane 2.09e+000 1.09e-002 2,2,4-Trimethylpentane 2.33e-002 1.41e-004 Benzene 1.29e+000 5.37e-003 Toluene 5.03e+000 2.46e-002
Ethylbenzene 3.18e+000 1.80e-002 Xylenes 5.73e+000 3.24e-002 C8+ Heavies 3.02e+000 2.74e-002 ------------------------------- --------- --------- Total Components 100.00 3.09e-001
TANKS 4.0.9dEmissions Report - Summary Format
Tank Indentification and Physical Characteristics
IdentificationUser Identification: Pioneer CF Stabilized Condensate TankCity: MoundsvilleState: West VirginiaCompany: Appalachia Midstream ServicesType of Tank: Vertical Fixed Roof Tank
Description: Total of six 400 bbl storage vessels holding stabilized condensate. Each storage vessel will receive up to 38,000 bbl of stabilized condensate per year.
Tank DimensionsShell Height (ft): 20.00Diameter (ft): 12.00Liquid Height (ft) : 19.00Avg. Liquid Height (ft): 10.00Volume (gallons): 16,800.00Turnovers: 95.00Net Throughput(gal/yr): 1,596,000.00Is Tank Heated (y/n): N
Paint CharacteristicsShell Color/Shade: White/WhiteShell Condition GoodRoof Color/Shade: White/WhiteRoof Condition: Good
Roof CharacteristicsType: ConeHeight (ft) 0.00Slope (ft/ft) (Cone Roof) 0.06
Breather Vent SettingsVacuum Settings (psig): -0.03Pressure Settings (psig) 0.03
Meterological Data used in Emissions Calculations: Pittsburgh, Pennsylvania (Avg Atmospheric Pressure = 14.11 psia)
Page 1 of 5TANKS 4.0 Report
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TANKS 4.0.9dEmissions Report - Summary Format
Liquid Contents of Storage Tank
Pioneer CF Stabilized Condensate Tank - Vertical Fixed Roof TankMoundsville, West Virginia
Daily Liquid Surf.Temperature (deg F)
LiquidBulk
Temp Vapor Pressure (psia)Vapor
Mol.LiquidMass
VaporMass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations
Stabilized Condensate All 51.94 47.06 56.81 50.33 4.7743 4.3390 5.2511 60.2678 94.63 2,2,4-Trimethylpentane 0.4700 0.4055 0.5431 114.2300 0.0043 0.0007 114.23 Option 2: A=6.8118, B=1257.84, C=220.74 Benzene 0.9298 0.8065 1.0684 78.1100 0.0005 0.0001 78.11 Option 2: A=6.905, B=1211.033, C=220.79 Cyclohexane 0.9696 0.8439 1.1105 84.1600 0.0108 0.0035 84.16 Option 2: A=6.841, B=1201.53, C=222.65 Ethylbenzene 0.0815 0.0682 0.0971 106.1700 0.0129 0.0003 106.17 Option 2: A=6.975, B=1424.255, C=213.21 Heptane (-n) 0.4785 0.4109 0.5555 100.2000 0.1696 0.0267 100.20 Option 3: A=37358, B=8.2585 Hexane (-n) 1.5451 1.3522 1.7601 86.1700 0.0476 0.0242 86.17 Option 2: A=6.876, B=1171.17, C=224.41 Hexanes 1.5451 1.3522 1.7601 86.1700 0.0753 0.0383 86.17 Option 2: A=6.876, B=1171.17, C=224.41 iso-Butane 33.1744 30.3990 36.1806 58.1300 0.0100 0.1090 58.13 Option 1: VP50 = 31.982 VP60 = 38.144 iso-Pentane 7.9463 7.1399 8.8396 72.1500 0.0316 0.0825 72.15 Option 1: VP50 = 7.592 VP60 = 9.423 Methylcyclohexane 0.4402 0.3794 0.5089 98.1800 0.0414 0.0060 98.18 Option 2: A=6.823, B=1270.763, C=221.42 n-Butane 22.4567 20.4389 24.6593 58.1300 0.0545 0.4024 58.13 Option 1: VP50 = 21.583 VP60 = 26.098 n-Pentane 5.7463 5.1349 6.4279 72.1500 0.0688 0.1299 72.15 Option 1: VP50 = 5.476 VP60 = 6.873 Octane (-n) 0.1188 0.1049 0.1349 114.2300 0.4444 0.0174 114.23 Option 1: VP50 = .112388 VP60 = .145444 Propane 95.7217 88.6799 103.2639 44.1100 0.0050 0.1582 44.11 Option 1: VP50 = 92.73 VP60 = 108.19 Toluene 0.2556 0.2178 0.2987 92.1300 0.0065 0.0005 92.13 Option 2: A=6.954, B=1344.8, C=219.48 Xylene (-m) 0.0677 0.0565 0.0807 106.1700 0.0168 0.0004 106.17 Option 2: A=7.009, B=1462.266, C=215.11
Page 2 of 5TANKS 4.0 Report
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TANKS 4.0.9dEmissions Report - Summary Format
Individual Tank Emission Totals
Emissions Report for: Annual
Pioneer CF Stabilized Condensate Tank - Vertical Fixed Roof TankMoundsville, West Virginia
Losses(lbs)Components Working Loss Breathing Loss Total EmissionsStabilized Condensate 5,275.20 795.97 6,071.17 Propane 834.28 125.88 960.17 iso-Butane 574.88 86.74 661.63 n-Butane 2,122.84 320.31 2,443.15 iso-Pentane 435.01 65.64 500.65 n-Pentane 685.47 103.43 788.90 Cyclohexane 18.22 2.75 20.97 Hexanes 201.95 30.47 232.42 Methylcyclohexane 31.60 4.77 36.37 Octane (-n) 91.59 13.82 105.40 Benzene 0.78 0.12 0.90 Ethylbenzene 1.82 0.27 2.09 Hexane (-n) 127.61 19.25 146.86 Toluene 2.87 0.43 3.30 2,2,4-Trimethylpentane 3.54 0.53 4.07 Xylene (-m) 1.98 0.30 2.28 Heptane (-n) 140.78 21.24 162.02
Page 4 of 5TANKS 4.0 Report
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TANKS 4.0.9dEmissions Report - Summary Format
Tank Indentification and Physical Characteristics
IdentificationUser Identification: Pioneer CF Produced Water TankCity: MoundsvilleState: West VirginiaCompany: Williams Ohio Valley MidstreamType of Tank: Vertical Fixed Roof TankDescription: 400 bbl produced water storage tank
Tank DimensionsShell Height (ft): 20.00Diameter (ft): 12.00Liquid Height (ft) : 19.00Avg. Liquid Height (ft): 10.00Volume (gallons): 16,800.00Turnovers: 37.50Net Throughput(gal/yr): 630,000.00Is Tank Heated (y/n): N
Paint CharacteristicsShell Color/Shade: White/WhiteShell Condition GoodRoof Color/Shade: White/WhiteRoof Condition: Good
Roof CharacteristicsType: ConeHeight (ft) 0.00Slope (ft/ft) (Cone Roof) 0.06
Breather Vent SettingsVacuum Settings (psig): -0.03Pressure Settings (psig) 0.03
Meterological Data used in Emissions Calculations: Pittsburgh, Pennsylvania (Avg Atmospheric Pressure = 14.11 psia)
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TANKS 4.0.9dEmissions Report - Summary Format
Liquid Contents of Storage Tank
Pioneer CF Produced Water Tank - Vertical Fixed Roof TankMoundsville, West Virginia
Daily Liquid Surf.Temperature (deg F)
LiquidBulk
Temp Vapor Pressure (psia)Vapor
Mol.LiquidMass
VaporMass Mol. Basis for Vapor Pressure
Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations
Produced Water (95% Water + 5% Condensate) All 51.94 47.06 56.81 50.33 0.2465 0.2101 0.2893 28.3522 18.75
Gasoline (RVP 12) 5.4430 4.9447 5.9807 64.0000 0.0500 0.5080 92.00 Option 4: RVP=12, ASTM Slope=3 Water 0.1930 0.1614 0.2307 18.0000 0.9500 0.4920 18.00 Option 1: VP50 = .178073 VP60 = .255246
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TANKS 4.0.9dEmissions Report - Summary Format
Individual Tank Emission Totals
Emissions Report for: Annual
Pioneer CF Produced Water Tank - Vertical Fixed Roof TankMoundsville, West Virginia
Losses(lbs)Components Working Loss Breathing Loss Total EmissionsProduced Water (95% Water + 5% Condensate) 101.34 18.57 119.92
Water 49.86 9.14 59.00 Gasoline (RVP 12) 51.48 9.44 60.92
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Application Fee Determination
Check payable to WVDEP – Division of Air Quality with the appropriate application fee (per 45CSR13 and 45CSR22).
Payment Method:
☒ Check attached to front of application. ☐ I wish to pay by electronic transfer. Contact for payment (incl. name and email address):
na
☐ I wish to pay by credit card. Contact for payment (incl. name and email address): na
Payment Amount:
☒ $500 (Construction, Modification, and Relocation) ☐ $300 (Class II Administrative Update) ☒ $1,000 NSPS fee for 40 CFR60, Subpart IIII, JJJJ and/or OOOO and/or OOOOa1
☒ $2,500 NESHAP fee for 40 CFR63, Subpart ZZZZ and/or HH2
1 Only one NSPS fee will apply. 2 Only one NESHAP fee will apply. The Subpart ZZZZ NESHAP fee will be waived for new
engines that satisfy requirements by complying with NSPS Subparts IIII and/or JJJJ. NSPS and NESHAP fees apply to new construction or if the source is being modified.
Total Amount Due: $4,000
** End of Application for G35-D General Permit Registration **