FINAL_HOR_Attachment_Fcont'd_thru_G-Northampton_Compressor_Station

FORMS
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) EVISED 12/01/01 NCDENR/Dlvision of Air Quality -Application for Air Permit to Construct/Operate B ,iMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01 Caterpillar G3516B Emergency Generator CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form B8) D Liquid storage tanks (Form 83) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Caterpillar G3516B EXPECTED OP. SCHEDULE: 100 HRNR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, llZZ PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE -
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) Mfg/AP-42 0.638 0.032 0.638 0.032 0.638 0.032 PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42 0.638 0.032 0.638 0.032 0.638 0.032 PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42 0.638 0.032 0.638 0.032 0.638 0.032 SULFUR DIOXIDE (SO2) AP-42 0.008 3.88E-04 0.008 3.88E-04 0.008 3.88E-04 NITROGEN OXIDES (NOx) Mfg 2.00 0.100 2.00 0.100 2.00 0.100 'ARBON MONOXIDE (CO) Mfg 9.98 0.499 9.98 0.499 9.98 0.499 AOLATILE ORGANIC COMPOUNDS (VOC) Mfg 2.16 0.108 2.16 0.108 2.16 0.108 LEAD OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr 1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 0.0003 0.00002 0.0003 0.00002 0.0003 0.00002 1, 1,2-Trichloroethane 79-00-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1, 1-Dichloroethane 75-34-3 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1,2-Dichloroethane 107-06-2 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1,2-Dichloropropane 78-87-5 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 1,3-Butadiene 106-99-0 AP-42 0.004 0.0002 0.004 0.0002 0.004 0.0002 1,3-Dichloropropene 542-75-6 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001 2,2,4-Trimethylpentane 540-84-1 AP-42 0.004 0.0002 0.004 0.0002 0.004 0.0002
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr 1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 0.0003 0.01 0.03 1,2-Dichloroethane 107-06-2 AP-42 0.0002 0.00 0.02 1,3-Butadiene 106-99-0 AP-42 0.004 0.09 0.38 Acetaldehyde 75-07-0 AP-42 0.04 0.86 3.59 Acrolein 107-02-8 AP-42 0.04 0.86 3.60 Benzene 71-43-2 AP-42 0.009 0.22 0.90 Benzo(a)pyrene 50-32-8 AP-42 0.00000003 0.0000006 2.63E-06
q,boo Tetrachloride 56-23-5 AP-42 0.0003 O.ot 0.03 Attachments: (1) emissions calculations and supporting documentation; (2) indicale all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe ow these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-178
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B
.i!MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-01
Caterpillar G3516B Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7)
0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form B8) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Caterpillar G3516B EXPECTED OP. SCHEDULE: 100 HR/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZllZ
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42
PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42
SULFUR DIOXIDE (S02) AP-42
NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source c.. )ARBON MONOXIDE (CO) Mfg
{/OLATILE ORGANIC COMPOUNDS (VOC) Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Acetaldehyde 75-07-0 AP-42 0.04 0.002 0.04 0.002 0.04 0.002
Acrolein 107-02-8 AP-42 0.04 0.002 0.04 0.002 0.04 0.002
Benzene 71-43-2 AP-42 0.01 0.0004 0.01 0.0004 0.01 0.0004
Biphenyl 92-52-4 AP-42 0.00002 0.000001 0.00002 0.000001 0.00002 0.000001
Carbon Tetrachloride 56-23-5 AP-42 0.0003 0.00001 0.0003 0.00001 0.0003 0.00001
Chlorobenzene 108-90-7 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001
Chloroform 67-66-3 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001
Ethylbenzene 100-41-4 AP-42 0.0005 0.00002 0.00 0.00002 0.0005 0.00002
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Chlorobenzene 108-90-7 AP-42 0.0002 0.005 0.02
Chloroform 67-66-3 AP-42 0.0002 0.005 0.02
Ethylene Dibromide 106-93-4 AP-42 0.0003 0.0081 0.03
Formaldehyde 50-00-0 AP-42 0.26 6.13 25.53
Hexane (or n-Hexane) 110-54-3 AP-42 0.002 0.05 0.21
Methylene Chloride 75-09-2 AP-42 0.0007 0.02 0.07
Phenol 108-95-2 AP-42 0.0002 0.005 0.02
ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and desaibe how these are monitored and with what frequency; and (3) describe any mon�oring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-179
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Av-Permit to Construct/Operate B
LMISSION SOURCE DESCRIPTION:EMISSION SOURCE ID NO:EG-01
Caterpillar G3516B Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):
0 Coal,wood,oil, gas, other burner (Form B1)0 Woodworking (Form B4)O Manufact. of chemicals/coatings/inks (Form B7)
0 Int.combustion engine/generator (Form B2)0 Coating/finishing/printing (Form B5) 0 Incineration (Form B8)
O Liquid storage tanks (Form B3) 0 Storage silos/bins (Form B6) 0 Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE:November 2018 DATE MANUFACTURED:2016 or Later
MANUFACTURER / MODEL NO.: Caterpillar G3516B EXPECTED OP. SCHEDULE: 100 HRNR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZZZ.
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION:<20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42
PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42
SULFUR DIOXIDE (SO2)AP-42
NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source
(_ 'ARBON MONOXIDE (CO) Mfg
�OLATILE ORGANIC COMPOUNDS (VOC)Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS_SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS / LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Ethylene Dibromide 106-93-4 AP-42 0.0003 0.00002 0.0003 0.00002 0.0003 0.00002
Formaldehyde 50-00-0 AP-42 0.26 0.01 0.26 0.01 0.26 0.01
Hexane (or n-Hexane)110-54-3 AP-42 0.002 0.0001 0.002 0.0001 0.002 0.0001
Methanol 67-56-1 AP-42 0.011 0.0006 0.01 0.0006 0.01 0.0006
Methylene Chloride 75-09-2 AP-42 0.001 0.00003 0.001 0.00003 0.001 0.00003
Naphthalene 91-20-3 AP-42 0.0004 0.00002 0.0004 0.00002 0.0004 0.00002
PAH AP-42 0.0006 0.00003 0.0006 0.00003 0.0006 0.00003
Phenol 108-95-2 AP-42 0.0002 0.00001 0.0002 0.00001 0.0002 0.00001
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Styrene 100-42-5 AP-42 0.0003 0.006 0.03
Toluene 108-88-3 AP-42 0.004 0.11 0.45
Vinyl Chloride 75-01-4 AP-42 0.0001 0.003 0.01
Xylene 1330-20-7 AP-42 0.001 0.03 0.12
ttachments: (1) emissions calculations and supporting documentation; (2)indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and
desclibe how these are monttored and with what frequency; and (3) describe any monitoring devices, gauges, or lest ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-180
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate 8
-.!:MISSION SOURCE DESCRIPTION:EMISSION SOURCE ID NO:EG-01
Caterpillar G3516B Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):
0 Coal,wood,oil, gas, other burner (Form B1)D Woodworking (Form B4)O Manufacl of chemicals/coatingsflnks (Form B7)
0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) 0 Incineration (Form BB)
D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED:2016 or Later
MANUFACTURER / MODEL NO.: Caterpillar G3516B EXPECTED OP. SCHEDULE: 100 HR/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZll.
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION:100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION:<20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFDRMA TIDN FDR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM)Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42
PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42
SULFUR DIOXIDE (SO2)AP-42
NITROGEN OXIDES (NOx)Mfg See Form B, Page 1, for criteria pollutant totals for this source
(_ )ARBON MONOXIDE (CO)Mfg
VOLATILE ORGANIC COMPOUNDS (VOC) Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FDR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS I LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Styrene 100-42-5 AP-42 0.0003 0.00001 0.0003 0.00001 0.0003 0.00001
Toluene 108-88-3 AP-42 0.004 0.0002 0.004 0.0002 0.004 0.0002
Vinyl Chloride 75-01-4 AP-42 0.0001 0.000006 0.0001 0.000006 0.0001 0.000006
Xylene 1330-20-7 AP-42 0.001 0.00006 0.001 0.00006 0.001 0.00006
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FDR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
See Form B, Pages 1-3, for TAP totals for this source
ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) anddescribe how these are monitored and with what frequency; and (3) describe any monitoring devices. gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-181
Attachment F. Air Quality Permit Application Review Documents
FORM B2
EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS)
REVISED 12101/01 NCDENR/Dlvlslon of Air Quality • Application for Air Permit to Construct/Operate I B2
EMISSION SOURCE DESCRIPTION: Caterpillar G3516B Emergency Generator EMISSION SOURCE ID NO: EG-01
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-04
CHECK ALL THAT APPLY 0 EMERGENCY D SPACE HEAT D ELECTRICAL GENERATION
D PEAK SHAVER D OTHER (DESCRIBE):
GENERATOR OUTPUT (KW): 1,300 ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): NIA
ENGINE OUTPUT (HP): 1,818
TYPEICE: 0 GASOLINE ENGINE D DIESEL ENGINE UP TO 800 HP 0 DIESEL ENGINE GREATER THAN 800 HP 0 DUAL FUEL ENGINE
0 OTHER (DESCRIBE): NG SI ICE emergency generator (complete below)
ENGtNE TYPE D RICH BURN 0 LEAN BURN
EMISSION REDUCTION MODIFICATIONS D INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION [,] OTHER Air/fuel ratio
OR STATI0NARY(GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR 0R TURBINE (complete below)
FUEL· 0 NATURAL GAS D OIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN D TURBINE
0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE):
CYCLE: D COGENERATION D SIMPLE CONTROLS: 0 COMBUSTION MODIFICATIONS (DESCRIBE): D REGENERATIVE D COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION D
CONTROLS: 0 WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER 0 UNCONTROLLED 0 D UNCONTROLLED D LEAN-PREMIX
FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL)
MAXIMUM DESIGN REQUESTED CAPACITY
FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR)
Natural Gas MMBtu 14.9 NIA • FUEL CHARACiTERISTICS (C0MPLETE ALL THAl' ARE APPLICABLE)
SULFUR CONTENT
FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT)
Natural Gas 1,020 scf 0.0005
MANUFACTURER'S SPECIFIC EMISSl0N FACT0RS (IF AVAILABLE)
· POLLUTANT NOX co PM PM10 voe OTHER
EMISSION FACTOR g/hp-hr 0.50 2.49 NA NA 0.54
UNIT g/hp-hr g/hp-hr g/hp-hr
DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS:
COMMENTS:
Attach Additional Sheets As Necessary
Page F-182
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B
MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-02
Generac SG100 Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7)
0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage silos/bins (Form B6) D Other (Form B9)
START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Generac SG100 EXPECTED OP. SCHEDULE: 100 HR/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZllZ
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THI$ SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) AP-42 0.052 0.003 0.052 0.003 0.052 0.003
PARTICULATE MA TTER<10 MICRONS (PM10) AP-42 0.052 0.003 0.052 0.003 0.052 0.003
PARTICULATE MATTER<2.5 MICRONS (PM25) AP-42 0.052 0.003 0.052 0.003 0.052 0.003
SULFUR DIOXIDE (SO2) AP-42 0.001 3.18E-05 0.001 3.18E-05 0.001 3.18E-05
NITROGEN OXIDES (NOx) Mfg 0.001 4.92E-05 0.001 4.92E-05 0.001 4.92E-05 C ARBON MONOXIDE (CO) Mfg 0.020 0.001 0.020 0.001 0.020 0.001
/OLATILE ORGANIC COMPOUNDS (VOC) Mfg 0.056 0.003 0.056 0.003 0.056 0.003
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 2.51E-05 1.26E-06 2.51E-05 1.26E-06 2.51E-05 1.26E-06
1, 1,2-Trichloroethane 79-00-5 AP-42 2.00E-05 9.98E-07 2.00E-05 9.98E-07 2.00E-05 9.98E-07
1, 1-Dichloroethane 75-34-3 AP-42 1.48E-05 7.41E-07 1.48E-05 7.41E-07 1.48E-05 7.41E-07
1,2-Dichloroethane 107-06-2 AP-42 1.G0E-05 7.99E-07 1.60E-05 7.99E-07 1.60E-05 7.99E-07
1,2-Dichloropropane 78-87-5 AP-42 1.69E-05 8.45E-07 1.69E-05 8.45E-07 1.69E-05 8.45E-07
1,3-Butadiene 106-99-0 AP-42 3.11E-04 1.55E-05 3.11E-04 1.55E-05 3.11E-04 1.55E-05
1,3-Dichloropropene 542-75-6 AP-42 1.66E-05 8.30E-07 1.66E-05 8.30E-07 1.66E-05 8.30E-07
2,2,4-Trimethylpentane 540-84-1 AP-42 3.21E-04 1.G0E-05 3.21E-04 1.60E-05 3.21E-04 1.60E-05
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
1, 1,2,2-Tetrachloroethane 79-34-5 AP-42 2.51E-05 6.03E-04 0.003
1,2-Dichloroethane 107-06-2 AP-42 1.60E-05 3.84E-04 0.002
1,3-Butadiene 106-99-0 AP-42 3.11E-04 0.007 0.031
Acetaldehyde 75-07-0 AP-42 0.003 0.071 0.294
Acrolein 107-02-8 AP-42 0.003 0.071 0.295
Benzene 71-43-2 AP-42 7.35E-04 0.018 0.073
Benzo(a)pyrene 50-32-8 AP-42 2.15E-09 5.16E-08 2.15E-07
qamoo T �,..,,aid• 56-23-5 AP-42 2.81 E-04 0.001 0.028
llachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable pennit limits (e.g. hours of operation, emission rates) and desclibe ow these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-183
Attachment F. Air Quality Permit Application Review Documents
•
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
REVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Pennit to Construct/Operate B
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-02 Generac SG100 Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERA TING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatingsflnks (Form 87)
0 Int.combustion engine/generator (Form 82) D Coating/finishing/printing (Form 85) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage silos/bins (Form 86) D Other (Form 89)
START CONSTRUCTION DAl April 2011IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Generac SG 100 EXPECTED OP. SCHEDULE: 100 HRNR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZll
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CON'TROLS / LIMITS) (BEFORE CONTROLS/ LIMITS) I (AFTER CON'TROLS / LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM10) Mfg/AP-42
PARTICULATE MATTER<2.5 MICRONS (PM25) Mfg/AP-42
SULFUR DIOXIDE (SO2) AP-42
NITROGEN OXIDES (NOx) Mfg See Fonn B, Page 1, for criteria pollutant totals for this source
CARBON MONOXIDE (CO) Mfg
VOLATILE ORGANIC COMPOUNDS (VOC) Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CON'TROLS / LIMITS) (AFTER CONlROLS / LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Acetaldehyde 75-07-0 AP-42 0.003 1.47E-04 0.003 1.47E-04 0.003 1.47E-04
Acrolein 107-02-8 AP-42 0.003 1.47E-04 0.003 1.47E-04 0.003 1.47E-04
Benzene 71-43-2 AP-42 7.35E-04 3.67E-05 7.35E-04 3.67E-05 7.35E-04 3.67E-05
Biphenyl 92-52-4 AP-42 1.50E-06 7.48E-0B 1.50E-06 7.4BE-0B 1.50E-06 7.4BE-0B
Carbon Tetrachloride 56-23-5 AP-42 2.30E-05 1.15E-06 2.30E-05 1.15E-06 2.30E-05 1.15E-06
Chlorobenzene 108-90-7 AP-42 1.6BE-05 B.41E-07 1.6BE-05 B.41E-07 1.6BE-05 B.41E-07
Chloroform 67-66-3 AP-42 1.78E-05 B.92E-07 1.7BE-05 B.92E-07 1.78E-05 B.92E-07
Ethyl benzene 100-41-4 AP-42 4.09E-05 2.05E-06 4.09E-05 2.05E-06 4.09E-05 2.05E-06
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Chlorobenzene 108-90-7 AP-42 1.68E-05 4.04E-04 0.002
Chloroform 67-66-3 AP-42 1.7BE-05 4.2BE-04 0.002
Ethylene Dibromide 106-93-4 AP-42 3.40E-04 0.008 0.003
Formaldehyde 50-00-0 AP-42 0.021 0.502 2.091
Hexane (or n-Hexane) 110-54-3 AP-42 1.69E-04 0.004 0.017
Methylene Chloride 75-09-2 AP-42 5.57E-05 0.001 0.006
Phenol 108-95-2 AP-42 1.59E-05 3.83E-04 0.002
Attachments (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and descnbe how these are monitored and with what frequency; and (3) describe any monitoring devices gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-184
Attachment F. Air Quality Permit Application Review Documents
•
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
REVISED 12/01/01 NCDENR/Divlsion of Air Quality -Application for Air Permit to Construct/Operate B
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-02
Generac SG100 Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatingsflnks (Form 87)
0 Int.combustion engine/generator (Form 82) D Coaling/finishing/printing (Form 85) D Incineration (Form 88) D Liquid storage tanks (Form 83) D Storage silos/bins (Form 86) D Other (Form B9)
START CONSTRUCTION DAl April 2011IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Generac SG100 EXPECTED OP. SCHEDULE: 100 HR/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZ:ZZ.
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMA T/ON FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS / LIMITS) (BEFORE CONTROLS / LIMITS) I (AFTER CONTROLS / LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42
PARTICULATE MATTER<2 5 MICRONS (PM2 ,l Mfg/AP-42
SULFUR DIOXIDE (SO2) AP-42
NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source
CARBON MONOXIDE (CO) Mfg
VOLATILE ORGANIC COMPOUNDS (VOC) Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS / LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Ethylene Dibromide 106-93-4 AP-42 2.78E-05 1.39E-06 2.78E-05 1.39E-06 2.78E-05 1.39E-06
Formaldehyde 50-00-0 AP-42 0.021 0.001 0.021 0.001 0.021 0.001
Hexane (or n-Hexane) 110-54-3 AP-42 1.69E-04 8.43E-06 1.69E-04 8.43E-06 1.69E-04 8.43E-06
Methanol 67-56-1 AP-42 9.40E-04 4.70E-05 9.40E-04 4.70E-05 9.40E-04 4.70E-05
Methylene Chloride 75-09-2 AP-42 5.57E-05 2.78E-06 5.57E-05 2.7BE-06 5.57E-05 2.78E-06
Naphthalene 91-20-3 AP-42 3.65E-05 1.82E-06 3.65E-05 1.82E-06 3.65E-05 1.82E-06
PAH AP-42 5.08E-05 2.54E-06 5.08E-05 2.54E-06 5.0BE-05 2.54E-06
Phenol 108-95-2 AP-42 1.59E-05 7.97E-07 1.59E-05 7.97E-07 1.59E-05 7.97E-07
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Styrene 100-42-5 AP-42 2.0BE-05 4.9BE-04 0.002
Toluene 108-88-3 AP-42 3.65E-04 0.009 0.036
Vinyl Chloride 75-01-4 AP-42 9.36E-06 2.25E-04 9.36E-04
Xylene 1330-20-7 AP-42 1.02E-04 0.002 0.010
Attachments· (1) emissions calculations and supporting documentation, (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency: and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-185
Attachment F. Air Quality Permit Application Review Documents
•
•
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
REVISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate B
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: EG-02
Generac SG100 Emergency Generator CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05
DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): Natural gas fired emergency generator used to provide power during emergency periods when the primary source of power to the facility is unavailable.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form B7) 0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) D Liquid storage tanks (Form 83) D Storage silos/bins (Form B6) D Other (Form B9)
START CONSTRUCTION DAl April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Generac SG100 EXPECTED OP. SCHEDULE: 100 HRMR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Yes, JJJJ NESHAP (SUBPART?): No MACT (SUBPART?): Yes, ZZZZ
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 100 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS / LIMITS) I (AFTER CONTROLS / LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) Mfg/AP-42
PARTICULATE MATTER<10 MICRONS (PM,0) Mfg/AP-42
PARTICULATE MATTER<2 5 MICRONS (PM2 s) Mfg/AP-42
SULFUR DIOXIDE (SO2) AP-42
NITROGEN OXIDES (NOx) Mfg See Form B, Page 1, for criteria pollutant totals for this source
CARBON MONOXIDE (CO) Mfg
VOLATILE ORGANIC COMPOUNDS (VOC) Mfg
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Styrene 100-42-5 AP-42 2.08E-05 1.04E-06 2.08E-05 1.04E-06 2.08E-05 1.04E-06
Toluene 108-88-3 AP-42 3.65E-04 1.82E-05 3.65E-04 1.82E-05 3.65E-04 1.82E-05
Vinyl Chloride 75-01-4 AP-42 9.36E-06 4.68E-07 9.36E-06 4.68E-07 9.36E-06 4.68E-07
Xylene 1330-20-7 AP-42 1.02E-04 5.08E-06 1.02E-04 5.08E-06 1.02E-04 5.08E-06
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
See Form B, Pages 1-3, for TAP totals for this source
Attachments: (1) emissions calculations and supporting documentation: (2) indicate all requested state and federal enforceable permit limits (e g hours of operation, emission rates) and describe how these are monitored and with what frequency, and (3) describe any monitoring de111ces, gauges, or test ports for this souru
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-186
Attachment F. Air Quality Permit Application Review Documents
FORM B2
EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS)
REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality· Application for Air Permit to Construct/Operate I 82
EMISSION SOURCE DESCRIPTION: Generac SG100 Emergency Generator EMISSION SOURCE ID NO: EG-02
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-05
CHECK ALL THAT APPLY 0 EMERGENCY D SPACE HEAT D ELECTRICAL GENERATION
D PEAK SHAVER D OTHER (DESCRIBE):
GENERATOR OUTPUT (KW): 100 ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR): NIA
ENGINE OUTPUT (HP): 148.9
TYPE ICE: 0 GASOLINE ENGINE D DIESEL ENGINE UP TO 600 HP D DIESEL ENGINE GREATER THAN 600 HP D DUAL FUEL ENGINE
0 OTHER (DESCRIBE) NG SI ICE emergency generator -(complete below)
ENGINE TYPE D RICH BURN D LEAN BURN
EMISSION REDUCTION MODIFICATIONS 0 INJECTION TIMING RETARD D PREIGNITION CHAMBER COMBUSTION 0 OTHER Air/fuel ratio
OR STATIONARY GAS TURBINE (complete below) NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below)
FUEL O NATURAL GAS D OIL ENGINE TYPE: 0 2-CYCLE LEAN BURN 0 4-CYCLE LEAN D TURBINE
0 OTHER (DESCRIBE): 0 4-CYCLE RICH BURN 0 OTHER (DESCRIBE):
CYCLE: D COGENERATION D SIMPLE K;ONTROLS: O COMBUSTION MODIFICATIONS (DESCRIBE): D REGENERATIVE D COMBINED NONSELECTIVE CATALYTIC REDUCTION 0 SELECTIVE CATALYTIC REDUCTION 0
CONTROLS: D WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER 0 UNCONTROLLED 0D UNCONTROLLED D LEAN-PREMIX
FlJEL USAGE (INCLUDE STARTUP/BACKUP FUEL)
MAXIMUM DESIGN REQUESTED CAPACITY
FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR)
Natural Gas cf/hr 1116.0 N/A
FUEL CHARACTERISTICS (COMPLETE ALL THAl' ARE APPLICABLE)
SULFUR CONTENT
FUEL TYPE BTU/UNIT UNITS (% BY WEIGHT)
Natural Gas 1,020 scf 0.0005
MANUFACTURER'S SPECIFIC l;_�l�SION FACTORS (IF AVAILABLE)
POLLUTANT NOX co PM PM10 voe OTHER
EMISSION FACTOR g/hp-hr 0.003 0.06 NA NA 0.17
UNIT g/hp-hr g/hp-hr g/KW-hr
DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS:
COMMENTS:
Attach Additional Sheets As Necessary
Page F-187
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: WH-01 Hurst LPW-G-125-60W Hot Water Boiler CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-06 DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS {ATTACH FLOW DIAGRAM): Natural gas fired hot water boiler used to provide building heat
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) D Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form B8) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DATE: April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: Hurst LPW-G-125-60W EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE;_ SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) AP-42 0.039 0.171 0.039 0.171 0.039 0.171 PARTICULATE MATTER<10 MICRONS (PM10) AP-42 0.039 0.171 0.039 0.171 0.039 0.171 PARTICULATE MATTER<2.5 MICRONS (PM25) AP-42 0.039 0.171 0.039 0.171 0.039 0.171 SULFUR DIOXIDE (SO2) AP-42 0.003 0.014 0.003 0.014 0.003 0.014 NITROGEN OXIDES (NOx) AP-42 0.257 1.13 0.257 1.13 0.257 1.13 C""-ARBON MONOXIDE (CO) AP-42 0.432 1.89 0.432 1.89 0.432 1.89 JOLATILE ORGANIC COMPOUNDS (VOC) AP-42 0.028 0.124 0.028 0.124 0.028 0.124 LEAD OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMA T/ON FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr Benzene 71-43-2 AP-42 1.08E-05 4.73E-05 1.08E-05 4.73E-05 1.08E-05 4.73E-05 Dichlorobenzene 106-46-7 AP-42 6.18E-06 2.71E-05 6.18E-06 2.71E-05 6.18E-06 2.71E-05 Formaldehyde 50-00-0 AP-42 3.86E-04 0.002 3.86E-04 0.002 3.86E-04 0.002 Hexane (or n-Hexane) 110-54-3 AP-42 0.009 0.041 0.009 0.041 0.009 0.041 Naphthalene 91-20-3 AP-42 3.14E-06 1.38E-05 3.14E-06 1.38E-05 3.14E-06 1.38E-05 Toluene 108-88-3 AP-42 1.75E-05 7.67E-05 1.75E-05 7.67E-05 1.75E-05 7.67E-05 Arsenic Compounds AP-42 1.03E-06 4.51E-06 1.03E-06 4.51E-06 1.03E-06 4.51E-06 Beryllium 7440-41-7 AP-42 6.18E-08 2.71E-07 6.18E-08 2.71E-07 6.18E-08 2.71E-07
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE -INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr Benzene 71-43-2 AP-42 1.08E-05 2.59E-04 0.095 Dichlorobenzene 106-46-7 AP-42 6.18E-06 1.48E-04 0.054 Formaldehyde 50-00-0 AP-42 3.86E-04 0.009 3.38 Hexane (or n-Hexane) 110-54-3 AP-42 0.009 0.222 81.2 Toluene 108-88-3 AP-42 1.75E-05 4.20E-04 0.153 Arsenic Compounds AP-42 1.03E-06 2.47E-05 0.009 Beryllium 7440-41-7 AP-42 6.18E-08 1.48E-06 5.41E-04
qoom;,m 7440-4�9 AP-42 5.06E-OB 1.36E-04 0.050 ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe ow these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-188
Attachment F. Air Quality Permit Application Review Documents
•
•
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality. Application for Air Permit to Construct/Operate B
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: WH-01
Hurst LPW-G-125-60W Hot Water Boiler CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): EP-06
DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Natural gas fired hot water boiler used to provide building heat
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES):
0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7) D Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form 88) D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: Hurst LPW-G-125-60W EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: <20 % OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS / LIMITS) I (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) AP-42
PARTICULATE MATTER<10 MICRONS (PM10) AP-42
PARTICULATE MATTER<2.5 MICRONS (PM,.) AP-42
SULFUR DIOXIDE (SO2) AP-42
NITROGEN OXIDES (NOx) AP-42 See Form B, Page 1, for criteria pollutant totals for this source
CARBON MONOXIDE (CO) AP-42
VOLATILE ORGANIC COMPOUNDS (VOC) AP-42
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSStONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS / LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Cadmium 7440-43-9 AP-42 5.66E-06 2.48E-05 5.66E-06 2.48E-05 5.66E-06 2.48E-05
Chromium Compounds AP-42 7.21E-06 3.16E-05 7.21E-06 3.16E-05 7.21E-06 3.16E-05
Cobalt 7440-48-4 AP-42 4.32E-07 1.89E-06 4.32E-07 1.89E-06 4.32E-07 1.89E-06
Manganese Compounds AP-42 1.96E-06 8.57E-06 1.96E-06 8.57E-06 1.96E-06 8.57E-06
Mercury 7439-97-6 AP-42 1.34E-06 5.86E-06 1.34E-06 5.86E-06 1.34E-06 5.86E-06
Nickel 7440-02-0 AP-42 1.0BE-05 4.73E-05 1.08E-05 4.73E-05 1.08E-05 4.73E-05
Selenium 7782-49-2 AP-42 1.24E-07 5.41E-07 1.24E-07 5.41E-07 1.24E-07 5.41E-07
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Chromium Compounds AP-42 7.21E-06 1.73E-04 0.063
Manganese Compounds AP-42 1.96E-06 4.69E-05 0.017
Mercury 7439-97-6 AP-42 1.34E-06 3.21E-05 0.012
Nickel 7440-02-0 AP-42 1.08E-05 2.59E-04 0.095
Attachments: (1) emissions calculations and supporting documentation, (2) indicate aK requested state and federal enforceable pelTTl� lim�s (e g. hours of operahon, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitonng devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-189
Attachment F. Air Quality Permit Application Review Documents
FORM 81
EMISSION SOURCE (WOOD, COAL, OIL, GAS, OTHER FUEL-FIRED BURNER)
REVISED 09/22/16 NCDEQ/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I 81
EMISSION SOURCE DESCRIPTION: Hurst LPW-G-125-60W Hot Water Boiler EMISSION SOURCE ID NO: WH-01
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO: 1 OF 1 EMISSION POINT (STACK) ID NO(S): EP-06
DESCRIBE USE: PROCESS HEAT X SPACE HEAT ELECTRICAL GENERATION
CONTINUOUS USE STAND BY/EMERGENCY OTHER (DESCRIBE):
HEATING MECHANISM: X INDIRECT DIRECT
MAX. FIRING RATE (MMBTU/HOUR): 5.25
WOOD-FIRED BURNER
WOOD TYPE: BARK WOOD/BARK WET WOOD DRY WOOD OTHER (DESCRIBE):
PERCENT MOISTURE OF FUEL:
UNCONTROLLED CONTROLLED WITH FL YASH REINJECTION CONTROLLED W/O REINJECTION
FUEL FEED METHOD: EAT TRANSFER MEDIA: STEAM AIR OTHER (DESCRIBE)
COAL-FIRED BURNER �
TYPE OF BOILER IF OTHER DESCRIBE:
PULVERIZE[ OVERFEED STOKER UNDERFEED STOKER SPREADER STOKER FLUIDIZED BED
0WET BED UNCONTROLLED UNCONTROLLED UNCONTROLLED CIRCULATING
0DRY BED CONTROLLED CONTROLLED FL YASH REINJECTION RECIRCULATING
NO FLYASH REINJECTION • OIUGAS-FIRED BURNER
TYPE OF BOILER: UTILITY INDUSTRIAL x COMMERCIAL INSTITUTIONAL
TYPE OF FIRING: NORMAL TANGENTIAL x LOW NOX BURNERS NO LOW NOX BURNER
OTHER FUEL-FIRED BURNER
TYPE(S) OF FUEL:
TYPE OF BOILER: UTILITY INDUSTRIAL COMMERCIAL INSTITUTIONAL
TYPE OF FIRING: TYPE(S) OF CONTROL(S) (IF ANY):
FUEL USAGE (INCLUDE STARTUP/BACKUP FUELS)
MAXIMUM DESIGN REQUESTED CAPACITY
FUEL TYPE UNITS CAPACITY (UNIT/HR) LIMITATION (UNIT/HR)
Natural Gas set 5,147 5,147
FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE)
SPECIFIC SULFUR CONTENT ASH CONTENT
FUEL TYPE BTU CONTENT (% BY WEIGHT) (% BY WEIGHT)
Natural Gas 1020/scf 0.0005 0
COMMENTS:
Attach Additional Sheets As Necessary
Page F-190
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) ISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: TK-1 TK-1 Pipeline Liquids Storage Tank CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): TK-1 will have a capacity of 1,000 gallons and will receive liquids from the compressor engine fluids filter.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) 0 Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form 87) 0 Int.combustion engine/generator (Form B2) O Coating/finishing/printing (Form 85) O Incineration (Form 88) 0 Liquid storage tanks (Form 83) O Storage silos/bins (Form 86) D Other (Form 89) START CONSTRUCTION DAl April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/INK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE �
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) ---- ---PARTICULATE MATTER<10 MICRONS (PM10) -------PARTICULATE MATTER<2.5 MICRONS (PM,,) -------SULFUR DIOXIDE (SO2) -------NITROGEN OXIDES (NOx) -------( ')RBON MONOXIDE (CO) -------,.,fQLATILE ORGANIC COMPOUNDS (VOC) Mass balance 0.033 0.145 0.033 0.145 0.033 0.145 LEAD OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS I LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
NA
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT ANO CAS NO. EF SOURCE lb/hr lb/day lb/yr NA
Qchments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limijs (e.g. hours of operation, emission rates) and describe these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-191
Attachment F. Air Quality Permit Application Review Documents
FORM 83
EMISSION SOURCE (LIQUID STORAGE TANK)
Q REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Alr Permit to Construct/Operate I B3
EMISSION SOURCE DESCRIPTION: Pipeline liquids Storage Tank EMISSION SOURCE ID NO: TK-1
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
EACH STORAGE TANK
DESCRIBE IN DETAIL THE STORAGE TANK (ATTACH FLOW DIAGRAM): TK-1 will have a capacity of 1,000 gallons and will receive liquids from the compressor engine fluids filter.
LIQUID STORED: Liquids from compressor engine fluids filter LIQUID MOLECULAR WEIGHT (LB/LB-MOLE): TBD
TANK CAPACITY (GAL): 1,000 VAPOR MOLECULAR WEIGHT (LB/LB-MOLE): TBD
AVERAGE LIQUID SURFACE TEMPERATURE (F): 77 VAPOR PRESSURE AT AVE. LIQUID SURFACE TEMP (PSIA): 7.70 (Reid)
MIN. LIQUID SURFACE TEMP (F): 44 MAX. LIQUID SURFACE TEMP (F): BO MAX. TRUE VAPOR PRESS. (PSIA): 7.70 (Reid)
BULK LIQUID TEMPERATURE (F): BREATHER VENT SETTINGS (PSIG) __ VACUUM __ PRESSURE
SHELL DIAMETER (FT): 4.12 SHELL CONDITION: X GOOD POOR IS TANK HEATED: YES X NO
SHELL COLOR: Grey/light MAXIMUM THROUGHPUT (GAL/YR): 5,000 MAXIMUM TURNOVERS PER YEAR: 5.00
WORKING VOLUME (GAL): 1,000 ACTUAL THROUGHPUT (GAL/YR): 5,000 ACTUAL TURNOVERS PER YEAR: 5.00
MAX. FILLS PER DAY: TBD MAX. FILLING RATE (GAUMIN): TBD MIN. DURATION OF FILL (HR/FILL): TBD
VERTICAL FIXED ROOF TANKS
SHELL HEIGHT (FT): 10 ROOF TYPE: X CONE OR DOME IROOF HEIGHT (FT): 4.12
AVERAGE LIQUID HEIGHT (FT): 5 ROOF CONDITION: X GOOD OR POOR
MAXIMUM LIQUID HEIGHT (FT): 10 ROOF COLOR: Grey
HORIZONTAL TANKS 0 SHELL LENGTH (FT): NA IS TANK UNDERGROUND?: YES X NO
FLOATING ROOF TANKS
DESCRIBE PERTINENT TANK DATA SUCH AS DECKS, RIM-SEALS, LIQUID DENSITY@ 60 DEG F:
NA
DESCRIBE ANY MONITORING OR WARNING DEVICES (SUCH AS LEAK AND FUME DETECTION INSTRUMENTATION):
NA
COMMENTS:
()
Attach Additional Sheets As Necessary
Page F-192
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
ISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B
ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: TK-2
TK-2 Hydrocarbon Waste Tank CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
TK-2 will have a capacity of 2,500 gallons and will store waste oil.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES): D Coal,wood,oil, gas, other burner (Form 81) D Woodworking (Form 84) D Manufact. of chemicals/coatings/inks (Form 87) D Int.combustion engine/generator (Form 82) D Coating/finishing/printing (Form 85) D Incineration (Form BB) 0 Liquid storage tanks (Form 83) D Storage silos/bins (Form 86) D Other (Form 89)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) -------
PARTICULATE MATTER<10 MICRONS (PM 10) -------
PARTICULATE MATTER<2.5 MICRONS (PM25) -------
SULFUR DIOXIDE (SO2) -------
NITROGEN OXIDES (NOx) -------
( \RBON MONOXIDE (CO)-------
-(QLATILE ORGANIC COMPOUNDS (VOC) Mass balance 5.01E-06 2.19E-05 5.01E-06 2.19E-05 5.01E-06 2.19E-05
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
NA
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
NA
Q.achments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe w these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-193
Attachment F. Air Quality Permit Application Review Documents
FORM 83
EMISSION SOURCE (LIQUID STORAGE TANK) C REVISED 12/01/01 NCDENR/Division of Air Quality -Appl ication for Air Permit to Construct/Operate I B3
EMISSION SOURCE DESCRIPTION: Hydrocarbon Waste Tank EMISSION SOURCE ID NO: TK-2
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
EACH STORAGE TAN�
DESCRIBE IN DETAIL THE STORAGE TANK (ATTACH FLOW DIAGRAM): TK-2 will have a capacity of 1,000 gallons and will store waste oil.
LIQUID STORED: Waste Oil LIQUID MOLECULAR WEIGHT (LB/LB-MOLE): TBD
TANK CAPACITY (GAL): 2,500 VAPOR MOLECULAR WEIGHT (LB/LB-MOLE): TBD
AVERAGE LIQUID SURFACE TEMPERATURE (F): 77 VAPOR PRESSURE AT AVE. LIQUID SURFACE TEMP (PSIA): 0.0001
MIN. LIQUID SURFACE TEMP (F): 44 MAX. LIQUID SURFACE TEMP (F): BO MAX. TRUE VAPOR PRESS. (PSIA): 0.0001
BULK LIQUID TEMPERATURE (F): BREATHER VENT SETTINGS (PSIG) __ VACUUM __ PRESSURE Default Tanks 4.09d settings
SHELL DIAMETER (FT): 4.6 SHELL CONDITION: X GOOD POOR IS TANK HEATED: YES X NO
SHELL COLOR: Grey/Light MAXIMUM THROUGHPUT (GAL/YR): 12,500 MAXIMUM TURNOVERS PER YEAR: 5.00
WORKING VOLUME (GAL): 2,500 ACTUAL THROUGHPUT (GAL/YR): 12,500 ACTUAL TURNOVERS PER YEAR: 5.00
MAX. FILLS PER DAY: TBD MAX. FILLING RATE (GAUMIN): TBD MIN. DURATION OF FILL (HR/FILL): TBD
VERTICAL FIXED ROOF TANKS
SHELL HEIGHT (FT): 20 ROOF TYPE: X CONE OR DOME IROOF HEIGHT (FT): 4.6
AVERAGE LIQUID HEIGHT (FT): 10 ROOF CONDITION: X GOOD OR POOR
MAXIMUM LIQUID HEIGHT (FT): 20 ROOF COLOR: Grey
HORIZONTAL TANKS C SHELL LENGTH (FT): NA IS TANK UNDERGROUND?: YES X NO
FLOATING ROOF TANKS
DESCRIBE PERTINENT TANK DATA SUCH AS DECKS, RIM-SEALS, LIQUID DENSITY@ 60 DEG F:
NA
DESCRIBE ANY MONITORING OR WARNING DEVICES (SUCH AS LEAK AND FUME DETECTION INSTRUMENTATION):
NA
COMMENTS:
C
Attach Additional Sheets As Necessary
Page F-194
Attachment F. Air Quality Permit Application Review Documents
FORMS
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES) ISED 12/01/01 NCDENR/Division of Air Quality. Application for Air Permit to Construct/Operate B ISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: TK-3 TK-3 Ammonia Tank CONTROL DEVICE ID NO(S): NA OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM): TK-3 will have a capacity of 13,400 gallons and will store aqueous ammonia.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM 81-89 ON THE FOLLOWING PAGES): 0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatingsflnks (Form B7) D Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB) 0 Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) D Other (Form B9) START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25 EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS I LIMITS) (AFTER CONTROLS/ LIMITS) AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr PARTICULATE MATTER (PM) -------PARTICULATE MATTER<1D MICRONS (PM10) -------PARTICULATE MATTER<2.5 MICRONS (PM25) --. ----SULFUR DIOXIDE (SO2) -------NITROGEN OXIDES (NOx) ---. ---( \RBON MONOXIDE (CO) -. ------1tJLATILE ORGANIC COMPOUNDS (VOC) ---. ---LEAD OTHER -·HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS) HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr NA
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr Ammonia Eng. Data Neg. Neg. Neg.
Qachmenls: (1) emissions calculations and supporting documenlalion; (2) indicate all requested slate and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe w these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or lest ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-195
Attachment F. Air Quality Permit Application Review Documents
FORM 83
EMISSION SOURCE (LIQUID STORAGE TANK) C REVISED 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate I 83
EMISSION SOURCE DESCRIPTION: Ammonia Tank EMISSION SOURCE ID NO: TK-3
CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
EACH STORAGE TANK '
DE-,1.,RIBE IN Dl:TAIL THE STORAGE TANK (ATTACH FLOW DIAGRAM): TK-3 will have a capacity of 13,000 gallons and store aqueous ammonia.
LIQUID STORED: Aqueous ammonia LIQUID MOLECULAR WEIGHT (LB/LB-MOLE): TBD
TANK CAPACITY (GAL): 13,400 VAPOR MOLECULAR WEIGHT (LB/LB-MOLE): TBD
AVERAGE LIQUID SURFACE TEMPERATURE (F): NA VAPOR PRESSURE AT AVE. LIQUID SURFACE TEMP (PSIA): NA
MIN. LIQUID SURFACE TEMP (F): NA MAX. LIQUID SURFACE TEMP (F): NA MAX. TRUE VAPOR PRESS. (PSIA): NA
BULK LIQUID TEMPERATURE (F): BREATHER VENT SETTINGS (PSIG) __ VACUUM __ PRESSURE
SHELL DIAMETER (FT): 8.2 SHELL CONDITION: X GOOD POOR IS TANK HEATED: YES X NO
SHELL COLOR: Grey/Light MAXIMUM THROUGHPUT (GAL/YR): NA MAXIMUM TURNOVERS PER YEAR: NA
WORKING VOLUME (GAL): 13,400 ACTUAL THROUGHPUT (GAL/YR): NA ACTUAL TURNOVERS PER YEAR: NA
MAX. FILLS PER DAY: NA MAX. FILLING RATE (GAUMIN): NA MIN. DURATION OF FILL (HR/FILL): NA
VERTICAL FIXED ROOF TANKS
SHELL HEIGHT (FT): ROOF TYPE: X CONE OR DOME IRoOF HEIGHT (FT):
AVERAGE LIQUID HEIGHT (FT): ROOF CONDITION: X GOOD OR POOR
MAXIMUM LIQUID HEIGHT (FT): ROOF COLOR: Grey
HORIZONTAL TANKS C SHELL LENGTH (FT): 32.9 IS TANK UNDERGROUND?: YES X NO
FLOATING ROOF TANKS
DESCRIBE PERTINENT TANK DATA SUCH AS DECKS, RIM-SEALS, LIQUID DENSITY@ 60 DEG F:
NA
DESCRIBE ANY MONITORING OR WARNING DEVICES (SUCH AS LEAK AND FUME DETECTION INSTRUMENTATION):
NA
COMMENTS:
0
Attach Additional Sheets As Necessary
Page F-196
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B
)MISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-01
Fugitive Leaks -Slowdowns CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Fugitive Emissions from station blowdowns.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):
0 Coal,wood,oil, gas, other burner (Form 81) 0 Woodworking (Form 84) O Manufact. of chemicals/coatings/inks (Form 87)
0 Int.combustion engine/generator (Form 82) 0 Coating/finishing/printing (Form 85) 0 Incineration (Form 88)
D Liquid storage tanks (Form 83) 0 Storage silos/bins (Form 86) 0 other (Form 89)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NO V 25
EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) . --. . . -
PARTICULATE MATTER<10 MICRONS (PM,0) . . -. . -.
PARTICULATE MATTER<2.5 MICRONS (PM25) . -. . -. -
SULFUR DIOXIDE (SO2) -. -. . . -
NITROGEN OXIDES (NOx) . . -. . -. l )ARBON MONOXIDE (CO) -. -. . -.
'{loLATILE ORGANIC COMPOUNDS (VOC) Mass balance 4.30 18.84 4.30 18.84 4.30 18.84
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Hexane 110-54-3 Mass balance 0.24 1.06 0.24 1.06 0.24 1.06
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Hexane 110-54-3 Mass balance 0.24 5.81 2120.00
l!achments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and
describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-197
Attachment F. Air Quality Permit Application Review Documents
•
FORM 89
EMISSION SOURCE (OTHER)
REVISED: 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate I
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-01
Fugttive Leaks -Slowdowns CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO: 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM):
Fugttive Emissions from station btowdowns.
MATERIALS ENTERING PROCESS -CONTINUOUS PROCESS MAX. DESIGN REQUESTED CAPACITY
TYPE UNITS �PACITY (UNIT/� LIMITATION(UNIT/HR)
Natural gas NA NA NA
MATERIALS ENTERING PROCESS • BATCH OPERATION MAX.DESIGN REQUESTED CAPACITY
TYPE UNITS l>ACITY (UNIT/BA LIMITATION (UNIT/BATCH)
NA
MAXIMUM DESIGN (BATCHES / HOUR): NA
REQUESTED LIMITATION (BATCHES / HOUR): NA (BATCHES/YR): NA
FUEL USED: NA TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): NA
MAX. CAPACITY HOURLY FUEL USE: NA REQUESTED CAPACITY ANNUAL FUEL USE: NA
COMMENTS:
Attach Additional Sheets as Necessary
B9
Page F-198
Attachment F. Air Quality Permit Application Review Documents
FORMB
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
EVISED 12/01/01 NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate B
,,EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-02
Fugitive Leaks -Piping CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAIL THE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Fugitive Emissions from station piping leaks.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):
0 Coal,wood,oil, gas, other burner (Form B1) D Woodworking (Form B4) D Manufact. of chemicals/coatings/inks (Form B7)
0 Int.combustion engine/generator (Form B2) D Coating/finishing/printing (Form B5) D Incineration (Form BB)
D Liquid storage tanks (Form B3) D Storage silos/bins (Form B6) 0 Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) - ------
PARTICULATE MATTER<10 MICRONS (PM10) -------
PARTICULATE MATTER<2.5 MICRONS (PM25) -------
SULFUR DIOXIDE (S02) -------
NITROGEN OXIDES (NOx)-------l \ARBON MONOXIDE (CO) -------
\/OLATILE ORGANIC COMPOUNDS (VOC) EPA 0.080 0.352 0.080 0.352 0.080 0.352
LEAD
OTHER
HAZARDQUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Hexane 110-54-3 Mass Balance 0.005 0.020 0.005 0.020 0.005 0.020
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Hexane 110-54-3 Mass Balance 0.005 0.110 40.0
,ttachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-199
Attachment F. Air Quality Permit Application Review Documents
•
FORM B9
EMISSION SOURCE (OTHER)
REVISED: 12/01/01 NCDENR/Dlvlslon of Air Quality. Application for Air Permit to Construct/Operate I
EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fug-02
Fugitive Leaks -Piping CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO: 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM):
Fugitive Emissions from station piping leaks.
MATERIALS ENTERING PROCESS -CONTINUOUS PROCESS MAX. DESIGN REQUESTED CAPACITY
TYPE UNITS iAPACITY (UNIT/I-LIMITATION(UNIT/HR)
Natural gas NA NA NA
MATERIALS ENTERING PROCESS -BATCH OPERATION MAX. DESIGN REQUESTED CAPACITY
TYPE UNITS �ACITY (UNIT/BA LIMITATION (UNIT/BATCH) NA
MAXIMUM DESIGN (BATCHES / HOUR): NA
REQUESTED LIMITATION (BATCHES / HOUR): NA (BATCHES/YR): NA
FUEL USED: NA TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): NA
MAX. CAPACITY HOURLY FUEL USE: NA REQUESTED CAPACITY ANNUAL FUEL USE: NA
COMMENTS:
Attach Additional Sheets as Necessary
B9
Page F-200
Attachment F. Air Quality Permit Application Review Documents
FORM D1
FACILITY-WIDE EMISSIONS SUMMARY
(1EVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate
CRITERIA AIR POLLUTANT EMISSIONS INFORIVIATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS /
LIMITATIONS) LIMITATIONS)
AIR POLLUTANT EMITTED tons/yr tons/yr
PARTICULATE MATTER (PM) 18.3 18.3
PARTICULATE MATTER< 10 MICRONS (PM,0) 18.3 18.3
PARTICULATE MATTER< 2.5 MICRONS (PM25) 18.3 18.3
SULFUR DIOXIDE (SO2) 3.10 3.10
NITROGEN OXIDES (NOx) 19.2 47.5
CARBON MONOXIDE (CO) 31.0 84.9
VOLATILE ORGANIC COMPOUNDS (VOC) 21.2 22.7
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS I (BEFORE CONTROLS I
LIMITATIONS) LIMITATIONS)
HAZARDOUS AIR POL LUTANT EMITTED CAS NO. tons/yr tons/yr
1, 1,2,2-Tetrachloroethane 79.34.5 1.66E-05 1.66E-05
1, 1,2-Trichloroethane 79-00-5 1.32E-05 1.32E-05
1, 1-Dichloroethane 75-34-3 9.78E-06 9.78E-06
1,2-Dichloroethane 107-06-2 1.06E-05 1.06E-05
1,2-Dichloropropane 78-87-5 1.12E-05 1.12E-05
1,3-Butadiene 106-99-0 3.69E-04 5.33E-04 l "'\3-Dichloropropene 542-75-6 1.10E-05 1.10E-05
'1,2,4-Trimethylpentane 540-84-1 2.12E-04 2.12E-04
Aceta ldehyde 106-99-0 0.017 0.032
Acrolein 75-07-0 0.004 0.007
Benzene 71-43-2 0.005 0.010
Biphenyl 92-52-4 9.88E-07 9.88E-07
Carbon Tetrachloride 56-23-5 1.52E-05 1.52E-05
TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
D1
POTENTIAL EMISSIONS
(AFTER CONTROLS /
LIMITATIONS)
tons/yr
18.3
18.3
18.3
3.10
19.2
31.0
21.2
POTENTIAL EMISSIONS
(AFTER CONTROLS I
LIMITATIONS)
tons/yr
1.66E-05
1.32E-05
9.78E-06
1.06E-05
1.12E-05
3.69E-04
1.10E-05
2.12E-04
0.017
0.004
0.005
9.88E-07
1.52E-05
INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15A NCAC 2Q
.0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY.
Modeling Required ? Note
TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No 1
1, 1,2,2-Tetrachloroethane 79-34-5 3.32E-04 0.008 0.033 X 1
1,2-Dichloroethane 107-06-2 1.97E-04 0.005 0.021 X 1
1,3-Butadiene 106-99-0 0.004 0.099 0.739 X 1
Acetaldehyde 75-07-0 0.042 1.02 34.4 X 1
Acrolein 75-07-0 0.039 0.948 8.78 X 1
Ammonia 7664-41-7 2.83 67.9 24,773 X 1
Benzene 71-43-2 0.011 0.258 10.2 X 1
Benzo(a)pyrene 50-32-8 2.84E-08 6.82E-07 2.84E-06 X 1
Carbon Tetrachloride 56-23-5 5.62E-04 0.013 0.030 X 1
Chlorobenzene 108-90-7 2.22E-04 0.005 0.022 X 1
Chloroform 67-66-3 2.36E-04 0.006 0.024 X 1
Dichlorobenzene 106-46-7 6.18E-06 1.48E-04 0.054 X 1
Ethylene Dibromide 106-93-4 6.79E-04 0.016 0.037 X 1 c"(ormaldehyde 50-00-0 0.528 12.7 2,229 X 1
Aexane (or n-Hexane) 110-54-3 0.258 6.2 2,241 X 1
COMMENTS:
Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC
02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these sources Is less than 450 MMBtu/hr, and they will be the only source of benzene at the facility.
Page F-201
Attachment F. Air Quality Permit Application Review Documents
FORM D1
FACILITY-WIDE EMISSIONS SUMMARY
Q REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality. Application for Alr Permit to Construct/Operate D1
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS / (AFTER CONTROLS /
LIMITATIONS) LIMITATIONS) LIMITATIONS)
AlR POLLUTANT EMITTED tons/yr tons/yr tons/yr
PARTICULATE MATTER (PM)
PARTICULATE MATTER< 10 MICRONS (PM10)
PARTICULATE MATTER< 2.5 MICRONS (PM2 5)
SULFUR DIOXIDE (SO2)
NITROGEN OXIDES (NOx) See Form D1, Page 1, for criteria pollutant totals.
CARBON MONOXIDE (CO)
VOLATILE ORGANIC COMPOUNDS (VOC)
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS I (AFTER CONTROLS /
LIMITATIONS) LIMITATIONS) LIMITATIONS)
HAZARDOUS AIR POLLUTANT EMITTED CAS NO. tons/yr tons/yr tons/yr
Chlorobenzene 108-90-7 1.11 E-05 1.11E-05 1.11E-05
Chloroform 67-66-3 1.18E-05 1.18E-05 1.18E-05
Dichlorobenzene 106-46-7 2.71E-05 2.71 E-05 2.71E-05
Ethyl benzene 100-41-4 0.012 0.024 0.012
Ethylene Dibromide 106-93-4 1.84E-05 1.84E-05 1.84E-05 n Formaldehyde 75-07-0 1.11 2.21 1.11
Hexane (or n-Hexane) 110-54-3 1.12 1.12 1.12
Methanol 67-56-1 6.21E-04 6.21E-04 6.21E-04
Methylene Chloride 75-09-2 3.68E-05 3.68E-05 3.68E-05
Napthalene 91-20-3 5.34E-04 0.001 5.34E-04
PAH 8.73E-04 0.002 8.73E-04
Phenol 108-95-2 1.05E-05 1.05E-05 1.05E-05
Propylene oxide 75-56-9 0.011 0.022 0.011
Styrene 100-42-5 1.37E-05 1.37E-05 1.37E-05
Toluene 108-88-3 0.050 0.100 0.050
TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15A
NCAC 2Q .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY.
Modeling Required ? Note
TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No 1
Methylene Chloride 75-09-2 7.36E-04 0.018 0.074 X 1
Phenol 108-95-2 2.11E-04 0.005 0.021 X 1
Styrene 100-42-5 2.74E-04 0.007 0.027 X 1
Toluene 108-88-3 0.016 0.388 99.8 X 1
Vinyl Chloride 75-01-4 1.24E-04 0.003 0.012 X 1
Xylene 1330-20-7 0.007 0.166 49.0 X 1
• COMMENTS:
Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A
NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat Input value for these sources is less than 450 MMBtu/hr, and they will be the only source
of benzene at the facility.
Page F-202
Attachment F. Air Quality Permit Application Review Documents
FORM D1
FACILITY-WIDE EMISSIONS SUMMARY r REVISED 12/01/01 NCDENR/Dlvision of Air Quality -Application for Air Permit to Construct/Operate D1
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS/ (BEFORE CONTROLS/ (AFTER CONTROLS/
LIMITATIONS) LIMITATIONS) LIMITATIONS)
AIR POLLUTANT EMITTED tons/yr tons/yr tons/yr
PARTICULATE MATTER (PM)
PARTICULATE MATTER< 10 MICRONS (PM10)
PARTICULATE MATTER< 2.5 MICRONS (PM25)
SULFUR DIOXIDE (SO2)
NITROGEN OXIDES (NOx) See Form D1, Page 1, for criteria pollutant totals.
CARBON MONOXIDE (CO)
VOLATILE ORGANIC COMPOUNDS (VOC)
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS/ (AFTER CONTROLS/
LIMITATIONS) LIMITATIONS) LIMITATIONS)
HAZARDOUS AIR POLLUTANT EMITTED CAS NO. tons/yr tons/yr tons/yr
Vinyl Chloride 75-01-4 6.18E-06 6.18E-06 6.18E-06
Xylene 1330-20-7 0.024 0.049 0.024
Arsenic Compounds 4.51E-06 4.51E-06 4.51E-06
Beryllium 7440-41-7 2.71E-07 2.71E-07 2.71E-07
Cadmium 7440-43-9 2.48E-05 2.48E-05 2.48E-05 C Chromium Compounds 3.16E-05 3.16E-05 3.16E-05
Cob alt 7440-48-4 1.89E-06 1.89E-06 1.89E-06
Manganese Compounds 8.57E-06 8.57E-06 8.57E-06
Mercury 7439-97-6 5.86E-06 5.B6E-06 5.86E-06
Nickel 7440-02-0 4.73E-05 4.73E-05 4.73E-05
Selenium 7782-49-2 5.41E-07 5.41E-07 5.41E-07
TOXIC AIR POLLUTANTIEMISSIONS INFORMATION -FACILITY-WIDE
INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS/ LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE (TPER) IN 15A
NCAC 20 .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY.
Modeling Required ? Note
TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No
Arsenic Compounds 1.03E-06 2.47E-05 0.009 X 1
Beryllium 7440-41-7 6.18E-08 1.48E-06 5.41E-04 X 1
Cadmium 7440-43-9 5.66E-06 1.36E-04 0.050 X 1
Chromium Compounds 7.21E-06 1.73E-04 0.063 X 1
Manganese Compounds 1.96E-06 4.69E-05 0.017 X 1
Mercury 7439-97-6 1.34E-06 3.21E-05 0.012 X 1
Nickel 7440-02-0 1.0BE-05 2.59E-04 0.095 X 1
C COMMENTS:
Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A
NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these sources is less than 450 MMBtulhr, and they will be the only source
of benzene at the facility.
Page F-203
Attachment F. Air Quality Permit Application Review Documents
FORM D2
AIR POLLUTANT NETTING WORKSHEET
.vised:12/01/01 NCDENR/Division of Air Quality -Applic ation for Air Permit to Construct/Operate I D2
luRPOSE OF NETTING: X AIR TOXICS PSD (100/250 tons per year) PSD SIGNIFICANT LEVELS
AIR POLLUTANT: All (See Form D1) CAS NO.:
EMISSION SOURCE ID NOS.: Facility-Wide
SECTION A -EMISSION OFFSETTING ANALYSIS FOR MODIFIED/NE W SOURCES
Summarize in this section EMISSIONS -USE APPROPRIATE COLUMNS ONLY
using the B forms LB/YEAR LB/DAY LB/HR
MODIFICATION See comments below
INCREASE
-MINUS--MINUS--MINUS--MINUS-
MODIFICATION
DECREASE
=EQUALS= =EQUALS= = EQUALS= = EQUALS=
NET CHANGE
FROM MODIFICATION
SECTION B-FACILITY-WIDE EMISSION NETTING ANALYSIS
CREDITABLE See comments below
INCREASE
-MINUS--MINUS--MINUS--MINUS-
CREDITABLE (; DECREASE
= EQUALS= =EQUALS= =EQUALS= =EQUALS=
NET CREDITABLE
CHANGE
SECTION C -FACILITY-WIDE EMISSIONS
TOTAL FACILITY See comments below
EMISSIONS
TPER LEVELS (20 .0711)
CHECK HERE IF AN AIR DISPERSION MODELING ANALYSIS IS REQUIRED
COMMENTS:
The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics
permitting requirements per 15A NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these
sources is less than 450 MM Btu/hr, and they will be the only source of benzene at the facility.
Page F-204
Attachment F. Air Quality Permit Application Review Documents
FORM D4
EXEMPT AND INSIGNIFICANT ACTIVITIES SUMMARY
�ISEO: 12/01/01 NCDENR/Divlslon of Air Quality -Application for Air Permit to Construct/Operate I 04 ..,, ACTIVITIES EXEMPTED PER 2Q .0102 OR
INSIGNIFICANT ACTIVITIES PER 2Q .0503 FOR TITLE V SOURCES
SIZE OR BASIS FOR EXEMPTION OR INSIGNIFICANT
DESCRIPTION OF EMISSION SOURCE PRODUCTION RA TE ACTIVITY
1. Natural Gas Boiler (used for building heat)5.25 MMBtu/hr Per 15A NCAC .:u.0102(h)(1)(B), fuel combustion equipment
(excluding internal combustion engines) firing exclusively
natural gas or liquefied petroleum gas or a mixture of these
fuels.
2. TK-1, Pipeline Liquids Storage Tank, will receive and store pipeline 1,000 gallons Per 15A NCAC 02Q.0102(g)(14)(B), sources for which there
liquids captured by the station's separators and filter-separator. are no applicable requirements.
3. TK-2, Hydrocarbon Waste Tank, will receive and store used oil 2,500 gallons Per 15A NCAC 02Q.0102(g)(4), storage tanks with no
used in oil-filled operational equipment throughout the facility. applicable requirements other than Stage I controls pursuant
to 15A NCAC 020.0928, Gasoline Service Stations Stage I.
4. TK-3, Aqueous Ammonia Storage Tank, will be used to supply 13,400 gallons Per 15A NCAC 02Q.0102(g)(4), storage tanks with no
aqueous ammonia to the SCRs. applicable requirements other than Stage I controls pursuant
to 15A NCAC 020.0928, Gasoline Service Stations Stage I.
TK-4, Odorant Storage Tank 6,000 gallons Per 15A NCAC 02Q.0102(g)(14)(B), sources for which there
are no applicable requirements.
6.
7.
8,
9.
10.
�
Page F-205
Attachment F. Air Quality Permit Application Review Documents
FORM D
TECHNICAL ANALYSIS TO SUPPORT PERMIT APPLICATION
REVISED: 12/01/01 NCDENR/Dlvlslon of Air Quality -Appllcatlon for Air Permit to Construct/Operate
PROVIDE DETAILED TECHNICAL CALCULATIONS TO SUPPORT ALL EMISSION, CONTROL, AND REGULATORY
DEMONSTRATIONS MADE IN THIS APPLICATION. INCLUDE A COMPREHENSIVE PROCESS FLOW DIAGRAM AS
NECESSARY TO SUPPORT AND CLARIFY CALCULATIONS AND ASSUMPTIONS. ADDRESS THE
FOLLOWING SPECIFIC ISSUES ON SEPARATE PAGES:
D5
A SPECIFIC EMISSIONS SOURCE (EMISSION INFORMATION) (FORM B) -SHOW CALCULATIONS USED, INCLUDING EMISSION FACTORS, MATERIAL BALANCES,
AND/OR OTHER METHODS FROM WHICH THE POLLUTANT EMISSION RATES IN THIS APPLICATION WERE DERIVED. INCLUDE CALCULATION OF POTENTIAL
BEFORE AND, WHERE APPLICABLE, AFTER CONTROLS. CLEARLY STATE ANY ASSUMPTIONS MADE AND PROVIDE ANY REFERENCES AS NEEDED TO
SUPPORT MATERIAL BALANCE CALCULATIONS.
B SPECIFIC EMISSION SOURCE (REGULATORY INFORMATION)(FORM E2 • TITLE V ONLY)· PROVIDE AN ANALYSIS OF ANY REGULATIONS APPLICABLE TO
INDIVIDUAL SOURCES AND THE FACILITY AS A WHOLE. INCLUDE A DISCUSSION OUTING METHODS (e.g. FOR TESTING AND/OR MONITORING
REQUIREMENTS) FOR COMPLYING WITH APPLICABLE REGULATIONS, PARTICULARLY THOSE REGULATIONS LIMITING EMISSIONS BASED ON PROCESS
RATES OR OTHER OPERATIONAL PARAMETERS. PROVIDE JUSTIFICATION FOR AVOIDANCE OF ANY FEDERAL REGULATIONS (PREVENTION OF
SIGNIFICANT DETERIORATION (PSD), NEW SOURCE PERFORMANCE STANDARDS (NSPS), NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR
POLLUTANTS (NESHAPS), TITLE V), INCLUDING EXEMPTIONS FROM THE FEDERAL REGULATIONS WHICH WOULD OTHERWISE BE APPLICABLE TO THIS
FACILITY. SUBMIT ANY REQUIRED TO DOCUMENT COMPLIANCE WITH ANY REGULATIONS. INCLUDE EMISSION RATES CALCULATED IN ITEM "A" ABOVE,
DATES OF MANUFACTURE, CONTROL EQUIPMENT, ETC. TO SUPPORT THESE CALCULATIONS.
C CONTROL DEVICE ANALYSIS (FORM C) -PROVIDE A TECHNICAL EVALUATION WITH SUPPORTING REFERENCES FOR ANY CONTROL EFFICIENCIES LISTED
ON SECTION C FORMS, OR USED TO REDUCE EMISSION RATES IN CALCULATIONS UNDER ITEM "A" ABOVE. INCLUDE PERTINENT OPERATING
PARAMETERS (e.g. OPERATING CONDITIONS, MANUFACTURING RECOMMENDATIONS, AND PARAMETERS AS APPLIED FOR IN THIS APPLICATION) CRITICAL
TO ENSURING PROPER PERFORMANCE OF THE CONTROL DEVICES). INCLUDE AND LIMITATIONS OR MALFUNCTION POTENTIAL FOR THE PARTICULAR
CONTROL DEVICES AS EMPLOYED AT THIS FACILITY. DETAIL PROCEDURES FOR ASSURING PROPER OPERATION OF THE CONTROL DEVICE INCLUDING
MONITORING SYSTEMS AND MAINTENANCE TO BE PERFORMED.
D PROCESS AND OPERATIONAL COMPLIANCE ANALYSIS· (FORM E3 • TITLE V ONLY) -SHOWING HOW COMPLIANCE WILL BE ACHIEVED WHEN USING
PROCESS, OPERATIONAL, OR OTHER DATA TO DEMONSTRATE COMPLIANCE. REFER TO COMPLIANCE REQUIREMENTS IN THE REGULATORY ANALYSIS IN
ITEM "B" WHERE APPROPRIATE. LIST ANY CONDITIONS OR PARAMETERS THAT CAN BE MONITORED AND REPORTED TO DEMONSTRATE COMPLIANCE
WITH THE APPLICABLE REGULATIONS.
PROFESSIONAL ENGINEERING SEAL -PURSUANT TO 15A NCAC 2Q .0112 • APPLICATION REQUIRING A PROFESSIONAL ENGINEERING SEAL,"
A PROFESSIONAL ENGINEER REGISTERED IN NORTH CAROLINA SHALL BE REQUIRED TO SEAL TECHNICAL PORTIONS OF THIS APPLICATION FOR
NEW SOURCES AND MODIFICATIONS OF EXISTING SOURCES. (SEE INSTRUCTIONS FOR FURTHER APPLICABILITY).
I,-----------------� attest that this application for _________________ _
1----------------has been reviewed by me and is accurate, complete and consistent with the information supplied
in the engineering plans, calculations, and all other supporting documentation to the best of my knowledge. I further attest that to the best of my
knowledge the proposed design has been prepared in accordance with the applicable regulations. Although certain portions of this submittal
package may have been developed by other professionals, inclusion of these materials under my seal signifies that I have reviewed this material
and have judged it to be consistent with the proposed design. Note: In accordance with NC General Statutes 143-215. 6A and 143-215. 6B, any
person who knowingly makes any false statement, representation, or certification in any application shall be guilty of a Class 2 misdemeanor which
may include a fine not to exceed $10,000 as wall as civil penalties up to $25,000 per violation.
(PLEASE USE BLUE INK TO COMPLETE THE FOLLOWING)
NAME: Jeffrey H. Twaddle, P.E.
DATE:
COMPANY: ERM Southeas( Inc.
ADDRESS: 5000 Meridian Blvd., Ste. 300, Franklin, TN 37067
TELEPHONE: [phone]
SIGNATURE:
PAGES CERTIFIED: ----=-_...;_...;...;..;......;__...;.....;_......;......;_..;_.....;_..;..;.....;;..;;.:...
CT-02-SCR & CT-02-OC, and
CT-03-SCR & CT-03-OC
Attachment C -Potential to Emit Calculations
(IDENTIFY ABOVE EACH PERMIT FORM AND ATTACHMENT
THAT IS BEING CERTIFIED BY THIS SEAL)
PLACE NORTH CAROLINA SEAL HERE
Page F-206
Attachment F. Air Quality Permit Application Review Documents
AITACHMENTB
FACILITY PLOT PLAN
•
ERM DOMINION -ACP-3 ST A TION
Page F-207
Attachment F. Air Quality Permit Application Review Documents
"z .. ;1
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Page F-208
Attachment F. Air Quality Permit Application Review Documents
AITACHMENT C
POTENTIAL TO EMITCALCULATIONS
ERM DOMINION -ACP-3SfATION
Page F-209
Attachment F. Air Quality Permit Application Review Documents
Table C-1 Permit to Construct Application Pro;ect Equipment List
ACP Compressor Station 3 -Northampton County, North Carolina
Emission Source Manufacturer Model/Type Point ID
CT-01 Compressor Turbine Solar Turbines Taurus 70-10802S
CT-02 Compressor Turbine Solar Turbines Centaur 50-6200LS
CT-03 Compressor Turbine Solar Turbines Centaur 40-4700S
EG-01 Emen::iency Generator Caterpillar G3516B
EG-02 Emen::iencv Generator Generac SG100
WH-01 Boiler Hurst LPW-G-125-60W
FUG-01 Fuqitive Leaks -Slowdowns --
FUG-02 Fuoitive Leaks -Pioinq --
TK-1 Pipeline Liquids Tank --
TK-2 Hydrocarbon (Waste Oil) Tank ----
TK-3 Ammonia Tank ----
Rated
Caoacitv
10,915 hp
6,200 hp
4,700 ho
1,818hp
148.9 hp
5.25 MMBtu/hr --
1,000 oal
2,500 qal
13,400 qal
Page F-210
Attachment F. Air Quality Permit Application Review Documents
•
Tablt! C-2 Potl!11tial E111issio1,s Fro111 Co111bustio11 Sourcl!s
ACP Co111prt!ssor Statio11 3 -Nortlta111pto11 Co1111ty, Nortlt Caroli11a
TurbinP Oner•tionill Parameters· Emergrnry Grner;11tor OpPqtipnil HDUDi
Nonnal Hours or Oooration: 8,677
Hours al Low load7<50%)
Nonnal Hours 01 ue:rauun:
Hours or Low Tcmn. '< 0 l.lC' ,. "' Hours of Slalrl-u" 1Shul-Jown
Total Hours of Qn•ralion (hr/vr):
Pn!-ControJ fplenti;al lo Emit
Combustion Soun:u
Solar Taurus 70 Turbine
Solar Centaur 50L Turbine
Solar Centaur 40 Turbtne
Catemlnar G35168 Eaen
Generac SG 100 Enen
Boiler
0
50
11-1
8,760
Power D ........
10 ,915
6.200
4.700
1.81B
14B 9
5.25
Total (ton/II rj
Turbine Control EffiriPncirs
Control Trchno---· NOx
SelL'Cltvc Cata)uttc Reduction fCcnlaur-10\ 80!;
St.•lt>eltvc Catalut1c Rl'\lu«. tmn fAII OUtt•rs\ -1-1,;
Ox1d.illon CataJu,;t 'Centaur-IQ\
Ox1datton CaLa)ust 'All O\ht�r.;\
Posl-Con(rol Potential 19 Emit -
Combusllon Soun:H Datlnn
Solar Taurus 70 Turt>ine 10915
Solar Cenlaur SOL Turbine 6200
Solar Centaur 40 Turbine 4700
Caterolllar G3516B Eaen 1818
Generac SG 100 Eaen 148.9
Boller 5.25
Total /ton/I/ m
Notes:
Unlls Fuel NOx co
ho Natural Gas U9 23 8
ho Natural Gas 9 25 14 8
hn Nalun,I Ga, 22.0 25 6
ho Natural Ga, 0100 0-499
ho Natural Ga, 4,92E-05 9.85E-04
MMBtu/hr Natural Ga1 1.13 1.89
47.3 66.6
co voe
90 % 50% 60% 50%
Units Fuel NOx co
ho Natural Gas 8.25 4 76
ho Natural Gas 5 14 2.96
ho Natural Gas 4 39 2.56
ho Natural Gas 0,100 0499
ho Natural Gas 4 92E-05 9.85E-04
MMBlu/hr Natural Gas 1 13 189
19.0 12.7
(1) Turbine emissions are cak:ulated by the following formula: ER• Run Hours / 2000 • (1 -Control Efficiency)O
ER = Emlssk>n Rate for particular equipment and poUutant (lbs/hr)
2000 = the amount of lbs In a ton
voe
1-36
0834
0702
010B
0 003
0.124
3.13
voe
0660
0.417
0 351
0108
0.003
0124
1.68
(2) Emergency Generator emissions are calculated by the following formula: Power Rating • Run Hours • EF / 2000.D
Power Rating • Engine hp rating (hp)
EF = Emission Factor from either manufacturer's data or AP-42 (lblhp-hr}
2000 = the amount of lbs in a ton
(3) Boller/Heater emissions calculated by the following formula: EF • Power Rating • Run Hours / t+fV / 2000
EF = AP-42 Emission Factor (lb/MMSCF}
Power Rallng = Boller/Healer Heal Capacity (MMBlu/hr)
HHV • Nalural Gas High HeaUng Value (1020 MMBtu/MMSCFJ
100
902
U3
0 894
0 760
3,BBE-04
3, 18E-05
0014
3.10
902
143
0.894
0.760
3 BBE-04
3.1BE-05
0.014
3.10
•
Crllerlo Polhrtanlll IIPYI
Talat PM Total PM10 TolalPM2.li
8.41 8.41 8-41
5.26 5.26 5.26
4 47 4.47 4.47
0.032 0.032 0.032
0003 0.003 0.003
0.171 0171 0.171
18.3 18.3 18.3
Crllerlo P_nta ,-,
Talat PM TolalPM10 Talat PM2.5
8.41 8,41 B 41
5.26 5.26 5.26
447 4 47 447
0032 0 032 0.032
0.003 0003 0.003
0.171 0.171 0.171
18.3 18.3 18.3
(4) Turbines are equipped wHh 5electlve Catalytic Reducllon (SCR) and o>ddallon calalysl for control of NOx (44%), co (60%), and voe (50%)
(5) Taurus Centaur 40 oxidation catalyst has a control of 90 % for CO
(6) Emergency generator engine hp taken from manufacturer data
(7) Boller assumed to have low-NOx burners
(8) see the "HAP Emissions" worksheet for a more detailed breakdown of HPP emissions
(9) Sea Emissions Factors table for Emissions Factors for each operating scenario.
(10) Each start-up/shut-down event assumed to last 10 minutes
Boiler/HH(rr Opeqfipn;al P.tnmeters:
Nnrm,11 Hours ofOpt_ration: j 8.760
GHO EmiHlons '"' Ammonlo ,mv, HAPn=•
PMF PMF-10 PMF-2.5 PMC CO2 CH4 N20 COZe ..... '""""""
2.42 2.42 2.42 5.99 49.980 362 1.26 50 ,446 5 77 0 525
1.51 151 151 374 31.295 2.26 0 788 31587 358 0352
1.29 1.29 1,29 3.18 26.71B 1 92 0 671 26,966 3 02 0286
0025 0025 0.025 0007 10 1 0 B59 0 122 0 0018
0002 0002 0.002 0001 759 0 015 0 759 0 0 002
0 043 0043 0.043 0129 2.705 0 052 0050 2,721 0 0 043
5.29 ,.,. �.29 13.1 111,559 8.72 2.77 112,602 12.4 1.23
GHG Emlulona •-Ammonla l'HIVI HAPtt-
PMF PMF-10 PMF-2.li PMC CO2 CH4 N20 C02a �· -··-
2.42 2.42 2.42 599 49,980 362 1.26 50.446 577 0 525
1.51 1.51 151 3 74 31,295 2.26 0 788 31,587 3.58 0 352
1,29 1.29 1.29 3.18 26,71B 1 92 0.671 26.966 3 02 0286
0.025 0.025 0 025 0.007 10 1 0 859 0 122 0 0018
0.002 0.002 0 002 0001 759 0 015 0 759 0 0002
0 043 0 043 0 043 0,129 2,705 0 052 0 050 2,721 0 0 043
5.29 5.29 5.29 13.1 111,559 8.72 2.11 112,602 12.4 .23
Page F-211
Attachment F. Air Quality Permit Application Review Documents
•
Ta#Jl,; C-3 Evt11t Based Potr11tinl Emissio11s From Co,ulmstion Sor,rces ACP Compressor Station 3 -Nortl,ampton Cou11ty, NortJ, Caroli11a
Start-UP Emlllk>n iPW!1fR cnpJIMJI
Combusllon Sources ,� Unlb I .... Saa Tairus 70 Turbne 10915 hn NftlfalO. Sow Cemaur 50L Turbine 6200 h• Na1Ura1Ga Solar CentaJr 40 Turt>ine 4700 ho NaturalGa
Ota/
SbuMkMD EmlnkJn :iWYNYYID CPIIIMJI
r...-••tlon Sou,ca I�= Unlb I .... Sos Ta.wua o Turbne 10915 ho N....,Gaa Soar CMtaw 50L Turbc'le 8200 ho NnlralG• Solar Centaur 40 TUfbtne 4700 h• NnnlG• ... ,
Total s0!8 l'misslon• (tOn.,.,,,
,2mm11sz[ Dlowdown l;;1D11lsm1
_Source�ation I -
�
r'alhtl,111.I
TIUI St,..&in MG&«ulu WirlaN N .. �voc C'•rh111.�
Ni, ......... t'Jharr voe ""'�� n-HuLlrr -� n-l'C'Na"" b .. 1 ........ n-Hr.anr n-HrfltillW' Tat.alVOCFr.Ktion Tat.al HAI' Fr.action
Rbmllm!n (mm :i:l•dne la:s:a12
�[]�1
3""00 sd/ .... 1 305 ,d--18 b-l>mol 93% " 1691 lb/ .... ,
W•ighl (Val-� \"t\.f.-<1Wlft --�· I I � fl¥•-II Fnc-Oon (W\. � , ...
,&,&.01 1.0U:I. ,.,,,. 211111 0.994'. 1-U,.tM 9UJ� ....,..,
30.117 '-"'' .-
-'-1.IO ..... , ,.,.,,._,, .,,, ....... 511.11 ..,.,l.ffllo 12.15 """' --,,.,, .., .... .....7A.II '""" ......
Ull.21 ""'" .....,..,,. .. 1 ...
, .......... E--·· 100 0040 100 0040 100 0035 0.115
1-;.;:;;;-NOl 100 0055 100 0020 100 0015 o.-
I 6.206
111:!!m!l�denbll!IJ:
Blowdown lrum Shuldcwon Voklme-.:nawrate Methane Molecular W I MelhanePercentW I Shutdown Blowdawn
I iai I I di+o Ern1U10n1 I CH4 75834 1o» 75834 1 093 75834 1893
227 5179
ll!ie:�D Cm:! ��l!IE?!:n li!"DI"
missions voe cH• cote
3675 ,= 125 39 3130 3675 360 12539 3139 3675 360 12539 3139 11.024 11.41 370 1411
sd/"'ent
..,..,..,
ttMIJp .... Combladan Soun:a E-voe CH4 ACP-3 1 1167 121 ,.. ...Toal 1.111 1.21 "'·' "'
I Total Blowelown Emlnlons (ronM!rJ I UI.II I 19.5 I 043 I 1i10H
.. . co � CO2 �H4 368 0042 2595 0168 302 3.46 0040 23 45 0160 27 45 322 0037 1960 014! 2330 10.33 0.111 811.D 0.471 ....
� .. GHQ£-co CO2 CtM CO2"
487 00'3 200 0212 34 1 1770 0020 1095 ooao 1285 1.510 0017 905 0068 10.75
7.150 ·--41.7 o.-.,.
I 11.21 I o.209 I 111.1 I 0.130 I 13&
83000 KIi-i 305 ,d--16 b-l>mol 93% " 2603 lblewnt
....... 0125
0125 D.125 O.l75
7 HAPI 0.207 0.207
0207 0.122
HAi's 0068 O.DII
I 1.08
Page F-212
Attachment F. Air Quality Permit Application Review Documents
•
Table C-4 Combustion Source Criteria Pollutant Emission Factors
ACP Compressor Station 3 -Northampton Co1111ty, North Carolina
Equipment Name Solar Centaur 40 Turbine Solar Centaur SOL Turbine Solar Taurus 70 Turbine
Notes
Fuel Units Natural Gas I lb/hr Natural Gasl lb/hr Natural Gasllblhr
NOx 4.70 1.98 3.18 1.7808 1.1088 0.94
co 5.70 3.30 5.30 1.06 0,66 0.57
Solar Turbine Normal Operation Emission Factons (lblhr)
voe I so2 I PMF I PMF-10 I PMF-2.5 0.160 I 0.11 I 0.29 I 0,29 I 0.29
o.190 I 0.20 I 035 I 035 I 035
o.310 I o.33 I 055 I 055 I 055 0.155 0.095 0.08
(1) Pre-Control Em1ss1on Rates for NOx, CO, VOC, PMF, PMC, and CO2 taken from Solar Turbine Data al 100 % load and o degrees F
PMC CO2 073 6100 0.85 7145 137 11411
(2) Em1ss1on Factors for S02, CH4, N20 taken from AP-42 1n (lbs/MMBlu) and mulbpl1ed by turbine fuel throughput by Solar Turbine at 100 % load and o degree F to get Emission Rates (3) Assume PMF=PMF-1 D=PMF-2.5, Filterable and Condensable based on Solar Turbine Emission Factor and ratio of AP-42 Table 3.1 factors (4) NH3 emission rates based on a 10 ppm ammonia slip from the SCR based on manufacturer information (5) C02e emission rate calculated by multiplying each GHG (CO2, CH4, N20) by its Global Warming Potential (GWP) and adding them together (6) CO2 GWP = 1; CH4 GWP = 25; N20 GWP = 298 [40 CFR Part 98)
E�•-ntName Solar Centaur 40 Turbine Solar Centaur SOL Turbine Solar Taurus 70 Turbine
Notes
Solar Turbine Alternate Ollerlltlon Emission Factons llblhrl
Fuel Units Natural Gas lb/hr Natural Gas lb/hr Natural Gas lb/hr
<0lltlal'ffaF NOx 62.7 26.4 42.4 23.744 14.784 12.533333
co 34 .2 19.8 31.8 . 6.36 3.96 3.42
voe 0.320 0380 0620 .. 0.31 0.19 0.16
Solar Turbine Low Load F r>nAHHnn NOx co voe36.6 2280 6.40 15 .4 1320 7,60 24.7 2120 12 .4
(1) Pre-Control low temperature Emission Rates for NOx, CO, VOC. Conservatively assume 120 ppm NOx, 150 ppm CO, and 5 ppm VOC (10% of UHC) per Table 2 of Solar PIL 167 (2) Pre-Control low load Emission Rates for NOx, CO, VOC. Conservatively assume 70 ppm NOx, 10,000 ppm CO, and 100 ppm VOC (10% of UHC) per Table 4 of Solar PIL 167
Solar Turbine start-up and Shutdown Emission Factons (lb/event)
CH• 0.44 0,52 083
Start_.., EFs Shutdown EFs E�n-Name Fuel Units NOx co voe CO2 CH4 CO2e NOx co Solar Centaur 40 Turbine Natural Gas lb/event 07 64 4 07 392 30 466 03 30,2 Solar Centaur SOL Turbine Natural Gas lb/event 0.8 69 .1 0.8 469 32 549 04 35.4 Solar Taurus 70 Turbine Natural Gas lb/event 0.8 73.1 0.8 519 34 603 11 93.4
Notes (1) Start-up and Shutdown Em1ss1ons based on Solar Turbines Incorporated Product Information Letter 170: Emission Estimates at Start-up, Shutdown, and Commissioning for SoLoNOx Combustion Products (13 June 2012). Emission Estimates do not include S02, PM, N20, or any HAPs. (2) VOCs assumed to be 20% of UHC and CH4 assumed lo be 80% of UHC. (3) C02e em1ss1on rate calculated by multiplying each GHG (CO2, CH4) by its Global Warming Potential (GWP) and adding them together (4) CO2 GWP = 1; CH4 GWP = 25, [40 CFR Part 98)
Eaulpment Tv"" Fuel Units NOx co Boiler< 100 MMBtu Natural Gas lb/MMscf 50 84 1300 KW Caterpillar Eaen Natural Gas lblhn-hr 0.0011023 0.00549 100 kW Generac Eaen Natural Gas lb/ho-hr 0.000007 0.00013
Noles (1) Em1ss1on factors for natural gas boilers taken from AP-42 Tables 1.4-1 & 1.4-2 (2) Boiler assumed lo have low-NOx burners
voe 5.5 0,00119 0.00037
(3) Emission Factors for Space & Water Heaters taken from AP-42 Tables 1.4-1 & 1.4-2 (4) Emission Factors for 2 SLB engine taken from AP-42 Table 3.2-1
Ennlne and Boller Emission Factons S02 PMF PMF-10 0.6 1.9 1 .9 4.269E-06 0,000278822 0000278822 4.269E-06 0.000278822 0000278822
(5) NOx, CO, VOC, CO2, and CH4 emission factors for Caterpillar Egens taken from Caterpillar Manufacturer data
PMF-2.5 1.9 0000278822 0000278822
(6) NOx, CO, and VOC emission factors for Generac Egans taken from Generac manufacturer statement of exhaust emissions for SCAQMO certification
PMC 57 719565E-05 719565E-05
(7) S02 , PMF, PMF-10, PMF-2.5, PMC, and N20 Emission factors for Caterpillar Egens taken from AP-42 Table 3 2·1 and converted using manufacturer fuel data (8) S02, PMF, PMF-10, PMF-2 .5, PMC, and N20 Emission factors for Generac Egens taken from AP-42 for natural gas combustion (9) Assume PMF=PMF-10=PMF-2.5 (10) C02e em1ss1on rate calculated by multiplying each GHG (CO2, CH4, N20) by its Global Warming Potential (GWP) and adding them together (11) CO2 GWP = 1; CH4 GWP = 25; N20 GWP = 298 [40 CFR 98)
voe CO2 0.3 181 04 217 11 575
CO2 CH4 I 120000 2.3 I 1,111131 0,0094451 101 ,9472 o 001954 I
N20 CO2e NH3 0.15 6157 0690 0.18 7212 0.818029 11517 1.317
CH4 CO2e 1.4 215 16 257 42 681
N20 I CO2e NH3 2 .2 I 120713 0.00 0 I 1 000 o I 102 000
Page F-213
Attachment F. Air Quality Permit Application Review Documents
Table C·5 Hn;nrdo11s Air Poll11tn11t (HAP) Emissio11s From Co111b11stio11 Sources
ACP Compressor Statio11 3 · Nortltn111pto11 Comity, North Carolina
OuanU ACP-3
Pollutant
. .... ....... -..12-0ichlo, .. 1.J.�Trimemvit>enzent
1 3-St.uciene
-�do Acrclem Anthracene IhlOfobenzene
..
CNoroethane
C�Ofm Ch . .,,.. ...
�vr:1�tane acene
, ..
..........
J.� ...
Ohexane Mett1Vlene Chloride
n-Nonane n-Octane ... AH Ir .. , ... I-Barium
lum Cadmium
Chromium
<,;0bell o=
Manaanese
Mercu,v
Molybdenum "cir� Selenium Vanadum
Zinc
Lead ITotal HAPs
Hazardous t,Jr Pollutant
Notes.
HAP?
es Yes Yes No No Yes Yes No Yes Yes Yes
No No No No No
Yes Yes No No Yes No No
No No No Yes No
No Yes
Yes Yes Yes No No
No No Yes No Yes Yes
No
No Yes Yes No
No Yes No Yes No
No Yes Yes
No No
No Yes
No Yes No Yes No Yes Yes Yes Yes
No Yes Yes Yes Yes No Yes Yes No Yes Yes No No Yes ... ..
Pl EmlSSlom above are on a per unit basis
Annual HAP Emissions (lb/yr) 1 1 1 1 -·� Sola,c.ntau, llalarTaunaa BoUet<100
olDTurblne &ol TUJbfne 70Tu�ne MMBtu
,700 ll200 10915 5.25
h• ho h• MMBl\1/hr
1125 1100 7201
Iv
0.001 0.uw 0.001 0.uoo
0.000
0.000 0.000
0.u,r:,
0.000
0.000
0.000 0.000
94.885
0.000
0.05' 139.n4
0.000
541.000 M4.n51 992.m 3.382 81.1�
0.000
0.028
117.229
0.001
a.141
0.000
D.153
0.000
0.198 0.001
0.050
0.063·
0.004
0.038
0.017
0.012
0.050 0.005 0.001
0.104
1.308
0.023 572934 704.0151 1050.586
573 704 1051 85.1
u., .. ..... o.�s 0.043
1 1
1300KW 10011W CotefJll'lar Generacl!gen -
1111 1411.1
h• ho .. , ·""'0.002 18 u.w1 0 18 0.001 .051 0.004 n� 0.002 .021 0. 0.006 u 1 •.• ,9 0.0 1 0.020 0. 0,391 0.0 0.010 0. 1
,nn1 o.
. 001 0 . . 5� 0 o. .= 0.
0. .e., 0. .ODO n
0.000 0.000 o.uuu 0.000 0.000
0.000 0.000 2197 0.180
O.N, 0.017 0.028 0.007
0.U21 0.002
O.CJ'.118 n=
0.000 0.14� u.u12
0.044 0.004
32. 98 2.eee 0.UU4 .0 n=
0.000
0. 1 0.000
2'. 14 2.001
0.017 o., ..
1. 0.142 1.147 0.094
0,156 0.013 0.00II 0.0011 u. 14 0.UU1 0.034 nnn3
0.045 0.004 o . .....,
0.708 0.058
0.000 o.w, u.000 0,0151 0.002 1J.Zf8 1.087
0.000 0.000
0.025 0.002
0,445 0.038
0.011 0.001 u.124 0.0111
lU 3.0Z
u.u1a O.w,
(2) calculations for the cat«pil!lar emergency generatm assume 100 houri of operation, all other cak:l.tlalions assume e,7e0 hou� of opera1ion (3) Heat ra� fOf Solar Turbines ta)(en from Solar Oatnheet1
(4) Solar turl:ines have a 50% KAP control l!!ffioency due lo the Olddation Catal)'l,t
Page F-214
Attachment F. Air Quality Permit Application Review Documents
Table C-6 Comb11stio11 Source HAP Emission Factors
ACP Compressor Stntiou 3 -Nort/111111pto11 Co1111t_v, Nort/1 Cnroli1111
Eml11k>n Factor•
PoMutant
11 2 2-Tetrachlofoethane
1 1 2-Trlehloroethane
11-O ichloroethane
1 2 J.Trlmethvtbenzene
124-Trlmethvtbenzene
1 2-Oichloroethane
12-Oichloro no
1 3 5-Trimethvtbenzene
1 J.Butadiene
1 3-D�hlor ne
2 2 4-TrWl"lethvtoentane
2-Metn-.1naonthalene
J.MethvlchloranUvene
7 12-0fflethvlbenzla anthracene
AcenaDhthene
AcenaDhthvlene
Aeetaldehvde
Acroleln
Anthracene
Benzfalanthracene
Benzene
Benzolalovrene
Benzolblfluoranthene
Butane
Butvr/lsobuMaldehvde
Carbon Tetrachloride
Chk>robenzene
Chk>roethane
Chk>rofo,m c�ne
Cvclohexane
Cvclooentane
Oibenzola h'8nthracene
Hexane (or n-Hexanel
lndenol1 2 3-c dlcvrene
lsobutane
Methanol
Meth111MW"lohexane
Methvlene Chloride
n-Nonane
n-Octane
Naohthah!:ne
PAH
Pentane (or n-Pentane)
PeMene
Phenanthrene
Phenol
Prooane
ProDYleneOxicfe
Pvrene
Stvrene
Tetrachloroethane
Toluene
Wivl Chloride+A32
Xvlene
Arsenic
� Chromium
Cobalt c�,
Manaanese
Mercurv
Molvbdenum
Nd<el
Selenium
Vanadium Znc
Lead
Total HAPs
Hazardous Air Potlutant
Notes
Solar Centaur Solar Centaur Solar Taurua HAP? 40Turblne SOL Turbine 70Turblne
lb/MMBIII lb/MMBIU lb/MMBtu
Yes
Yes
Yes
No
No
Yes
Yes
No
Yes
Yes
y ..
No
No
No
No
No
Yes
Yes
No
No
Yes
No
No
No
No
No
Yes
No
No
Yes
Yes
Yes
Yes
No
No
No
No
Yes
No
Yes
Yes
No
No
Yes 29E-03 2 9E-03 2 9E-03
Yes
No
No
Yes
No
Yes
No
No
Yes
Yes
No
No
No
Yes
No
Yes
No
Yes
No
Yes
Yes
y .. Yes
No
Yes
Yes
Yes
Yes
No
Yes
Yes
No
Yes
Yes
No
No
Yes
3.1E-03 3.1E-03 3.1E-03
(1) Emission factors for Solar and Capstone natural gas1urbl"les from AP-42 Table 3 1·3
(2) Emission factors for natural gas boilers from AP-42 Tables 1 4-2, 1 4-3, and 1.4-4
Boller< 100
MMBtu
lb/MMscf
2.4E-05
1.BE-06
1.6E-05
1.8E-06
1.8E-06
2.<E-06
1.BE-06
2.1E-03
1.2E-06
1.8E-06
1.2E-06
1.BE-06
2 1E+OO
1 8E-06
1 2E-06
1 2E-03
3 1E+OO
3.0E-06
2 8E-06
7 SE-02
1 BE+OO
1 8E-06
6 1E-04
26E+OO
17E-05
1.6E+OO
5.0E-06
3.4E-03
2.0E-04
4.4E-03
1.2E-05
1.1E-03
1.4E-03
8.4E-05
8.SE-04
3.8E-04
2.6E-04
1.1E-03
2.1E-03
2.4E-05
2.3E-03
2.9E-02
5.0E-04
1:IOOKW 100kW
CaterpUtar Ganerac
Egon Egon
1-... hr 11,11, ... 1,.
1.7E-07 1.7E-07
1.3E-07 1.3E-07
9.9E-08 9.9E-08
9.0E-08 9.0E-08
2.8E-07 2.BE-07
1.1E-07 1.1E-07
1.1E-07 1.1E-07
<.6E-08 <.6E-08
2.1E-06 2.1E-06
1.1E-07 1.1E-07
2.2E-06 2.2E-06
5.4E-08 5.4E-08
3.4E-09 3.4E-09
8.1E-09 8.1E-09
2.0E-05 2.0E-05
2.0E-05 2.0E-05
1.BE-09 1.BE-09
8.SE-10 8.SE-10
4.9E-06 4.9E-06
1.<E-11 1.4E-11
2.2E-11 2.2E-11
6.0E-11 6.0E-11
6.3E-11 6.3E-11
1.1E-11 1.1E-11
1.0E-08 1.0E-08
1.2E-05 1.2E-05
1.1E-06 1.1E-06
1.SE-07 1.SE-07
1.1E-07 1.1E-07
1.2E-07 1.2E-07
1.7E-09 1.7E-09
7.BE-07 7.BE-07
2.4E-07 2.4E-07
1.BE-04 1.BE-04
2.7E-07 2.7E-07
1.9E-07 1.9E-07
9.2E-10 9.2E-10
<.3E-09 4.3E-09
1.4E-04 1.4E-04
1.1E-06 1.1E-06
2.SE-11 2.SE-11
9.SE-06 9.SE-06
6.3E-06 6.3E-06
8 6E-07 8.6E-07
3.7E-07 3.7E-07
7.SE-08 7.BE-08
1.9E-07 1.9E-07
2.SE-07 2.SE-07
3 <E-07 JAE-07
3 9E-06 3.9E-06
1 JE-11 13E-11
9 OE-09 9.0E-09
1.1E-07 11E-07
7.3E-05 7 JE-05
1.SE-09 1 SE-09
1.4E-07 1 4E-07
2.SE-06 2.SE-06
6 JE-08 6 3E-08
6.BE-07 6 BE-07
(3) EmisSion factors for 2 SLB natural gas engnes and Caterpillar and Generac nalural gas emergency generators taken from AP-42 Table 3 2-1
(4) Emission factors for Solar natural gas turbines and Caterpilar and Generac natural gas emergencygeneralors canverted using 1 KWh= 3412 Btu and 1 kw= 1 341 hp
(5) EmisSIOn Factors (lblMMStu ) for Formaldehyde and Total HAPs for Solar Turbines from Solar PH.. 168
Page F-215
Attachment F. Air Quality Permit Application Review Documents
Table C-7 Pote11tial E111issio11s From Fugitive Leaks
ACP Compressor Statio11 3 -Nortl,a111pto11 Comity, North Caro/i11n
Fugilive Emissions (FUG)
Source �in_nalmn.
Pemlion,!I P·uamds:rF
Annual Hours of Operation (hr/ yr}:
CompreHor Fughl•e EmlH\onP R••e
Equl.pmenl
Solar Turbine
11,7<;0
Scrvke
Go,
FUC-<12
CH4 EmlNlon F<iclo�ll
Ion/comp-hr
267E-02
1. 0.•foult met.h.ine basis and efflmion (octor taken fmmT1:1l>k>6-6ofCompc.'11tliumofGn."-'I\OOU11CC.. EmliaioM Ml'lhoJolor,it.'5£or lhcOil and C... Industry, Al'I. Auguat 2Cm
2. SampleculrulaUons:Hoursolof"l'"llkwl(hr/yr} • EF (ton/ mmpn!19.lt•hrJ/ Mdhancfractk,n
Plrc:Uot Nahlr.11 CH Far:ltlve EmlHI 1 :ii:111:1 ::i1:1z 1 �1,11,1 :Ii 1,111111:1nma
E� -·Em!Nlet,f,c,_llt s.-.c ...... T ... IHCl'oOutWl!miMloao VOCW<lcbt •--· ,� .... --
Valves Go, -I.SOE-OJ ""' 2.91 12.7 OJl26
PumpSl.-ols Go, 2.-IOE-03 0.00 0.00 OJJ26
Others (compn.':!wrs unJ others} Go, 8.t!OE-03 3 0.0.1 0.12 OJl26
Cnnm..:tors Go, 2.00E-OI I 2.00E-OI 8.76&0-I OJl26
Flanj�L'5 Go, 3 90E-OI J40 0.133 0.581 OJl26
Orcn-t.-mk..J lines Go, 2.00E-03 0.00 0.00 D.026
T ... I 3 13
1. El'A Prolorol.for Equipmcnl U.ub EmiJaions &I.HNltc IEPA-1Sl/R·9S-Ot7) Tllhk-2-1:0iland � Plftlurtion Op-ntl.11.>nS Em-in Frr.1urs.
2. Cumronmt rount based on &sio:Sysll·rm Eng1n1.ffing E,,;t�c.
,;-mi: Calgdii1n,,;
Polmtial �(lb/hr)• Emt91iun Flldor (ll/hr/suun.�) • Suun-cCounl
Polt.1\lial Em&ians (Ions/yr)• Uh/ht)......,• HouniofOpcrahun (hr/yr)• (I lon/2.LDJ lb).
voe-CO,w.tpl CO,l!miMloao .... mclloo ...
03:>I 0.0271 O.:HS
0.00 IJ.0271 0.00
0.00 0.0271 0.00
2.JOE-05 0.0271 2.38&"5
O.OIS D.0271 0.016
noo 0.0271 0.00
o., o,
CH.Weight
Fr.icllon111
Cl,91,4
CH,Wolgbt --
OJl95
OJl95
0.895
OJl95
OJl95
OJl95
c142m1a1o.
IPY
11..J
0.00
0.10
7.8-IE-OI
0.5211
0.00
12.ms
HAPWdgl,I HAPEmlulou """""" -
1.-IBE-03 1.88E-02
1,48E-03 O.OOE-+00
Ull&Ol 1.71E-0.1
1.48E-03 1.30£06
1.48E-03 tl.59£..CW
1.48E-Ol O.OOE+OO
0.02
Page F-216
Attachment F. Air Quality Permit Application Review Documents
Table C-8 Tank Emissions
ACP Compressor Station 3 -Northampton County, North Carolina
I Source Designation:TK-1, TK-2, TK-3
Tank Parameters
Source Type of Tank Contents Capacity Throughput Tank Diam. Tank Length Paint Color Paint
(gal) gal/yr ft ft Condition
TK-1 Horizontal, fixed Produced Fluids 1,000 5,000 4.12 10 Light Grey Good
TK-2 Horizontal, fixed Lube Oil 2,500 12,500 4.61 20 Light Grey Good
Total Emissions
VOC Emissions
Source Flashing Losses Working Losses Breathing Losses Total Losses
lb/hr tpy lb/hr tpy lb/hr tpy lb/hr tpy
TK-1111 ------0.033 0.145
TK-2121 NA NA 1.29E-06 5.65E-06 3.72E-06 1.63E-05 5.0lE-06 2.19E-05
1. Losses were calculated for TK-1 using E&P Tanks Software. See attached for output.
2. Losses were calculated for TK-2 using EPA's T ANI<S 4.09d software with default breather vent settings.
3. Losses (Emissions) from TK-3 13,400-gallon Ammonia tank assumed to be insignficant.
Page F-217
Attachment F. Air Quality Permit Application Review Documents
•
Table C-9 Proiect Pote11tial Emissio11s
ACP Compressor Statio11 3 -Nortl1ampto11 Co,mhJ, North Caroli11a
Criteria Pollutants ,m 1 GHG Emissions nD 1 Ammonia 1mv1 HAP ,tnu,
Combustion Sources ID NOx co voe SO2 PMF PMF-10 PMF-2.& PMC CO2 CH4 N20 CO2e NM.> IOUIIHAP
Solar Taurus 70 Turbine CT-01 8.35 13.1 0.775 1.43 2.42 2.42 2.42 5.99 50,035 4.00 1.26 50,511 5.77 0.525
Solar Centaur &OL Turbine CT-02 5.20 8.19 0.477 0.894 1.51 1.51 1.51 3.74 31,329 2.50 0.788 31,627 3.58 0.352
Solar Centaur 40 Turbine CT-03 4.44 7.29 0.405 0.760 1.29 1.29 1.29 3.18 26,747 2.14 0.671 27,000 3.02 0.286
Caterolllar G3516B Egen EG-01 0.100 0.499 0.108 3.88E-04 0.025 0.025 0.025 0.007 101 0.859 0 122 0 0.018
Generac SG100 Eaen EG-02 4.92E-05 0.001 0.003 3.18E-05 0.002 0.002 0.002 0.001 759 0.015 0 759 0 0.002
Boller WH-01 1.13 1.89 0.124 0.014 0.043 0.043 0.043 0.129 2,705 0.052 0.050 2,721 o 0.043
Fualtlve Leaks -Slowdowns FUG-01 . -18.8 .. -. . 19.5 643 16,092 -1.06
Fugitive Leaks -Plolm1 FUG-02 . -0.352 . -. -. 0.4 12 -301 . 0.02
Ploellne Liaulds Tank TK-1 --0.145 -. . . -. . ---.
Hydrocarbon (Waste 0111 Tank TK-2 --2.19E-05 -. -. -. . . ---
Tota/ rton,uvrJ 19.2 31.0 21.2 3.10 6.29 6.29 6.29 13.1 111 696 664 2.77 129,133 12.4 2.31
Page F-218
Attachment F. Air Quality Permit Application Review Documents
•
•
Tank 1 Emissions.txt
************************************************************************************ ****** *Project Setup Information* ************************************************************************************ ******
Project File : M:\0345197 DRS ATL Coast Pipe.PR\T501 Air Permit\ACP & SHP-Permitting\Air Permitting Round 2\Round 5\ACP-1 -Marts\Aug 2016 -EG and Tank Replacements\TK-1 -05152017 update to Throughput.ept Flowsheet selection : oil Tank with separator calculation Method : AP42 Control Efficiency 100.0% Known separator Stream Low Pressure Gas Entering Air composition No
Date 2017.06.05
************************************************************************************ ****** *Data Input************************************************************************************* ******
separator Pressure separator Temperature Molar GOR Ambient Pressure Ambient Temperature ClO+ SG ClO+ MW
--Low Pressure Gas
No. component 1 H2S 2 02 3 CO2 4 N2 5 Cl 6 C2 7 C3 8 i-C49 n-C410 i-c511 n-c512 C613 c?+14 Benzene15 Toluene16 E-Benzene17 Xylenes18 n-C619 224Trimethylp
C7+ Molar Ratio: C7 :1.0000
--sales Oil
Production Rate
552.00[psig] 77 .00 [FJ 0.0500 14. 70[psia]70.00[F]0.8990166.00
mol % 0.0000 0.0000 o.51120.529594.0604 4.7199 0.1590 0.0099 0.0099 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
CB : 1.0000
0.3[bbl/day]
C9 1.0000
Page 1
ClO+ 1.0000
Page F-219
Attachment F. Air Quality Permit Application Review Documents
•
Days of Annual Operation API Gravity Reid Vapor Pressure Bulk Temperature
--Tank and shell Data
Diameter shell Height cone Roof slope Average Liquid Height vent Pressure Range solar Absorbance
--Meteorological Data
Tank 1 Emissions.txt 365 [days/year] 46.0 7.70[psia] 80. 00 [F]
4.12 [ft] 10.00[ft] 0.06 5.00[ft] 0.06[psi] 0. 54
Page 1----------------------------------------------------------------E&P TANK
City Ambient Pressure Ambient Temperature
Charleston, WV 14. 70[psi a]70. OO[F]44.00[F]Min Ambient Temperature Max Ambient Temperature Total solar Insolation 65. 50 [F]1123.00[Btu/ftA2*day]
************************************************************************************ ****** *calculation Results************************************************************************************* ******
--Emission summary
Item uncontrolled [ton/yr] Total HAPS 0.000 Total HC 0.174 voes, C2+ 0.157 voes, C3+ 0.145
uncontrolled Recovery Info.
No
1 2 3 4 5 6 7 8 9 10 11
Vapor HC vapor GOR
8.5700 xlE-38.0800 xlE-326.29
Emission composition
Component uncontrolled [ton/yr] H2S 0.001 02 0.000 CO2 0.009 N2 0.000 Cl 0.017 C2 0.013 C3 0.032 i-c4 0.013 n-C4 0.042 i-c5 0.017 n-c5 0.020
Uncontrolled [lb/hr] 0.000 0.040 0.036 0.033
[MSCFD] [MSCFD] [SCF/bbl]
uncontrolled [lb/hr] 0.000 0.000 0.002 0.000 0.004 0.003 0.007 0.003 0.010 0.004 0.005 Page 2
Page F-220
Attachment F. Air Quality Permit Application Review Documents
•
12 C6 13 c7 14 cs 15 C9 16 ClO+ 17 Benzene 18 Toluene 19 E-Benzene20 Xylenes 21 n-c622 224Trimethylp Total
stream Data
0.006 0.006 0.002 0.000 0.000 0.000 0.000 0.000 0.000 0.004 0.000 0.182
Tank 1 Emissions.txt 0.001 0.001 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.001 0.000 0.042
---------------------------------------------------------------------------No. component Total Emissions MW LP Oil Fl ash oil sale oil Flash Gas w&s Gas
mol % mol % mol % mol % mol % mol % 1 H2S 34.80 0.0508 0.0349 0.0010 0.6834 0.0657 0.5435 2 02 32.00 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 3 CO2 44.01 0.2437 0.0907 0.0000 6.3467 0.0001 4.9092 4 N2 28.01 0.0102 0.0005 0.0000 0.3990 0.0001 0.3087 5 Cl 16.04 0.9543 0.1475 0.0000 33 .1362 0.0001 25.6311 6 C2 30.07 0.6701 0.3531 0.0000 13. 3133 0.0001 10.2979 7 C3 44.10 2.1827 1. 7648 0.3098 18.8508 12.6125 17.4378 8 i-C4 58.12 1.1269 1.0450 0. 5408 4.3934 9.3522 5.5165 9 n-C4 58.12 4.6091 4.4100 2.8709 12.5490 34.3185 17.4797 10 i-c5 72.15 3 .1066 3.0997 2.7402 3.3810 13.0110 5.5621 11 n-c5 72.15 5.0558 5.0823 4.7421 4.0000 16.4491 6.8196 12 C6 86.16 4.1726 4.2520 4.3903 1.0044 4.6741 1. 8355 13 c7 100.20 10.3655 10.6043 11. 2777 0.8388 4.1346 1. 5853Page 2----------------------------------------------------------------E&P TANK
14 CB 114.23 10.8426 11.1074 11. 9365 0.2806 1.4375 0.5426 15 C9 128.28 5.5127 5.6497 6.0913 0.0497 0.2624 0.0979 16 ClO+ 166.00 45.9695 47.1217 50.8962 0.0099 0.0544 0.0200 17 Benzene 78.11 0.5685 0.5808 0.6114 0.0778 0.3692 0.1438 18 Toluene 92.13 0.2132 0.2183 0.2341 0.0082 0.0407 0.0155 19 E-Benzene 106.17 0.0711 0.0729 0.0785 0.0009 0.0046 0.0017 20 Xylenes 106.17 0.6802 0.6971 0.7513 0.0075 0.0387 0.0146 21 n-C6 86.18 3.5939 3.6672 3.8242 0.6694 3.1745 1. 2368 Page 3
Page F-221
Attachment F. Air Quality Permit Application Review Documents
Tank 1 Emissions.txt 22 224Trimethylp 114.24 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
MW 123.89 126.03 130.08 38.64 65.28 44.68 Stream Mole Ratio 1.0000 0.9755 0.9684 0.0245 0.0072 0.0316 Heating value [BTU/SCF] 2044.13 3627.44 2402.74 Gas Gravity [Gas/Air] 1. 33 2.25 1. 54Bubble Pt.@ l00F [psi a] 56.28 19.66 5.57
RVP @ lO0F [psi a] 126.75 78.89 35.25
Spec. Gravity@ lO0F 0.800 0.803 0.811
Page 4
Page F-222
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report
ldentlncaUon
User Identification: City:
State:
Company:
Type of Tank:
Description:
Tank Dimensions Shell Length (ft):
Diameter (ft):
Volume (gallons):
Turnovers:
Net Throughput(gal/yr):
Is Tank Heated (y/n): Is Tank Underground (yin)
Paint Characteristics Shell Color/Shade:
Shell Condition
Breather Vent Settings
Vacuum Settings (psig):
Pressure Settings (psig)
TANKS 4.0.9d
Emissions Report -Detail Fonnat
Tank lndentification and Physical Characteristics
TK-2
West Virginia
Horizontal Tank Used Oil Aboveground Storage Tank
N N
Gray/Light
Good
20.00
4.61 2,500.00
5.00
12,500.00
-0.03
0.03
Meterological Data used in Emissions Calculations: Charleston, West Virginia (Avg Atmospheric Pressure= 14.25 psia)
file:///C:/Program%20Files%20(x86)/Tanks409d/summarydisplay.htm
Page I of 6
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Page F-223
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report
TK-2 • Horizontal Tank
TANKS 4.0.9d
Emissions Report - Detail Format
Liquid Contents of Storage Tank
Liquid DaK)'Uquid 51.rl. Bulk Tempenrti.re (deg F) Temp Vap« Vapot Presll.l'e (psla) Mol
Mbcture/Comporient Month Avg. Min. Max. (Mg F) Avg. Min. Mu Weight.
Liquid Mass
Fract
UsedOi Al 81.57 52.97 70.19 57.Z2 0.0001 0 0001 0 0001 3&0 0000
v-Mau MDI Basis tor Vapor Pressure
Fr11Cl Weig\t Celc:ulaUcm
Page 2 of 6
200.00 Option 1 VPeO = 0001 VP70 • 0001
file:///C:/Program%20Files%20(x86)/Tanks409d/summarydisplay.htm 6/5/2017
Page F-224
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report
TK-2 -Horizontal Tank
Annual En"isslon Calcaulations
Standing Losses (lb): Vapor Space Volume (cu ft): Vapor Density (lb/cu ft): Vapor Space Expansion Factor Vented Vapor Satoratlon Fac:l:or
Taoik Vap« Space Volume: Vapor Space Volume (cu ft): Taik Diameter (ft): Effective Oiamet« (ft}: VafKY Space Outage (ft): Tank Shel Lenglh (ft):
Vapor Density Vapor Density (lb/cu ft): Vapor Mcleculw Weight (lb/lb-mole): Vapor Presswa at Daily Average Liquid Sorface Temperature (psla): Daily Avg Liquid Su1aca Teffll. (deg R) Daily Average Ambient Temp. (deg. F): Ideal Gas Constant R (p,Ja cuft / (lb-mokleg RI): Liquid Bulk T11r11>eralure (deg. R): Ta,k Pwnt Solar Absorptance (Shell): Oaiy Total Solar lnst.1lation Factcr (Btulsqft day)·
Vapor Space Expansion Factor Vapor Space Expansion Factor Daily Vapor Temperature Range (deg. R): Daily Vapor Prnaure Range (psia): Breather Vent Presa. Setting Range(psia): Vapor Pttssu'II at Daily Avenige l.kp.,id Surfaoa T ernperature (psia): V9f)fl Ptesswe at Oaity Mirimum l.kp,fd Surface Temperature (psi a): Vapor Pres.ua at Oaitf Maximum l.iql,id Sufece Temperalwa (psia); Daily Avg. Liquid 51.rlace Temp. (deg R): Daity Min. l.Jq.Jld &.face Temp. (deg R): Daily Max. Liquid &Jttace Ta"" (deg R): Daily An'Clent Te"ll. Raige (deg. R):
Vented Vapor Saturation Factor Vented Vapor Sat!Jration Factor Vapor Pressure at Daily Average Liquid: Surface Temperature (psia): Vapar Space Outage (ft):
Wotking l.0sses (lb): Vapor Molecul• \Nelght (lbfb.rnola): Vap« Ptesst,e at Daily Average Liquid Swfaca Temperature (psia): Annual Net Throughput (galfyr ): Annual Tlmovers: Turnover FactDr Tank Diameter (ft): W0tking Loss Product Fadar
Total Losses (lb):
00326 212 8288 DODOO 0.0818 I.DODD
2128288 46100 10 8375 23050 20.DDOO
DDDDD 380.0000
DDDD1 521.2427 5.Ull833
10 731 516 8933 05'00
1,250 5726
0.0818 34 4127 DODOO ......
00001
0.0001
DDDD1 521.2427 512.83Q5 529.a.t511 21.5333
I.DODD
00001 2 3050
0.0113 3,0 DODD
00001 12,500.0000 SDODD 1.0000 46100 I.DODD
00439
TANKS 4.0.9d
Emissions Report -Detail Fonnat
Detail Calculations (AP-42)
file:///C:/P rogram%20Files%20(x86)/Tanks409d/summarydisplay.htm
Page 3 of 6
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Page F-225
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report Page 4 of 6
•
file:///C:/Program%20Files%20(x86)/Tanks409d/summarydisplay.htm 6/5/2017
Page F-226
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report
Emissions Report for: Annual
TK-2 -Horizontal Tank
II IComeonents II Jused Oil Ir
TANKS 4.0.9d
Emissions Report -Detail Fonnat
Individual Tank Emission Totals
Losses!lbsl
Wor1<i� Lossll Breathing LosslJ Total Emissions!
00111 0 0311 0,04
file:// IC :/Program%20F i les%20( x86)/Tanks409d/summarydisplay .htm
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Page F-227
Attachment F. Air Quality Permit Application Review Documents
TANKS 4.0 Report Page 6 of 6
•
file:///C:/Program%20Files%20(x86)/Tanks409d/summarydisplay.htm 6/5/2017
Page F-228
Attachment F. Air Quality Permit Application Review Documents
-
A1TACHMENTD
VENDOR SPECIFICATIONS
•
ERM DOMINION -ACP-3SfA1lON
Page F-229
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Emissions Estimates
Taurus 70-10802S
Assumptions: pipeline natural gas, sea level, 4"/4" inl�t/outlet losses, nominal p_erformance ...,-,.�u .--
rueIrIow, 1nermaI NVX NVX 1..V ... v UMI..
Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm)
0 5941 63.54 23.79 9 2.3 25 3.9 25
59 5430 56.92 24.27 9 2.0 25 3.4 25
100 4341 49.58 22.28 9 1.7 25 3.0 25 ,.,..,., 1oag -
fuel flow, Thermal NOx NOx co co UHC
Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm)
0 8912 7ti.1:11 29.49 9 2.8 25 4.7 25
59 8145 68.47 30.27 9 2.5 25 4.2 25
100 6512 59.08 28.05 9 2.1 25 3.5 25 ·,vv,., ioag
fuel flow, Thermal NOx NOx co co UHC
Temp, F HP mmbtu/hr LHV Eff, % (ppm) (lb/hr) (ppm) (lb/hr) (ppm)
0 11882 87.27 34.64 9 3.2 25 5.3 25
59 10860 79.24 34.87 9 2.8 25 4.8 25
100 8683 68.40 32.30 9 2.4 25 4.1 25
un ... vv ... vv ... ' '"'u" rmtu•"·" rn,ov,".11 cxnaust cxnaust rIow
(lb/hr) (ppm) (lb/hr) lb#hr lb/mmbtu lb/hr Temp (F) (lb/hr)
2.2 2.5 0.2 0.1;ll 0.02 1.4 910 199,373
2.0 2.5 0.2 74-07 0.02 1.3 991 170,275
1.7 2.5 0.2 633ti 0.02 1.1 1045 149576
-
UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp(F) (lb/hr)
2.7 2.5 0.3 l� 0.02 1.7 898 224,735
2.4 2.5 0.2 8905 0.02 1.5 957 194,658
2.0 2.5 0.2 7544 0.02 1.3 1019 165855
UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr)
3.1 2.5 0.3 11411 0.02 1.9 864 366,922
2.8 2.5 0.3 10301 0.02 1.7 908 334,207
2.3 2.5 0.2 8730 0.02 1.5 945 298619
Page F-230
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Emissions Estimates
Centaur 50-6200LS
Assumptions: pipeline natural gas, 150' elevation, 5"/lf' _i_rllet/outlet losses, n<>_min_al p_erformance -gv-�1�1,1 -·-
fuel flow, Thermal NOx NOx co co UHC
Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm)
0 3321 39.27 21.54 9 1.4 25 2.4 25
59 3006 35.20 21.73 9 1.3 25 2.1 25
100 2426 30.76 20.06 9 1.1 25 1.8 25 107e ioau -
fuel flow, Thermal NOx NOx co co UHC Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (ppm) (lb/hr) (ppm)
0 4981 47.21 26.85 9 1.7 25 2.9 25
59 4509 42.05 27.29 9 1.5 25 2.5 25
100 3639 36.70 25.23 9 1.3 25 2.2 25 lvv-,,. ,oaa
fuel flow, Thermal NOx NOx co co UHC
Temp, F HP mmbtu/hr LHV Eff,% (ppm) (lb/hr) (pp m) (lb/hr) (ppm)
0 6642 54.55 30.98 9 2.0 25 3.3 25
59 6012 50.72 30.16 9 1.8 25 3.1 25
100 4852 44.43 27.78 9 1.6 25 2.6 25
UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(lb/hr) (ppm) (lb/hr) lblhr lb/mmbtu lb/hr Temp(F) (lb/hr)
1.4 2.5 0.1 5155 0.02 0.9 837 139,384
1.2 2.5 0.1 4591 0.02 0.8 915 119,683
1.0 2.5 0.1 3938 0.02 0.7 966 103305 -
UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp(F) (lb/hr)
1.6 2.5 0.2 6189 0.02 1.0 849 152,889
1.5 2.5 0.2 5479 0.02 0.9 908 133,124
1.2 2.5 0.1 '4695 0.02 0.8 959 115664
---
UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr)
1.9 2.5 0.2 7145 0.02 1.2 871 161,184
1.7 2.5 0.2 6603 0.02 1.1 956 144,840
1.5 2.5 0.2 5679 0.02 1.0 1004 127484
Page F-231
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Emissions Estimates
Centaur 40-4700S
A ..OV'7o 1080 --
TUelTIOW, 1nerma1 nux
Temp, F HP mmbtu/hr LHV Eff, 0/4 (ppm)
0 2511 32.29 19.78 25
59 227.8 29.85 19.41 25
100 1735 26.09 16.92 25
fg79 IQilU -
fuel flow, Thermal NOx
Temp, F HP mmbtu/hr LHV Eff,% (ppm)
0 3767 39.31 24.39 25
59 3417 35.41 24.55 25
100 2602 30.78 21.51 25
llN7D"l!)aO
fuel flow, Thermal NOx
Temp, F HP mmbtu/hr LHV Eff,% (ppm)
0 5023 46.39 30.23 25
59 4556 42.27 29.51 25
100 3470 35.07 27.45 25
. r
nux l,U l,U
(lb/hr) (ppm) (lb/hr)
3.2 50 3.9
3.0 50 3.6
2.6 50 3.1
NOx co co
(lb/hr) (ppm) (lb/hr)
3.9 50 4.8
3.5 50 4.3
3.0 50 3.7
-
NOx co co
(lb/hr) (ppm) (lb/hr)
4.7 50 5.7
4.2 50 5.1
3.4 50 4.2
UH<; UMl, YU\# Y\J\# .. .., ... ,....,,v,.,..11 r-m,u,.,..11 cxnaust cxnaust Flow
(ppm) (lb/hr) (ppm) (lb/hr) lblhr lb/mmbtu lb/hr Temp(F) (lb/hr)
25 1.1 2.5 0.1 4259 0.02 0.7 726 140,550
25 1.0 2.5 0.1 3911 0.02 0.7 818 122.244
25 0.9 2.5 0.1 3355 0.02 0.6 876 106980
UHC UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(ppm) (lb/hr) (ppm) (lb/hr) lblhr lb/mmbtu lb/hr Temp (F) (lb/hr)
25 1.4 2.5 0.1 5177 0.02 0.9 736 156.668
25 1.2 2.5 0.1 46.35 0.02 0.8 810 136,464
25 1.0 2.5 0.1 3955 0.02 0.7 873 117366 -I ' UHC UHC voe voe CO2 PM10/2.5 PM10/2.5 Exhaust Exhaust Flow
(ppm) (lb/hr) (ppm) (lb/hr) lb/hr lb/mmbtu lb/hr Temp (F) (lb/hr)
25 1.6 2.5 0.2 6100 0.02 1.0 779 164,995
25 1.5 2.5 0.2 5526 0.02 0.9 840 148,793
25 1.2 2.5 0.1 4503 0.02 0.8 873 127331
Page F-232
Attachment F. Air Quality Permit Application Review Documents
SolarTurbines PIL 167 A Caterpillar Company . . Product lnformat1on Letter
PURPOSE
SoLoNOx Products:
Emissions in Non-SoLoNOx Modes
Leslie Witherspoon
Solar Turbines Incorporated
Solar's gas turbine dry low NOx emissions combustion systems, known as SoLoNOx ™,
have been developed to provide the lowest emissions possible during normal operating
conditions. In order to optimize the performance of the turbine, the combustion and fuel
systems are designed to reduce NOx, CO and unburned hydrocarbons (UHC) without
penalizing stability or transient capabilities. At very low load and cold temperature
extremes, the SoLoNOx system must be controlled differently in order to assure stable
operation. The required adjustments to the turbine controls at these conditions cause
emissions to increase.
The purpose of this Product Information Letter is to provide emissions estimates, and in
some cases warrantable emissions for NOx, CO and UHC, at off-design conditions.
Historically, regulatory agencies have not required a specific emissions level to be met at
low load or cold ambient operating conditions, but have asked what emissions levels are
expected. The expected values are necessary to appropriately estimate emissions for
annual emissions inventory purposes and for New Source Review applicability
determinations and permitting.
COLD AMBIENT EMISSIONS ESTIMATES
Solars standard temperature range warranty for gas turbines with SoLoNOx combustion
is � 0 °F (-20 °C). The Titan ™ 250 is an exception, with a lower standard warranty at
� -20°F (-29°C). At ambient temperatures below 0 °F, many of Solar's turbine engine
models are controlled to increase pilot fuel to improve flame stability and emissions are
higher. Without the increase in pilot fuel at temperatures below 0 °F the engines may
exhibit combustor rumble, as operation may be near the lean stability limit.
If a cold ambient emissions warranty is requested, a new production turbine configured
with the latest combustion hardware is required. For most models this refers to the
inclusion of Cold Ambient Fuel Control Logic.
Emissions warranties are not offered for ambient temperatures below -20 °F (-29°C). In
addition, cold ambient emissions warranties cannot be offered for the Centaur® 40
turbine.
Table 1 provides expected and warrantable (upon Solar's documented approval)
emissions levels for Solar's SoLoNOx combustion turbines. All emissions levels are in
ppm at 15% 02. Refer to Product Information Letter 205 for Mercury™ 50 turbine
emissions estimates.
For information on the availability and approvals for cold ambient temperature emissions
warranties, please contact Solar's sales representatives.
PIL 167 Revision 4 1 6 June 2012
© 2012 Solar Turbines Incorporated
Page F-233
Attachment F. Air Quality Permit Application Review Documents
•
Solar Turbines Incorporated Product Information Letter 167
Table 2 summarizes "expected" emissions levels for ambient temperatures below 0°F
(-20°C) for Solar's SoLoNOx turbines that do not have current production hardware or for
new production hardware that is not equipped with the cold ambient fuel control logic.
The emissions levels are extrapolated from San Diego factory tests and may vary at
extreme temperatures and as a result of variations in other parameters, such as fuel
composition, fuel quality, etc.
For more conservative NOx emissions estimate for new equipment, customers can refer
to the New Source Performance Standard (NSPS) 40CFR60, subpart KKKK, where the
allowable NOx emissions level for ambient temperatures < 0°F (-20°F) is 150 ppm NOx
at 15% 02. For pre-February 18, 2005, SoLoNOx combustion turbines subject to
40CFR60 subpart GG, a conservative estimate is the appropriate subpart GG emissions
level. Subpart GG levels range from 150 to 214 ppm NOx at 15% 02 depending on the
turbine model.
Table 3 summarizes emissions levels for ambient temperatures below -20°F (-29 °C) for
the Titan 250.
Table 1. Warrantable Emissions Between 0°F and-20°F (-20° to -29 °C)
for New Production
Turbine Fuel System Fuel Applicable NOx, co,
Model Load ppm ppm
Gas Only Gas 50 to 100% load 42 100 Centaur50 Dual Fuel Gas 50 to 100% load 72 100
Taurus™ 60 Gas Only or Dual Fuel Gas 50 to 1 00% load 42 100
Taurus 65 Gas Only Gas 50 to 100% load 42 100
Taurus 70 Gas Only or Dual Fuel Gas 50 to 100% load 42 100
Mars®go Gas Only Gas 50 to 100% load 42 100
Mars 100 Gas Only or Dual Fuel Gas 50 to 1 00% load 42 100
Titan 130 Gas Only or Dual Fuel Gas 50 to 100% load 42 100
Gas Only Gas 40 to 100% load 25 50 Titan 250 Gas Only 40 to 100% load 15 25 Gas
Centaur50 Dual Fuel Liquid 65 to 1 00% load 120 150
Taurus60 Dual Fuel Liquid 65 to 100% load 120 150
Taurus70 Dual Fuel Liquid 65 to 100% load 120 150
Mars 100 Dual Fuel Liquid 65 to 100% load 120 150
Titan 130 Dual Fuel Liquid 65 to 100% load 120 150
PIL 167 Revision 4 2
© 2012 Solar Turbines Incorporated
UHC,
ppm
50
50
50
50
50
50
50
50
25
25
75
75
75
75
75
6 June 2012
Page F-234
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated Product Information Letter 167
Table 2. Expected Emissions below 0°F (-20 °C) for SoLoNOx Combustion
Turbines
Turbine Fuel System Fuel Applicable NOx, co,
Model Load ppm ppm
Centaur40 Gas Only or Dual Fuel Gas 80 to 100% load 120 150
Gas Only Gas 50 to 100% load 120 150 Centaur50 Dual Fuel Gas 50 to 100% load 120 150
Taurus 60 Gas Only or Dual Fuel Gas 50 to 100% load 120 150
Taurus 65 Gas Only Gas 50 to 100% load 120 150
Taurus 70 Gas Only or Dual Fuel Gas 50 to 100% load 120 150
Mars 90 Gas Only Gas 80 to 100% load 120 150
Mars 100 Gas Only or Dual Fuel Gas 50 to 100% load 120 150
Titan 130 Gas Only or Dual Fuel Gas 50 to 100% load 120 150
Centaur40 Dual Fuel Liquid 80 to 100% load 120 150
Centaur50 Dual Fuel Liquid 65 to 100% load 120 150
Taurus60 Dual Fuel Liquid 65 to 100% load 120 150
Taurus 70 Dual Fuel Liquid 65 to 100% load 120 150
Mars 100 Dual Fuel Liquid 65 to 100% load 120 150
Titan 130 Dual Fuel Liquid 65 to 100% load 120 150
UHC,
ppm
50
50
50
50
50
50
50
50
50
75
75
75
75
75
75
Table 3. Expected Emissions below-20°F (-29 °C) for the Titan 250 SoLoNOx
Combustion Turbine
Turbine Fuel System Fuel Applicable NOx, co, UHC,
Model Load ppm ppm ppm
Titan 250 Gas Only Gas 40 to 100% load 70 150 50
COLD AMBIENT PERMITTING STRATEGY
There are several permitting options to consider when permitting in cold ambient
climates. Customers can use a tiered permitting approach or choose to permit a single
emission rate over all temperatures. Historically, most construction and operating
permits were silent on the ambient temperature boundaries for SoLoNOx operation.
Some customers have used a tiered permitting strategy. For purposes of compliance
and annual emissions inventories, a digital thermometer is installed to record ambient
temperature. The amount of time is recorded that the ambient temperature falls below
0 °F. The amount of time below 0 °F is then used with the emissions estimates shown in
Tables 1 and 2 to estimate "actual" emissions during sub-zero operation.
A conservative alternative to using the NOx values in Tables 1, 2 and 3 is to reference
40CFR60 subpart KKKK, which allows 150 ppm NOx at 15% 02 for sub-zero operation.
For customers who wish to permit at a single emission rate over all ambient
temperatures, inlet air heating can be used to raise the engine inlet air temperature (T1)
above 0°F. With inlet air heating to keep T1 above 0 °F, standard emission warranty
levels may be offered.
Inlet air heating technology options include an electric resistance heater, an inlet air to
exhaust heat exchanger and a glycol heat exchanger.
If an emissions warranty is desired and ambient temperatures are commonly below
-20°F (-29°C), inlet air heating can be used to raise the turbine inlet temperature {T1 ) to
at least -20°F. In such cases, the values shown in Table 1 can be warranted for new
production.
PIL 167 Revision 4 3 6 June 2012
© 2012 Solar Turbines Incorporated
Page F-235
Attachment F. Air Quality Permit Application Review Documents
•
Solar Turbines Incorporated Product Information Letter 167
EMISSIONS ESTIMATES IN NON-SOLONOX MODE (LOW LOAD)
At operating loads < 50% (<40% load for the Titan 250) on natural gas fuel and < 65%
(< 80% load for Centaur 40) on liquid fuels, SoLoNOx engines are controlled to increase
stability and transient response capability. The control steps that are required affect
emissions in two ways: 1) pilot fuel flow is increased, increasing NOx emissions, and 2)
airflow through the combustor is increased, increasing CO emissions. Note that the load
levels are approximate. Engine controls are triggered either by power output for single­
shaft engines or gas producer speed for two-shaft engines.
A conservative method for estimating emissions of NOx at low loads is to use the
applicable NSPS: 40CFR60 subpart GG or KKKK. For projects that commence
construction after February 18, 2005, subpart KKKK is the applicable NSPS and contains
a NOx level of 150 ppm @ 15% 02 for operating loads less than 75%.
Table 4 provides estimates of NOx, CO, and UHC emissions when operating in non­
SoloNOx mode for natural gas or liquid fuel. The estimated emissions can be assumed
to vary linearly as load is decreased from just below 50% load for natural gas (or 65%
load for liquid fuel) to idle.
The estimates in Table 4 apply for any product for gas only or dual fuel systems using
pipeline quality natural gas. Refer to Product Information Letter 205 for Mercury 50
emissions estimates.
Table 4. Estimated Emissions in non-SoLoNOx Mode
Ambient Fuel System Engine Load NOx,ppm CO,ppm
Centaur 40150, Taurus 60/65no, Mars 90/100, Titan 130
2: -20"F (-29°C) Natural Gas Less than 50% 70
Idle 50
< -20°F (-29°C)Natural Gas Less than 50% 120
Idle 120
Titan 250
2: -20"F (-29"C) Natural Gas Less than 40% 50
Idle 50
< -20°F (-29°C) Natural Gas Less than 40% 70
Idle 70
Centaur 50, Taurus sono, Mars 100, Titan 130
2: -20"F (-29°C)
< -20°F (-29°C)
2: -20°F (-29°C)
< -20°F (-29°C)
Solar Turbines Incorporated
9330 Sky Park Court
San Diego, CA 92123-5398
Liquid
Liquid
Liquid
Liquid
Caterpillar is a registered trademark of Caterpillar Inc.
Less than 65% 120
Idle 120
Less than 65% 120
Idle 120
Centaur40
Less than 80% 120
Idle 120
Less than 80% 120
Idle 120
8,000
10,000
8,000
10,000
25
2,000
150
2,000
1,000
10,000
1,000
10,000
1,000
10,000
1,000
10,000
UHC, ppm
800
1,000
800
1,000
20
200
50
200
100
3,000
150
3,000
100
3,000
150
3,000
Solar, Titan, Mercury, Mars, Centaur and SoLoNOx are trademarks of Solar Turbines Incorporated. Specifications subject
to change without notice. Printed in U.S.A.
PIL 167 Revision 4 4 6 June 2012
© 2012 Solar Turbines Incorporated
Page F-236
Attachment F. Air Quality Permit Application Review Documents
SolarTurhines PIL 168 A Caterpillar Company Product In rormation Letter
Volatile Organic Compound, Sulfur Dioxide,
and Formaldehyde Emission Estimates
Leslie Witherspoon
Solar Turbines Incorporated
PURPOSE
This Product Information Letter summarizes me­
thods that are available to estimate emissions of
volatile organic compounds (VOC), sulfur dio­
xide (SO2), and formaldehyde from gas turbines.
Emissions estimates of these pollutants are of­
ten necessary during the air permitting process.
INTRODUCTION
In absence of site-specific or representative
source test data, Solar refers customers to a
United States Environmental Protection Agency
(EPA) document titled "AP-42" or other appro­
priate EPA reference documents. AP-42 is a
collection of emission factors for different emis­
sion sources. The emission factors found in AP-
42 provide a generally accepted way of estimat­
ing emissions when more representative data
are not available. The most recent version of
AP-42 (dated April 2000) can be found at:
http://www.epa.gov/ttn/chief/ap42/ch03/index.html
Solar does not typically warranty the emission
rates for voe, SO2 or formaldehyde.
Volatile Organic Compounds
Many permitting agencies require gas turbine
users to estimate emissions of VOC, a subpart
of the unburned hydrocarbon (UHC) emissions,
during the air permitting process. Volatile organ­
ic compounds, non-methane hydrocarbons
(NMHC), and reactive organic gases (ROG) are
some of the many ways of referring to the non­
methane (and non-ethane) portion of an "un­
burned hydrocarbon" emission estimate.
For natural gas fuel, Solar's customers use 10-
20% of the UHC emission rate to represent voe
PIL 168, Rev 4
Caterpillar: Confidential Green
emissions. The estimate of 10-20% is based on
a ratio of total non-methane hydrocarbons to
total organic compounds. The use of 10-20%
provides a conservative estimate of voe emis­
sions. The balance of the UHC is assumed to
be primarily methane.
For liquid fuel, it is appropriate to estimate that
100% of the UHC emission estimate is voe.
Sulfur Dioxide
Sulfur dioxide emissions are produced by con­
version of sulfur in the fuel to SO 2 , Since Solar
does not control the amount of sulfur in the fuel,
we are unable to predict SO2 emissions without
a site fuel composition analysis. Customers
generally estimate SO2 emissions with a mass
balance calculation by assuming that any sulfur
in the fuel will convert to SO2. For reference, the
typical mass balance equation is shown below.
Variables: wt % of sulfur in fuel
Btu/lb fuel (LHV*)
MMBtu/hr fuel flow (LHV)
lb SO, =(
wt%Sulfur
)(
lb fuel
)(
10 6 Btu
)(
MMBtu fuel
)(
MW SO,
)hr l00 Btu MMBtu hr MW Sulfur
As an alternative to the mass balance calcula­
tion, EPA's AP-42 document can be used. AP-
42 (Table 3.1-2a, April 2000) suggests emission
factors of 0.0034 lb/MMBtu for gas fuel (HHV*)
and 0.033 lb/MMBtu for liquid fuel (HHV).
·LHV = Lower Heating Value; HHV = Higher Heating Value
Formaldehyde
In gas turbines, formaldehyde emissions are a
result of incomplete combustion. Formaldehyde
14 May 2012
Page F-237
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
in the exhaust stream is unstable and very diffi­
cult to measure. In addition to turbine characte­
ristics including combustor design, size, main­
tenance history, and load profile, the formalde­
hyde emission level is also affected by:
•Ambient temperature
•Humidity
•Atmospheric pressure
•Fuel quality
•Formaldehyde concentration in
the ambient air
•Test method measurement variability
•Operational factors
The emission factor data in Table 1 is an excerpt
from an EPA memo: "Revised HAP Emission
Product Information Letter 168
Factors for Stationary Combustion Turbines,
8/22/03." The memo presents hazardous air pol­
lutant (HAP) emission factor data in several cat­
egories including: mean, median, maximum,
and minimum. The emission factors in the
memo are a compilation of the HAP data EPA
collected during the Maximum Achievable Con­
trol Technology (MACT) standard development
process. The emission factor documentation
shows there is a high degree of variability in
formaldehyde emissions from gas turbines, de­
pending on the manufacturer, rating size of
equipment, combustor design, and testing
events. To estimate formaldehyde emissions
from gas turbines, users should use the emis­
sion factor(s) that best represent the gas tur­
bines actual / planned operating profile. Refer to
the memo for alternative emission factors.
Table 1. EPA 's Total HAP and Formaldehyde Emission Factors for <50 MW Lean-Premix
Gas Turbines burning Natural Gas
(Source: Revised HAP Emission Factors for Stationary Combustion Turbines, OAR-2002-0060, IV-B-09, 8/22/03)
Pollutant Engine
Load
Total HAP >90%
Total HAP All
Formaldehyde >90%
Formaldehyde All
Solar Turbines Incorporated
9330 Sky Park Court
San Diego, CA 92123-5398
95% Upper Confidence of
Mean, lb/MMBtu HHV
0.00144
0.00160
0.00127
0.00143
Caterpillar is a registered trademark of Caterpillar Inc.
95% Upper Confidence of
Data, lb/MMBtu HHV
0.00258
0.00305
0.00241
0.00288
Solar is a trademark of Solar Turbines Incorporated. Specifications subject to change without notice.
Printed in U.S.A. © 2008 Solar Turbines Incorporated. All rights reserved.
PIL 168, Rev 4 2
Caterpillar: Confidential Green
Memo Reference
Table 19
Table 16
Table 19
Table 16
14 May 2012
Page F-238
Attachment F. Air Quality Permit Application Review Documents
SolarTurbines PIL 170 A Caterpillar Company . . Product lntonnat1011 Letter
Emission Estimates at Start-up, Shutdown, and
Commissioning for SoLoNOx Combustion
Products
PURPOSE
Leslie Witherspoon
Solar Turbines Incorporated
The purpose of this Product Information Letter (PIL) is to provide emission estimates for
start-up and shutdown events for Solar® gas turbines with SoLoNOx™ dry low emissions
combustion systems. The commissioning process is also discussed.
INTRODUCTION
The information presented in this document is representative for both generator set (GS)
and compressor seUmechanical drive (CS/MD) combustion turbine applications. Opera­
tion of duct burners and/or any add-on control equipment is not accounted for in the
emissions estimates. Emissions related to the start-up, shutdown, and commissioning of
combustion turbines will not be guaranteed or warranted.
Combustion turbine start-up occurs in one of three modes: cold, warm, or hot. On large,
utility size, combustion turbines, the start-up time varies by the "mode". The start-up dura­
tion for a hot, warm, or cold Solar turbine is less than 10 minutes in simple-cycle and
most combined heat and power applications.
Heat recovery steam generator (HRSG) steam pressure is usually 250 psig or less. At
250 psig or less, thermal stress within the HRSG is minimized and, therefore, firing ramp­
up is not limited. However, some combined heat and power plant applications will desire
or dictate longer start-up times, therefore emissions assuming a 60-minute start are also
estimated.
A typical shutdown for a Solar turbine is <10 minutes. Emissions estimates for an elon­
gated shutdown, 30-minutes, are also included.
Start-up and shutdown emissions estimates for the Mercury™ 50 engine are found in PIL
205.
For start-up and shutdown emissions estimates for conventional combustion turbines,
landfill gas, digester gas, or other alternative fuel applications, contact Solar's Environ­
mental Programs Department.
START-UP SEQUENCE
The start-up sequence, or getting to SoLoNOx combustion mode, takes three steps:
1.Purge-crank
2.Ignition and acceleration to idle
3.Loading / thermal stabilization
During the "purge-crank" step, rotation of the turbine shaft is accomplished with a starter
motor to remove any residual fuel gas in the engine flow path and exhaust. During "igni-
PIL 170 Revision 5 1 13 June 2012
© 2012 Solar Turbines Incorporated
Page F-239
Attachment F. Air Quality Permit Application Review Documents
•
Solar Turbines Incorporated Product Information Letter 170
tion and acceleration to idle," fuel is introduced into the combustor and ignited in a diffu­
sion flame mode and the engine rotor is accelerated to idle speed.
The third step consists of applying up to 50% load 1 while allowing the combustion flame
to transition and stabilize. Once 50% load is achieved, the turbine transitions to SoLoNOx
combustion mode and the engine control system begins to hold the combustion primary
zone temperature and limit pilot fuel to achieve the targeted nitrogen oxides (NOx), car­
bon monoxide (CO), and unburned hydrocarbons (UHC) emission levels.
Steps 2 and 3 are short-term transient conditions making up less than 10 minutes.
SHUTDOWN PROCESS
Normal, planned cool down/shutdown duration varies by engine model. The Centaw® 40,
Centaur 50, Taurus™ 60, and Taurus 65 engines take about 5 minutes. The Taurus 70,
Mars® 90 and 100, Titan ™ 130 and Titan 250 engines take about 10 minutes. Typically,
once the shutdown process starts, the emissions will remain in SoLoNOx mode for ap­
proximately 90 seconds and move into a transitional mode for the balance of the esti­
mated shutdown time (assuming the unit was operating at full-load).
START-UP AND SHUTDOWN EMISSIONS ESTIMATES
Tables 1 through 5 summarize the estimated pounds of emissions per start-up and shut­
down event for each product. Emissions estimates are presented for both GS and
CS/MD applications on both natural gas and liquid fuel (diesel #2). The emissions esti­
mates are calculated using empirical exhaust characteristics.
COMMISSIONING EMISSIONS
Commissioning generally takes place over a two-week period. Static testing, where no
combustion occurs, usually requires one week and no emissions are expected. Dynamic
testing, where combustion will occur, will see the engine start and shutdown a number of
times and a variety of loads will be placed on the system. It is impossible to predict how
long the turbine will run and in what combustion I emissions mode it will be running. The
dynamic testing period is generally followed by one to two days of "tune-up" during which
the turbine is running at various loads, most likely within low emissions mode (warranted
emissions range).
Solar Turbines Incorporated
9330 Sky Park Court
San Diego, CA 92123-5398
Caterpillar is a registered trademark of Caterpillar Inc.
Solar, Titan, Mars, Taurus, Mercury, Centaur. Saturn, SoLoNOx, and Turbotronic are trademarks of Solar
Turbines Incorporated. All other trademarks are the intellectual property of their respective companies.
Specifications are subject to change without notice.
1 40% load for the Titan 250 engine on natural gas. 65% load for all engines on liquid fuel (except
80% load for the Centaur 40).
PIL 170 Revision 5 2 13 June 2012
© 2012 Solar Turbines Incorporated
Page F-240
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
Table 1. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set Applications
10 Minute Start-up and 10 Minute Shutdown
Natural Gas Fuel
Data will NOT be warranted under any circumstances
Centaur 40 4701 S Centaur 50 6201 S Taurus 60 7901 S Taurus 65 8401S
Product Information Letter 170
NOx co UHC CO2 NOx co UHC NOx co co UHC I CO2 lbs lbs lbs lbs lbs lbs lbs lbs lbs lbs lbs 0.6 58.1 3 .3 3 0.8 75.0 0.11 711.5 0.9 85.11
Total Emissions e!r Shutdown !lbs� 0.31 25.51 1.51 1&0! 0.41 31.11 1.111 1!t-il ul 34.71 2.ol ml ul 38.21 2.21 23�
Taurus 70 10801S Mars 90 13002S GSC Mars 100 16002S GSC Titan 130 20501 S Titan 250 30002S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 (lbs) (lbs) fibs) fibs) (lbs) fibs) fibs) fibs) fibs) fibs! f ibs) (lhl) l lbs l fibs) llbsl llbsl llbsl llbsl llbsl llbsl Total Emissions Der Start llbs' 1.1 103.9 5.9 63,,1 1.4 129.0 7.4 11611 1.6 151.2 11.6 M1 2.1 195.6 11.2 1,1!1A 2.5 12.1 1.5 1.925
Total Emissions e!r Shutdown Ubsll ul 110.11 d � d 147.91 ul 91� 1.91 166.el 9.51 11026! 2.41 210.ol 12.ol 1,JOJ! 3.ol 19.91 d 1,99�
Assumes ISO conditions: 59F, 60% RH, sea level, no losses
Assumes unit is operating at full load prior to shutdown.
Assumes natural gas fuel; ES 9-98 compliant.
PIL 170 Revision 5
© 2012 Solar Turbines Incorporated
3 13 June 2012
Page F-241
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
Table 2.Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set Applications
60 Minute Start-up and 30 Minute Shutdown
Natural Gas Fuel
Data will NOT be warranted under any circumstances
Centaur 40 4701 S Centaur 50 6201 S Taurus 60 7901 S Taurus 65 8401 S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC
fibs) llbsl flbsl fibs) fibs) llbsl llbsl fibs) fibs) llbsl llbsl llbsl llbsl fibs\ llbsl I Total Emissions oer Start libs 4.1 219.4 13.0 3,4"1 5.0 m.4 16.1 4 215 5.7 299.8 17.8 4,71111 6.1 326.5 19.3
Product Information Letter 170
CO2
llbsl 5,074
TotalEmisslonsperShutdown(lbsl! 1.81121.11 1.111,44� 2.31163.31 9.511,Bl4! 2.51163.51 9.611.994! 2.61111.21 1ul 2.11�
Taurus 70 10801S Mars 90 13002S NOx co UHC CO2 NOx
llbsl (lbs) (lbs) (lbs) (lbs) I Total Emissions oer Start llbsl 7.6 410.3 24.2 6,164
I Total Emissions per Shutdown llbsll 3.3 223.0 13.0 2-l
Assumes ISO conditions: 59F, 60% RH, sea level, no losses.
Assumes unit is operating at full load prior to shutdown.
Assumes natural gas fuel; ES 9-98 compliant.
PIL 170 Revision 5
© 2012 Solar Turbines Incorporated
10.5
4.3
co UHC
llbal (lbs ) 570.8 33.7
m.o 16.2
CO2
(Iba) 8,641
3,685'
4
Mars 100 16002S Titan 130 20501 S Titan 250 30002S NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2
(lbs) (lbs) (lbs) (Iba) (Iba) llba) (lbs) llbal llbsl llbs) (lbs) (lbs) 11.3 583.5 34.6 9,691 13.8 740.4 43.8 11,495 14.6 75.5 7.3 16.253
4.8 308.1 18.0 4 056 6.0 405.3 23.7 4,8261 6.2 52.6 4.1 1,222
13 June 2012
Page F-242
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
Table 3. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx CS/MD Applications
10 Minute Start-up and 10 Minute Shutdown
Natural Gas Fuel
Data will NOT be warranted under any circumstances
Centaur 40 4702S Centaur 50 6102S Taurus 60 7802S
NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2
fibs) flhlll flhlll flhlll 11h11) Rbll Rhll) (lblil 11h11) llbsl (1h11) llhcl
Total Emissions D9f Start fibs o.7 &U 3.7 392 O.B 69.1 4.0 46!1 0.7 64.l 3.7 410
Total Emissions per Shutdown (lbsd 0.3� 1.1! ml Q..4� 2.oeml Q..4� 1.9�
Taurus 70 10302S Mars 90 13002S CSIID Mars 100 16002S CSMD Titan 130 20502S
NOx co UHC CO2 NOx co UHC CO2 NOx co UHC CO2 NOx co UHC
flbsl (lbs) fibs) flba) fibs) (lbs) fibs) llbl) fibs) (lbs) fibs) (Iba) fibs) (lbs) 111>11 Total Emissions 119r Start fibs 0.8 73.1 4.2 515 1.2 109.l 6.2 -1.4 123.5 7.1 12!1 1.9 176.9 10.1
Product Information Letter 170
Titan 250 30002S
CO2 NOx co UHC CO2
fibs) (lbsl flbsl fibs) llbsl 1,161 2.6 26.2 1.7 1,794
Total Emissions per Shutdown (lbs)! 1.1� 5.lr:=::ml 1.5� 1.&c:=im 1.7� B.5� u! 201.&! 11.s! 1.2n! 2.9� 1.4�
Assumes ISO conditions: 59F, 60% RH, sea level, no losses.
Assumes unit is operating at full load prior to shutdown.
Assumes natural gas fuel; ES 9-98 compliant.
PIL 170 Revision 5
© 2012 Solar Turbines Incorporated
5 13 June 2012
Page F-243
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
Table 4. Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set
10 Minute Start-up and 10 Minute Shutdown
Liquid Fuel (Diesel #2)
Data will NOT be warranted under any circumstances
Centaur 40 4701 S Centaur 50 6201S
NOx co UHC CO2 NOx co UHC
(lbs) (lbs) (lbs) (lbs) (lbs) (lbs) (lbs)
Total Emissions per Start (lbs) 1.3 44.5 7.4 473 1.7 59.0 9.8
CO2
(lbs)
601
Total Emissions per Shutdown (lbsI 0.6 17.3 2.8 211 0.71 21.2 3.41 256
Taurus 70 10801S
NOx co
(lbs\ fibs\
Total Emissions per Start (lbs) 2.3 78.5
Total Emissions per Shutdown (lb 2.5 73.6
Assumes ISO conditions: 59F, 60% RH, sea level, no losses.
Assumes unit is operating at full load prior to shutdown.
Assumes #2 Diesel fuel; ES 9-98 compliant.
PIL 170 Revision 5
© 2012 Solar Turbines Incorporated
UHC
fibs\
13.0
12.0
Mass 100 16002S GSC
CO2 NOx co UHC CO2
fibs\ fibs\ fibs\ fibs\ (lbs)
823 3.4 114.1 18.8 1,239
889 3.81 111.4 18.11 1 !331
6
Product Information Letter 170
Taurus 60 7901S
NOx co UHC CO2
(lbs) (lbs) (lbs) (lbs)
1.7 59.8 9.9 636
0.81 23.5 3.81 286
Titan 130 20501S
NOx co UHC CO2
(lbs) (lbs) (lbs) (lbs)
4.3 147.5 24.4 1,547
4.71 139.1 22.61 1 t6TT
13 June 2012
Page F-244
Attachment F. Air Quality Permit Application Review Documents
Solar Turbines Incorporated
Table 5.Estimation of Start-up and Shutdown Emissions (lbs/event) for SoLoNOx Generator Set
60 Minute Start-up and 30 Minute Shutdown
Liquid Fuel (Diesel #2)
Data will NOT be warranted under any circumstances
Centaur 40 4701 S
NOx co UHC CO2
(lbsl (lbsl (lbs) (lbsl
Total Emissions per Start (lbs) 11.7 194.7 30.9 4,255
Total Emissions per Shutdown (lbs 4.41 84.7 13.61 1,816
Taurus 70 10801S
NOx co
(lbs) (lbs)
Total Emissions per Start (lbsl 18.4 360.3
Total Emissions per Shutdown (lbs 8.01 207.8
Assumes ISO conditions: 59F, 60% RH, sea level, no losses.
Assumes unit is operating at full load prior to shutdown.
Assumes #2 Diesel fuel; ES 9-98 compliant.
PIL 170 Revision 5
© 2012 Solar Turbines Incorporated
UHC CO2
(lbs) (lbs)
57.4 7,375
34.11 3,156
Centaur 50 6201S
NOx co UHC CO2
(lbsl (lbs) (lbsl (lbs)
15.2 271.9 43.3 5,302
6.71 164.3 27.0I 2,334
Mars 100 16002S
NOx co UHC CO2
(lbs) (lbs) (lbs) (lbs)
29.1 552.0 87.7 11,685
12.31 302.6 49.41 4,970
7
Product Information Letter 170
Taurus 60 7901S
NOx co UHC CO2
(lbs) (lbs) Obs) (lbsl
14.7 282.6 45.0 5,962
6.31 159.0 26.0I 2,515
Titan 130 20501 S
NOx co UHC CO2
(lbsl (lbs) (lbsl (lbsl
34.4 6TT.0 108.0 13,731
15.0I 388.5 63.71 5,876
13 June 2012
Page F-245
Attachment F. Air Quality Permit Application Review Documents
SCR SYSTEM DESIGN DATASHEET
E--�-•»m
Revision
OallofR
0
01 -Sm-2015
?f\CC[S'.:. DAlA
0ngnc.,.
CvstmerOesignC1se
Pen::enlload
AU.ntk:Coasl
ACP-3
5mo1o
17
Perren!
Flad Case Percent
EXHAUST OAS EMISSIONS OAT A {BEFORE COOLING)
Exhaust Gas Mas, Fkwmlla, Wei
Exhaust Gas Voluneti: Fbwala, Wet
ExhaustGasT�erain
Exhaust G,as COl'!!92PI
C-MW
02 Jlffl
H2O 18 015
N2 28013 CO2 4'-010 ,., ,. ...
...
ACFM
degreesF
8nlssmttcrnlhlSotm Cl %02 15
Rtlemot•pplicatff b'ppmvd lldff9N'n](cr,1
NoxaNO2
NoxesN02
co
co
502
502
503
503
COOLINO AIR DATA
Cooling 111 Mass Fkntnla, Wei
Coc*lg 111 Vahmett: FVM'l9. Wet
Anoent/ul�•
Rtlaiv9Hll'rlicit1
EXHAUST GAS EMISSIONS DAT A (AFTER COOLING)
Exhaust Gas Mass Flowalt, Wei
Exhausl Gas Voluneh: FD'IM'ille Wet
ExhllustGatlfn1)81Ul(a�c:aoing}
l;;d!!il!I �1 Cmm:!1!!1 c-MW
02 31 .999
H20 18.015
N2 28 013
CO2 44.010 ,., ,. ...
-... -... -... -... ...
ACFM
OegeesF . ..,.,. ...
ACFM
degreesF
w1%(we0
-(weQ
""'(weQ
-(weQ ""'(weQ
Ernissi\;ns tan lhl §wee O %02 1s ........ .,.,..,..,,,,....,.,_,,...i
NoxaN02 ppTIYd
NoxaU02
co
co
S02
502
503
503
Amounl ol Nox as N02
Nox Red.ldiln
0.....,�Req,nd
0.....,�Req,nd
� Nl'fflClnil Req.li'Ement
AqueowMm:r\DRtq.semeN
TolalMass ...... bySCR
Exhaust Gas Mass Fb.nle, Wei al SCR catalyst
Exhaust Gu Vol FlcMfale, Wet al SCR Catalyst
... -... -... -...
Percent
Percent ...
SCFM ... -... ...
ACFM
prirmprq warranm a 'M>2 1s ........ .,.,..,..,,,,....,.,_,/">I
NoxaN02 � NoxasN02
NHJSip
NH351p
"VTA�v.n:b'b.Ad.ise
anon Mtient ffflD!rBltl'e
O......,AITtlientPresue
SiteBmlon
Glum Dvd Preswe
RelainHIITDN
100
407
VARIOUS
2000
6()
... -...
-F
inH20
ft
inH20 . ..,.,.
Cne1 c.,.2 C1so3 CI.Y!A
Cenllll'40 Cen!a,40 c .......... Ctn!:atrSOL '""' 100% 1'°" 100%
NG NG ''" NG
1S<"4 117,403 111184 11741,C
8121il 73SOO 91781 1!0971
mo 873.0 1710 1�.0
15.7 1529 ,.., .... .. , 8.15 55 '1
71123 7341 , ... 73.01
241 221 , .. 2.83 .., , ... 091 U7 """ 10000 100.00 100.00
2501 ""' ,M 100 4M 3 .. .. 1 55
Sl00 "'N 2500 2500 "' .,, lJ1 ,., 000 GOO 000 000
000 ... •00 000
0.11< '"' '"
0.00 000 •00
711112 278001 292709 57444 9
13&7 6438 5653 13303
000 100,00 000 10000
IG00 6()00 6()00 6000
172175 155203 190450 1!41129 ..... 1!093& ..,.. 96292
7Sl00 75000 75000 75000
15JI 1815 1573 15115 ... 7.Ja 472 755
78JO 7371 7821 7365
231 U7 243 1.97
091 o .. 0,1 oaa
10000 10000 10000 10000
2500 2506 ''° 904
4H 344 115 155
5000 50.13 2500 2511
5U 4.19 331 263
000 000 000 000
000 ODO 000 000
000 000 000 000
0.00 000 000 GOO
000 000 000 000
0.00 000 000 000
000 0.00 000 000
50 50 50 50
ao00 ao.oo .... ....
327 327 327 327 .. .. .. ..
11 •6 5
11)&a m ... '52
33& 335 333 332
172513.1 1555382 190787 8 1852608
U073 81113 "556 -
50 50 50 50
093 '" 109 0116
1000 10.03 1000 1004 '" 0.51 ... 0!4
AFCU DES!Gtl
R8 1Concenhtion
c..,s c .... c ... , c ... a c ... , CnetO Case ti Casel2
T1i.n,s60 T1\I\IS60 TNUSIO Tai,w70 Manl00 Mn100 Trtan131 Titan1.l>
100% 100% I 100% 100% 100% 100% 100%
NG NG NG NG NG NG NG NG
186880 151704 2'ns5 179824 3ST228 2!19"5 43715& 3'1226
107807 96052 139492 11-207193 1mea 25415& 215260
.... o 099.0 ,, ... fle0.0 IISll.0 11530 9000 11930
14.50 13.93 1439 13.18 14 .13 '4.23 1440 13.H
5.8 1 '·" .., ,.,. 5.81 ,.oa 510 1.55
75.78 n.116 7574 n91 7515 73.oa 75.75 12.aa
300 2.10 105 a3 2.10 '.76 304 3.01
0.91 087 U1 D.17 0.91 0.87 0.91 0.87
1DD.00 100.DD 100.DO 10000 100.0D 100.IIO 100.00 100.DD
15.M 1500 15.00 15M 1500 1500 1500 1500
397 3.18 ..... ,.n 7.51 573 , .. 7.Ja
25.00 2500 25DO 25.00 2500 2500 25.00 2500
4.02 3.20 '" ,., 7.ll2 581 ,.sa 7.49
0.00 0.00 '" 000 000 0.00 0.00 D.00
0.00 000 •oo 0.00 0.00 000 0.00
000 0.00 •oo 000 0.00 0.00 0.00 0.00
0.00 00 GOO •oo 0.00 0.00 0.00 0.00
38705.3 87D13D 400722 733733 600748 104237.f 91151l3J 1470994
7475 15518 7739 "'" 11801 24139 19040 3'0S4
000 10000 0.00 100 00 000 10000 000 10000
6000 6000 60.00 60.00 6()00 6000 6000 6000
225585 21B717 287332 253107 427303 ,.,.., 536550 4Ba325
118559 113020 141553 131945 220715 2051115 2n2c 2Sl4a4
750.00 75000 75000 750.00 75000 75000 75000 T5000
15!ii 1512 1529 15 .. 1550 1578 1550 1562 '" 7.87 511 11, 4!4 7.70 4!4 '·"
78 .18 7311 78.05 7355 78 .15 73,;e 78.16 735'
250 203 2.13 210 250 204 249 2.12 '" oea 091 a.ea D.91 088 0.91 , ..
10000 10000 100.0G 100.00 10000 10000 10000 10000
1500 1507 ISDG 15.06 1500 1500 1500 1500 "' 3.18 53' 372 7.51 573 ... 7.Ja
2500 25.11 2500 2510 2500 2509 2500 25.11
402 320 542 3.83 7.62 581 ,sa 7.49
000 000 0.00 000 000 000 000 000
000 000 0.00 000 000 000 000 000
000 000 ODO , .. 000 000 000 0.00
000 000 000 000 000 000 000 000 "" 000 000 0.00 000 000 000 000
000 000 000 000 000 000 000 000
000 000 0.00 000 000 000 000 000
50 50 50 50 50 50 50 50
&ail ... , 15.57 aa.&7 &887 6U7 a&67 6667
327 327 327 327 327 327 655 327 .. .. .. .. .. .. 135 ..
10 •"1D 20 15 25 11
tall 787 1331 '" 1873 1'29 235& 1'41
337 335 3'1 337 "' 3'2 &a0 344
2259226 2190522 2878730 253534 1 427549.1 »40245 5372294 488571 .5
116734 114005 14&729 132120 220965 205373 277594 254645
50 so 50 50 50 50 50 50
1.32 1.05 1.78 126 250 UI 3.15 24'1
1000 1004 1000 1004 1000 1004 1000 1004
Ota o,a 132 093 1.15 1.41 233 112
Page F-246
Attachment F. Air Quality Permit Application Review Documents
G3516B
ENGIN: SPEED (rpm): COMPRESSION RATIO: AFTERCOOL.ER TYPE: AFTERCOOLER • STAGE 2 INLET ('F): AFTERCOOLER • STAGE 1 INLET ('F): JACKET WATER OIJTLEr ("F). ASPIRATION: COOLING SYSTEM: CONTROL SYSTEM:
GAS ENGINE TECHNICAL DATA
1800 11 SCAC 130 192 198 TA JW+OC+1AC, 2AC ADEM3
RATING STRATEGY: APPLICATION RATING LEVEL FUEL: FUEL SYSTEM·
FUEL PRESSURE RANGE(pslg): FUEL METHANE NUMBER: FUEL LHV (Blu/ld):
STANDARD
GENSET
, ., CONTINUOUS
EXHAUST MANIFOLD: COMBUSTION: ORY LOW EMISSION 0.5
ALTITUDE CAPABILITY AT 7rF INLET AIR TEMP.(") POWER FACTOR:
NAT GAS CAT LOW PRESSURE WITH AIR FUa RATIO CONTROL 1.5-5 0 80 905 2238 0.8 380-4160 NOx EMISSION LEVEL (glbhp-hr NOxl. VOLTAGEM:
RATING NOTES LOAD 100% 75% 50%
GENSET POWER (WITHOUT FAN (1)(2) fl'r.W 1300 975 650
GENSET POWER (WITHOUT FAN (1)(2) kVA 1625 1218 B12
ENGINE POWER (WITHOUT FAN (2) bhp 1818 1384 910
GENERATOR EFFICIENCY (1) % 95.9 95.B 95.8
GENSET EFFICIENCY(@ 1.0 Pow11t Factcr) {150 3041111 (3) % 34.7 33.2 31.1
THERMAL EFFICIENCY (41 % so.a 52.3 54.5
TOTAi. EFFICIENCY 14111 1.0 Power Factarl (5) 'II, 85.5 BS.5 as.a
ENGINE DATA
GENSET FUEL CONSUMPTION (1S0304611 (6) Btu/ekW•hr 996S 10415 11036
GENSET FUEL CONSUMPTION (NOMINAL (6)Btu/ekW-hr 10158 10618 11250
ENGINE FUa CONSUMPTION (NOMINAL (6) Blu/llhf>-hr 7261 7589 8037
AIR FLOW (7rF, 14.7 psla) � (7) ftJ/mln 4121 3172 21BB
AIR FLOW (7 ) lb/hr 1B272 14067 9702
FUEL FLOW (60'F, 14.7 psla) lldm 243 191 13S
COMPRESSOR OUT PRESSURE In Hg(abs) 87.4 82.5 60.2
COMPRESSOR OUT TEMPERATURE 'F 345 326 234
AFTERCOOLER AIR OUT TEMPERATURE "F 129 130 130
INLET MAN. PRESSl.fiE (B) In Hg(abl) 79.9 62.9 43.8
INLET MAN. TEMPERATURE (MEASUREO IN PLENUM (9) "F 139 140 140
TIMING (10) 'BTDC 22 22 22
EXHAUST TEMPERATURE• ENGINE OUTLET (11) 'F 974 985 1009
EXHAUST GAS FLOW (@engtna outlet temp, 14 5 pita) (WET (12) ftllmln 11850 9202 6461
EXHAUST GAS MASS FLOW (WET (12) lb/llr 18939 14590 10072
MAX INLET RESTRICTION (13) lnH20 10.04 7.99 3.98 MAX EXHAUST RESTRICTION 113) lnH20 20.07 12.41 5.51
EMISSIONS DATA -ENGINE OUT
NOx(a1N02) (14)(15) glbhp-nr 0.50 0.50 0.50 co (14)(16) g/bhp-nr 2.49 2.58 2.82
THC (m ol. wt. of 15.84) (14)(16) glbhp,hr 5.45 5.B2 6.78
NMHC (mol wt. of 15 84) (14)ll6) glbhp-nr 0.62 O.B7 1.02
NMNEHC (VOC1) (mol wt. of 15 84) (14)(16)(17) g/bh!Hll 0.54 0.58 0.68
HCHO (Fcrmaldetlyde) (14)(115) g/bh!Hlr 0.34 0.37 0.42
CO2 (1-4)(16) g/bhJ>-llr 504 527 559
EXHAUST OXYGEN (14)(18) %DRY 9.3 9.1 9.0
LAMBDA (141118) 1.73 1.70 1.66
ENERGY BALANCE DATA
LHVINPUT (19) Blulmln 220051 172501 121849
HEAT REJECTION TO JACKET WATER (JW) (20)l28) Btu/min 28688 25137 21558
HEAT REJECTION TO ATMOSPHERE (21) Btu/min 7365 6138 4912
HEAT REJECTION TO LUBE OIL (OC) (22)(26) Btu/min 7401 6761 5967
HEAT REJECTION TO EXHAUST (LHV TO 77°F) (23)(24) Btu/min 811155 63518 45440
HEAT REJECTION TO EXHAUST (LHV TO 248'F) (23) Blulmln 61754 48372 34572
HEAT REJECTION TO AJC • STAGE 1 (1AC) (25)(28) Btu/min 9380 9325 1345
HEAT REJECTION TO AJC • STAGE 2 (2AC) (26)(29) Btu/min 7961 5809 3073
PUMP POWER 1271 Btu/min 977 977 977
CONDITIONS AND DEFINITIONS Engine l'lllklg oblalned and presented In accoroanca wt1h ISO 3046/1, (Slandard rarerence condijlons of 77°F, 29.60 In Hg barometric pressure.) N11 overload pe,mttted at ratJng
ahown, C01111Jft the a"ltud11 dera11oo fadar chart far appYcallons that axcead Iha rated aftHuda or temperature
Emission lllvals ara al engine 11xhaU&I llang11 prlllr l11 any aftar lrlllllment. Vakles ara ballld on angina operating Bl ateady state conlfflfons, adjustlld to Iha apaclfled NOx lllvel Bl 100% bad. Talenlncas apedfled in dapendl!lll upon fuel qualty Fuel methane numbllr cannot vezy more than :1: 3.
Far notes Information consult page three.
Dala � br Gas Engloa Rat1n11 Pro Version ll.01.ClO Raf Dal.I Bal DMS843--03-001, Plfnl8d 211Mar2016 Paga I of 5
Page F-247
Attachment F. Air Quality Permit Application Review Documents
•
G3516B GAS ENGINE TECHNICAL DATA lmlERPlllAR.
FUEL USAGE GUIDE I
CAT METHANE NUMBEA:.._1-_,;;;,3 0;;;.....+-...;3;.;;S�.,_...;40.;;....-+--45.;.;;;...-+....;;;5;;;,0�.,_;;;.;55;.._+-..;;60;;....-1-�65;;;.-+-...;7�0-l.,_.;,.75;;;.-+-...;B..;0_.,_1�00;,....-4I SET POINT TIMING 22 21 20 I 21 22 22 I
DERATION FACTOR::t----,oe---+----,oe---+----,o,,.....-+--o,,.....-+-0,,.....-+-o,,---+....,,.o_-=-94,--+-""0""'92,,.....+----,--+l--:-1 -+----,--+----,----ti
ALTITUDE DERATION FACTORS AT RATED SPEED I
130 0.99 0.95 0.92 0B8
120 1 0.97 0.93 090 INLET 110 1 0.99 0.95 092 AIR 100 1 1 0.97 0.113 TEMP 90 1 1 0.99 095 "F 1 1 1 OD7
70 1 1 1 098
80 1 1 1 1
50 1 1 1 1
0 1000 2000 3 000
AFTERCOOLER HEAT REJECTION FACTORS lACHRFI
130 1.34 1.39 145
120 1.27 1.32 1 38 INLET 110 1.20 1.25 131 AIR 100 1.13 1.18 124 TEMP 90 1.08 1.11 117 "F 80 1 1.05 1 09
70 1 1 102
60 1 1 1
5 0 1 1 1
0 1000 2000
Dela generated by Gas Engine Rating Pro Veralon 6 01.00 Ref. Data Set OM5643-03-001, Pmtlld 29Mar2D16
1.48
1.39
1.32
1.25 1.18
1.11
1.04
1
1
3000
I
0.85 0.82 0.79 0.78 073 0,70 067 0.84 0.82
0.87 0.83 O.BO 0.77 074 D.71 OBB 0.65 D.83
0.88 0.BS O.B1 0.78 075 D.72 089 0.67 D.s.t
0.90 0.86 0.83 OBO 077 0.74 0.71 0.68 0.85
0.91 O.B8 0.84 081 07B 0.75 0.72 0.69 0.156
0.93 0.89 o.ae 0.83 079 0,78 D.73 0.70 0.67
0.95 0,91 0,88 084 0.81 0,7B 0.75 0.72 0.6D
0.97 0.93 0.89 0_86 0.82 0,79 0 .76 0.73 0,70
0,98 0.95 0.91 0.87 0.84 0.81 0.78 0.74 071
4000 5000 6000 7000 8000 9000 10000 11000 12000
ALTITUDE (FEET ABOVE SEA LEVEL)
1.48 148 1.48 1.48 1.48 1416 1.4'8 148 1.48
UD 139 1.39 1.39 1 .39 139 1.39 139 1.39
1.32 132 1.32 1.32 1 .32 132 1.32 1.32 1.32
1.25 1-25 1.25 1 .25 1.25 125 1.25 125 1.25
1.18 1.18 1.18 1.1B 1.18 118 1.18 118 1.111
1.11 1.11 1.11 111 1.11 1.11 1. 11 1 .11 1 .11
1.04 1 D4 104 104 1 .04 1 D4 1 .04 1.04 1 .04
1 1 1 1 1 1 1 1 1
1 1 1 1 1 1 1 1 1
4000 6000 6000 7000 8000 9000 10000 11000 12000
ALTITUDE (FEET ABOVE SEA LEVEL)
Page 2of5
Page F-248
Attachment F. Air Quality Permit Application Review Documents
G3516B GAS ENGINE TECHNICAL DATA mRPILLAR.
FUEL USAGE GUIDE: This table lhows Iha denlle fador and ful load set point timing niqulntd for a given fuel Nola 11181 denlllan and 1111 point timing adju1tmlllll may be �ulnid u lhe mlllhane number decnl11111, Methane number Is a acaill ID meuure detonation chlnlderlstlcl Df vlriDu1 fuels. The rnelhlne number Df a fuel Is detennlned by using the Caterpllar ma1h-number cak;ulallon.
ALTITUDE DERATION FACTORS: This table shows the derallon n,qulred for various air Inlet temperatures and atltudes. Uu 1h11 lnfonnatlan along with the fual 1111111111 guide chllll lo help datennln11 actual angina i:>CJMI' lot your 11111. The derat11 flldora lhlllMI do not take Into account eictemat cooing system capaclly. The Clerate laden pravlded asaume the eictemal cooing 1yai.m can maintain Iha apecllied Clllllng water lemperatURII at 111111 candllona.
ACTUAL ENGINE RATING; To detennln11 the adual rating of the engine at 11111 conditions, one must conlllder 11e1111111tely, limllB1l01111 due to fuel chanidemtlca and air system lmllatlona. The Fuel Uaag11 Gulde dsallon establllhes fuel lmltatlona. The AIHude/Tamperature deratlon ladora and RPC (reference Iha caterpllat Mlllhana Plagram) astabUSh air system tlmltllllons. RPC comes Into play when 1h11 AltltudefTempel'lllure darallon la lesa than 1.0 (100%), Under this candlllon, add the MU fad0r1 together VI/hen the site ccndillons do not �ulre an Allltude/ Temperature defale (fador Is 1.0), It Is assumed 1h11 turt,ocharger has IUfllc:IIIJII capablllty to overcome the tow luel relatlve poMI', and RPC Is l11ncnd. To determine the 1ctu1l power avallable, take 1h11 kMllst rating blltwNn 1) and 2). 1) Fuel UAge Guida Dllrallon 2) 1-((1·Altlludllfl'emparature Deratlon) + (1·RPC))
AFTERCOOLER HEAT REJECTION FACTORSIACHRFI: To maintain a constant air Inlet manllDld temperature, 1111118 Inlet air tamperature goes up, so must Iha 111111 rejedlon. All altitude Increases, the tur1>oeharger must wurk harder to oven:ome 1h11 lo\wlr atmospheric pressure. This lncrlla11111 the amount of heat 11181 must be RIIIIOVed from 1h11 lnllll air by the afle11:00ler. Use !hi aftmmclar heat rejlldlon flldor (ACHRF) to adju51 for Inlet air temp 1111d dttudll condlllons. See notes 28 and 29 for applk:llllon of this factor In c:alculallng Iha heal exchanger slzlng crtterla. Failure to property ac:cow1t lor these fedora could resun In detonation 111d cau11 the engln• to shutdoMI or fall.
INLET AND EXHAUST RESTRICTIONS FOR ALTITUDE CAPABILITY: The alltude dera1e chart 11 b8'ld on !hi fflllllrnum lnllll and mthaust reslllc:llon1 plDVlded on page 1. COnlacl fldOl'f for restridlons over the lfllldlled values. Heavy Deratas for higher nistrldlons Ml apply.
� 1. Generator efficiencies, power factor, and vollage are baaed on standmd generator. IGanlllll Power (ekW) 11 r;alcula1ed as: Engk,1 Power (bkW) x Generator Efficiency!, (Gensel Power(kVA) II calculated as: Engine Puwer (bkW) x Generator Elllclency f Power Fedor) 2. Rating Is with lwD engine driven M111r pumps. Tolerance Is (+)3, (-)0% ol lul load. 3. Gllnaet Efllclency pubUshed In ac:curdanca with ISO 31M6/1, based on a 1.0 powerfador. 4. Thermal Effldency Is calculated bllllld an energy recovery frcm the jacltet water, klbe ol� 1st stage llflen:oater, and exhaust to 2<48"1' with engine operation at ISO 3048ft Genslll Efficiency, and assumes unburned fuel II converted In an oxkllllon cataly11t. 5. TOlal elllclency Is calculated as: Gl!llllll Elllcfency + Thennal Efflclency. Tolnnce Is :t:10% of ful load dale. &. ISO 3046'1 Gensel fuel consumption taillranc:e la (+)5, (-)OIi, al the apeciflad power fader. Nominal genut and engine lull consumption tollllllnce Is :t: 3 0% of full load data at Iha IJIIC(llad power lador. 7. Air now vakl• 111 on a 'wel' basil, Flow 11 1 nominal v1kle with II totermice of :t: 5 % 8. Inlet manifold p1111aure la a nominal value with a lote!ance of :t: 5 'Iii. 9. Inlet manifold tempeniture Is I nominal value with a tolerance Df :t: !rF. 10. Timing Indicated Is for use with the minimum fuel methane number apedlled. Cansul Iha appropriate fuel usage guide for liming at Olher methane numben. 11. Elchaust temperature Is I ncmlnal vllkll with a tolerance of (+)63'F, (·)54'F. 12. Exhaull flow VMIII It on a 'Wei' balls. Flow Is a nominal vlklll with a tolerance of :t: 6 %. 13. Inlet and Exhaust Rllltrlctlon1 se maximum IIIIDMd vllkles at the am,spondlnJ! loedll. tna11ulng restrictions bewu,KI what Is specified will result In a lllgnlffcanl engine derate14. Eml111ion1 data Is at engine exhaust flange prior ta any Blier treatment. 15. NOx tolerances are :t: 18% Df apedfled vakle. 16. co, CO2, THC, NMHC, NMNEHC, and HCHO values are "Not to Excaed" levtls. THC, NMHC, and NMNEHC do not Include aldehydn. 17. voes· Volatile 0/IIBIIIC compounds as clllflned In us EPA 40 CFR 60, 1Ubpal1 JJJJ 1B. Exhaust Oxygen tolerance 11 :t: o 5; i....nbd.l tolerance IS :t: 0.05. Llmbdl and Elchaust Oxygen level are Iha resull ol adjusting the engine to operate 111 the specllied NOi level. 19. LHV rate tolerance II :t: 3.0%. 20. Hut rejecllon to jackal water value dlspla)'ed lnc:Wn heat to jacket waler alone. ValJII Is ba5lld on treated water. Tcleranca Is :t: 10% of ful load data 21. Heat rejection ID atmosphere based on llll8lad waler. Tolanlnce II t 50% Df Jul bad data. 22. Lube ol hlllll rata based on trelllld waler. Tolerance Is :t: 20% r:I fuD load data. 23. Exhaust heal rate based on trealecl waler. Tolerance 11 :t: 10% of ful load date. 24. Heat reJecllon to uhaust (LHV ta 77'F} vau11 llha.vn lncklde1 unburned fuel end Is not Intended lo be used for &lzlng or rec:overy calculatlon1 25. Heat rejection to A/C • Slage 1 baSed an treated water. Tolerance Is� of ful load data. 26. Heat rejedlon to NC· Siege 2 based an llllalld water. Tolerance Is t5% of run load data. 27. Pump� lnckldes engine driven Jacket water and lften:ooler waler pumps. Engine brake power Includes affects of pump power. 28. TOlal Jacket Water Circuit heat rejection II calculllled as: (JW x 1.1) + (OC JC 1.2) + (1AC x 1.05) + (0 764 x (1AC + 2AC) x (ACHRF • 1) x 1,05) Heat exchanger 11mg crHerfan 11 maximum crcull heat rejec:llon al aae conditions, 'MIil appll!d talenlnces. A caol1ng system safety lador may be mulllpled by 1h11 total circuit heat rejedlon to provide addltlcnal margin. 29. Total Second Stage Aften:ooter Cmill heat rejecllon la calculated as: (2AC x 1.05) +((!AC+ 2AC) x 0.238 x (ACHRF • 1) x 1.05). Heat exchanger 11zlng crtterfon Is ffl8lllmum c:ln:uH heat rejection al sNe condlllons, wlh applad talelllnces. A cooing systam aafaty factor may be mulllpOed by the total clrcuH heat rejection lo provide atdltl011al margin.
oata generated by Gas Engine RIiiing Pnl Vllrllon 6.01.00 Ref. Data Sat OM5643-03-001. Pr1rlled 29Mar2016 Paga3of 5
Page F-249
Attachment F. Air Quality Permit Application Review Documents
G3516B
ENGINE POWER (bhp): ENGINE SPEED (rpm): EXHAUST MANIFOLD:
1818 1800 DRY
GAS ENGINE TECHNICAL DATA
COOLING SYSTEM:
JACKET WATER OUTLET ("F):
Free Field Mechanical and Exhaust Noise
SOUND PRESSURE LEVEL (dB) I Octave Band Center FnKluenCV COBCFl
100% Load Data dBIAl 63Hz 125Hz 25GHz 500Hz 1kHz 2kHz 4kHz
Mechanical Distance frOm 3.3 109.3 64.7 81.4 87.B 94.9 98.1 95.4 93.9 Sound the Engine (ft) 23.0 92.4 47.8 64.5 70.9 7B 81.2 78.5 77
49.2 85.8 41.2 57.9 64.3 71.4 74.6 71.9 70.4
Exhaust Sound Distance from 4.9 112.1 70.5 105.3 90.6 92.1 91.7 98.5 100.2 lhe Engine (ft) 23.0 98.7 57.1 91.9 77.2 78.7 78.3 85.1 86 8
49.2 92.1 50.5 85.3 70.6 72.1 81.7 78 5 B0.2
SOUND PARAMETER DEFINITION: Dala Variablffty Slatement:
8kHz
105.2
88.3
81.7
99
85.6
79
JW+oc+1AC, 2AC
198
Sound data presented by Caterpillar has been measured in accordance with ISO 6798 In a Grade 3 test environment. MeasuremenlS made In accordance with ISO 6798 will result In some amounl of uncertainty. The uncertainties depend not only on the accuracies wHh which sound pressurelevels and measurement surface areas are detennlned, but also on the 'near-field error' which Increases for smaller measurement distances and lower frequencies. The uncertainty for a Grade 3 test envlrooment, that has a source that produces sounds thel are uniformly distribuled In frequency over the frequency range of Interest, Is equal to 4 dB (A-weighted). This uncertainty Is expressed as the largest value of the standard deviation.
Data g-rated by Gas Engine Rating Pro Version 6.01.00 Ref. Data Set OM564�1. Printed 29Mar2D111 Pag1141lf5
Page F-250
Attachment F. Air Quality Permit Application Review Documents
G3516B GAS ENGINE TECHNICAL DATA
Load Acceptance
30...-------.----------------w----r----.-----.---.. 30
25 -+----'�--..L.-
�20
f1&
]10
5
25
20
15
10
5
a.,.. _________________________________ ...,.. 0
0 10 20 30 40 50 60 70 80 90 100 lnltlal Load(%)
Tn1nslent Load Accentance
Frequency Oevlatlon +/• Volag11 Deviation +/• Recovery C1at1lllcatlon 111 Load Slap Tlmll Dllflned by (%) (%) (lee) 1508528·5
25 +111/-18 +12/-12 20
20 -+91.9 +9/·9 9 Gt
15 +71-7 +6/-8 7 Gt
10 +5/·5 +3/-3 5 Gt
5 +31-3 +1/.1 5 G1
.5 +3/-3 +1/·1 5
-to +51.5 +3/-3 5 ·15 +7/-7 +6/-8 7
-20 +91.9 +9/-9 9 -25 +161-16 +12/-12 20
Bnlaker Qm,n +25/-25 +35/-35 <10 Rea,v-s-•n..auon +1 75/-1.75 +5/·5
Sllladv 511111 s"""""""'°" +1.25/-1.25 +51-5
Ttpnslent lnfonnatlon
i;;:J Max 0G1
Noles
2
2
2
2
1
TI\11 transient load step• lstlld lb0vll are 111a111d as a percentage of 1h11 engln11'1 rua 111111d load a1 lndlcallld In 1h11 appropriate performance tlldlnlcal data lhet. Stt11 ambient cond�lons. fuel quallly. lnlet/llXhaul1 restrldlon and emission• 11111Jngs ¥AU al affect engine response to load change, Engines thGI are not operating at 1h11 standard conditlon1 statlld In 1h11 Technical dlla sheet should be set up ea:ordlng lo 1h11 guide Ines Included In the tedmlRI data: applying timing changes and/or engine denlles as needed. Adherence to the engine 11111tlng1 guldellnes wlU allDw 1h11 engines to retain Iha tn1n1lenl performance stated In 1h11 tabl111 above as a percentage of the Illa deraled power (Wlel'II appruprlale) Fuel supply pressure and stabffHy Is aitlcal lo transient performance. P111par lnstalallan requires Iha! al fuel llllln components (inclldlng flttera, &hut off vat.las, and regulators)
be sized to ensure ad11q11at11 fuel be dalval'lld to Iha engine. The lonowtng are fuel pressure requirements to be meal5Urlld at the angina moun1ad fuel con1r01 vah/11. a Steady State Fuel Pre95Ure Stabllty+/· ,15 psl/aec b Transient fuel Pressure Stablfdy +/· . 15 ptl/aac
Inlet water temperature to the SCAC must be malnlalned at 1pllcllllld vakle far al engines. H Is lmpanant that the external cooffng 1ys1em design Is able to maintain Iha Inlet water temp to the SCAC to within +/· 1 ·c during al anglntt-operatlng cycles. The SCAC lnllll temperature stablllty aitarlon 11 to maintain stable Inlet manltald ar temperature. The Air Fuel Rada contRII ,ys1em requlrel up to 180 IIIICOllds ta conwrve alter a load step has been performed for NOx to return lo namlnal 1111tlng. II lh11 lllabllzallon Ume 11 not met between load stap9 1h11 lranllllnt performance Isled In Iha cloc:urnant may not be met. om-ices In generator lnllltla may change the tramlent response or engine. Engine Governor a-tns and VoJtave
regulator llllllnga IIIIIY 111111d to be tuned for 1tt11 aindltlona. The time needed lo start and stablllza at rated englne •peed Is a minimum ol 60 seax,ds Blier a sua:es&fut aunk cycle. Engines must be maintained In accadance lo guldlllnes speclled In 1h11 Calerplllar Service Manuals appllcablll to each llllglne. Wear of oomponanla oulllde af 1h11 spadllad tolllllnces wtl affect 11111 ltanslant capablily of 1h11 engine. Tran1lent pe,fonnance dala Is re,nsantatlve of a "Hot" (previously loaded or fuly heat IIOBked) ganlllt.
1. For unloading Iha engine to 0% load from a loaded condlllan no lllllemal Input 11 needlld. The engine control algorithm employs a load aenalng stnllegy to dlll!IITllne a load d111p In Iha event that Iha lacal genentar breaker opens 1h11 Slnltegy provides control to 1h11 engine 1h11 resets aB ainlllll lnput1 to Iha ralad 111111 a>ndltlon. This prevents engine over speeding
and wl8 alaw the engine to remain running unbaa'ad 111 the retlld aynchranaua speed. 2. The engines 1padfled abo\111 have bean tested against Ille vollaga deviation, frequency deviation, and -.ry tlma requlrernanll deflnlld In ISO 8528 • 5. At this time 1h11 engines llatad above wlB meat daSI Gt tranlfent perfonnance as defined by ISO 8528 • 5 v.1lh llllteptlonl,
PREPARED BY. Data generat111111y Gal Engine Rating Pro v .. 1on a.01 oo Raf. Data Slit OMSIIG03-001. Pmtad 29Ms2016 Page5af5
Page F-251
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0[ I 100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
STANDBY POWER RATING 100 kW, 125 kVA, 60 Hz
PRIME POWER RATING* 90 kW, 113 kVA, 60 Hz
"Bultt In 1he USA using domesllc and foreign parts
*EPA Certified Prtme ratings are not available in the U.S. or its Territortes.
CODES AND STANDARDS
Generac products are designed to the following standards:
c®� UL2200,UL508,UL142,UL498 m NFPA70,99, 110,37
NFP4
CI::\·
�
�---
NEC700, 701,702,708
IS09001, 8528, 3046, 7637, Pluses #2b, 4
NEMA ICS10, MG1, 250, ICS6, AB1
ANSI C62.41
• osbpd IBC 2009, CBC 2010, IBC 2012, ASCE 7-05,ASCE 7-10, ICC-ES AC-156 (2012)
POWERING AHEAD
GENERAC" I INDUSTRIAL IPOWER
EC].· ..... -11 ...... --........ ·= .
Image used for illustration purposes only
For over 50 years, Generac has led the industry with innovative design and superior manufacturing.
Generac ensures superior quality by designing and manufacturing most of its generator components, including alternators, enclosures and base tanks, control systems and corn rnunications software.
Generac's gen sets utilize a wide variety of options, configurations and arrangements, allowing us to meet the standby power needs of practically every application.
Generac searched globally to ensure the most reliable engines power our generators. We choose only en gin es that have already been proven in heavy-duty industrial application under adverse conditions.
Generac is committed to ensuring our customers' service support continues after their generator purchase .
Page F-252
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0L I 100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
STANDARD FEATURES
ENGINE SYSTEM
General
•Oil Drain Extension
•Air Cleaner
•Fan Guard
•Stainless Steel flexible exhaust connection
•Factory Filled Oil & Coolant
•Radiator Duct Adapter (open set only)
•Critical Exhaust Silencer (enclosed only)
Fuel System
•Flexible fuel line -NPT Connection
•Primary and secondary fuel shutoff
Cooling System
•Closed Coolant Recovery System
•UV/Ozone resistant hoses
•Factory-Installed Radiator
•50/50 Ethylene glycol antifreeze
•Radiator drain extension
CONTROL SYSTEM
Control Panel
•Digital H Control Panel -Dual 4x20 Display
•Programmable Crank Limiter
•7-Day Programmable Exerciser
•Special Applications Programmable PLC
•RS-232/485
•All-Phase Sensing DVR
•Full System Stab.ls
•Utility Monitoring
•Low Fuel Pressure Indication
•2-Wire Start Compatible
•Power Output (kW)
•Power Factor
•kW Hours, Total & Last Run
Engine Electrical System
•Battery charging alternator
•Battery cables
•Battery tray
•Rubber-booted engine electricalconnections
•Solenoid activated starter motor
ALTERNATOR SYSTEM •UL2200 Genprotect ..•Class H insulation material
•2/3 Pitch
•Skewed Stator
•Brushless Excitation
•Sealed Bearings
•Amortisseur winding
•Full load capacity alternator
•ReaVReactive/Apparent Power
•All Phase AC Voltage
•All Phase Currents
•Oil Pressure
•Coolant TemperabJre
•Coolant Level
•Engine Speed
•Battery Voltage
•Frequency
•Date/Time Fault History (Event Log)
•Isochronous Governor Control
•Waterproof/sealed Connectors
•Audible Alarms and Shutdowns
•Not in Auto (Flashing Light)
•Auto/Off/Manual Switch
•E-Stop (Red Mushroom-Type)
•NFPA 110 Level I and II (Programmable)
•Customizable Alarms, Warnings, and Events
•Modbus protocol
•Predictive Maintenance algorithm
•Sealed Boards
•Password parameter adjustment protection
GENERAC" I INDUSTRIAL IPOWER
GENERATOR SET
•Internal Gensel Vibration Isolation
•Separation of circuits -high/low voltage
•Separation of circuits -multiple breakers
•Wrapped Exhaust Piping
•Standard Factory Testing
• 2 Year Limited Warranty (Standby rated Units)
•1 Year Warranty (Prime rated units)
•Silencer mounted in the discharge hood
(enclosed only)
ENCLOSURE (IF SELECTED)
•Rust-proof fasteners with nylon washers toprotect finish
•High performance sound-absorbingmaterial (L1 & L2)
•Gasketed doors
•Stamped air-intake louvers
•Air discharge hoods for radiator-upward
pointing
•Stainless steel lift off door hinges
•Stainless steel lockable handles
•Rhino Coat--Textured polyester powder coat
•Single point ground
•15 channel data logging
•0.2 msec high speed data logging
•Alarm information automatically comes upon the display
Alarms
•Oil Pressure (Pre-programmable LowPressure Shutdown)
•Coolant TemperabJre (Pre-programmedHigh Temp Shutdown)
•Coolant Level (Pre-programmed Low LevelShutdown)
•Low Fuel Pressure Alarm
•Engine Speed (Pre-programmed Overspeed Shutdown)
•Battery Voltage Warning
•Alarms & warnings time and date stamped
•Alarms & warnings for transient and steadystate conditions
•Snap shots of key operation parametersduring alarms & warnings
•Alarms and warnings spelled out (no alarmcodes)
Page F-253
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0L 1100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
CONFIGURABLE OPTIONS
ENGINE SYSTEM
General
o Engine Block Heater
o Oil HeateroAir Filter Restriction
o Stone Guad (Open Set Only)
Engine Electrical System
O 1 DA & 2.5A UL battery c�arger
o Battery Warmer
ALTERNATOR SYSTEM
O Alternator Upsizing o Anti-Condensation HeateroTropical Coating
O Permanent Magnet Excitation
CIRCUIT BREAKER OPTIONS
O Main Line Circuit Breaker
O 2nd Main Line Circuit Breaker
O Shunt Trip and Auxiliary Contact o Electronic Trip Breaker
GENERATOR SET
o Gen-Link Communications Software(English Only)
o Extended Factory Testing (3 Phase Only)
o IBC Seismic Certification
o 8 Position Load Center
o 2 Year Extended Warranty
o 5 Year Warranty
o 5 Year Extended Warranty
ENCLOSURE
o Standard EnclosureoLevel 1 Sound Attenuation
o Level 2 Sound Attenuation
o Steel Enclosure
o Aluminum Enclosure
O 150 MPH Wind Kit
o 12 voe Enclosure Lighting Kit
o 120 VAC Enclosure Lighting Kit
o AC/DC Enclosure Lighting Kit
o Door Alarm Switch
GENERAC" I INDUSTRIAL IPOWER
CONTROL SYSTEM
O NFPA 110 Compliant
o R emote Relay Board (8 or 16)o Oil Temperature Sender with IndicationAlarmoRemote E-Stop (Break Glass-Type,Surface Mount)o Remote E-Stop (Red Mushroom-Type,Surface Mount)o Remote E-Stop (Red Mushroom-Type,Flush Mount)o Remote Communication -BridgeoRemote Communication -Etherneto10A Run RelayoGround Fault Indication and ProtectionFunctions
•ENGINEERED OPTIONS
•
ENGINE SYSTEM
o Coolant heater ball valves
o Fluid containment pans
ALTERNATOR SYSTEM
o 3rd Breaker Systems
CONTROL SYSTEM
O Spare inputs (x4) / outputs (x4) -H Panel Only
o Battery Disconnect Switch
RATING DEFINITIONS
GENERATOR SET
o Special Testing
o Battery Box
ENCLOSURE
O Motorized Dampers
o Intrusion Alert Door Switch
o Ambient Heaters
Standby -Applicable for a varying emergency load for the duration of a utility power outage with no overload capability.
Prime -Applicable for supplying power to a varying load in lieu of utility for an unlimited amount of running time. A 10% overload capacity is available for 1 out of every 12 hours. The Prime Power option is only available on International applications. Power ratings in accordance with ISO 8528-1, Second Edition
Page F-254
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0L I 100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
APPLICATION AND ENGINEERING DATA
ENGINE SPECIFICATIONS
General
Make Generac
Cylinder# 8
Type V
Displacement -L (cu In) 8.9L (540)
Bore -mm (in) 114.23 (4.49)
Stroke -mm (in) 107.15 (4.25)
Compression Ratio 10.5:1
Intake Air Method Naturally Aspirated
Number of Main Bearings 5
Connecting Rods Forged
Cylinder Head Cast Iron
Cylinder Liners No
Ignition High Energy
Piston Type Aluminum Alloy
Crankshaft Type Forged Steel
Lifter Type Hydraulic Roller
Intake Valve Material Steel Alloy
Exhaust Valve Material Stainless Steel
Hardened Valve Seats Yes
•Engine Governing
Governor Electronic
Frequency Regulation (Steady State) ±0.25%
Lubrication System
Oil Pump Type Gear
Oil Filter Type Full-flow sping-on cartridge
Crankcase Capacity - L (qts) 8.5 (8.0)
ALTERNATOR SPECIFICATIONS
Standard Model 390mm
Poles 4
Field Type Revolving
Insulation Class -Rotor H
Insulation Class -Stator H
Total Harmonic Distortion <5%
Telephone Interference Factor (TIF) <50
•
BENERAC" I INDUSTRIAL IPOWER
Cooling System
Cooling System Type
Water Pump Row -gaVmin (Vmin)
Fan Type
Fan Speed (rpm)
Fan Diameter mm (in)
Coolant Heater Wattage
Coolant Heater Standard Voltage
Fuel System
Fuel Type
Carburetor
Secondary Fuel Regulator
Fuel Shut Off Regulator
Operating Fuel Pressure (Standard)
Operating Fuel Pressure (Optional)
Engine Electrical System
System Voltage
Battery Charging Alternator
Battery Size
Battery Voltage
Ground Polarity
Standard Excitation
Bearings
Coupling
Prototype Short Circuit Test
Voltage Regulator Type
Number of Sensed Phases
Regulation Accuracy (Steady State)
Pressurized Closed
26 (98)
Pusher
2330
558 (22)
1500
120V
Natural Gas, Propane Vapor
Down Draft
Standard
Standard
11" -14" H20
12VDC
Standard
See Battery Index
0161970SBY
12VDC
Negative
Brushless
Sealed Ball
Direct Drive
Yes
Full Digital
All
±0.25%
Page F-255
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0L I 100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
GENERAC" I INDUSTRIAL IPOWER
OPERATING DATA
POWER RATINGS
Single-Phase 120/240 VAC @1.0pf
Three-Phase 120/208 VAC @0.8pf
Three-Phase 120/240 VAC @0.8pf
Three-Phase 277/480 VAC @0.8pf
Three-Phase 347/600 VAC @0.8pf
STARTING CAPABILITIES (sKVA)
Alternator kW
Standard 100
Upsize 1 130
10%
79
116
FUEL CONSUMPTION RATES*
15%
118
174
480VAC
20% 25%
157 197
232 290
30%
236
348
Natural Gas Propane Vapor
100 kW Amps: 417 Amps: 417
100 kW Amps: 347 Amps: 347
100 kW Amps: 301 Amps: 301
100 kW Amps: 150 Amps: 150
100 kW Amps: 120 Amps: 120
sKVA vs. Voltage Dip
208/240 VAC
35% 10% 15% 20% 25% 30 % 35%
275 59 89 118 148 177 206
406 87 131 174 218 261 305
Natural Gas -ft 3/hr (m 3/hr)Propane Vapor -ft 3/hr (m 3/hr)
Percent Load Standby Percent Load Standby
25% 391 (11.1) 25% 157.4 (4.5)
50% 669 (19.0) 50% 269.9 (7.6)
75% 904 (25.6) 75% 364.4 (10.3)
100% 1116 (31.6) 100% 449.8 (12.7)
* Fuel supply installation must accommodate fuel consumption rates at 100% load.
COOLING
Air Flow (inlet air combustion and radiator) 113/min(m 3/min)
Coolant Flow per Minute gaVmin (Vmin)
Coolant System Capacity gal (I)
Heat Rejection to Coolant BTU/hr
Max. Operating Ambient Temperature (before derate) OF (OC)
Maximum Radiator Backpressure in f1i0
COMBUSTION AIR REQUIREMENT
Standby
Flow at Rated Power elm (m3/min) 282 (7.9)
ENGINE
Standby
Rated Engine Speed rpm 1800
Horsepower at Rated kW** hp 149
Piston Speed fVmin 1275
BMEP psi 125
** Refer to "Emissions Data Sheet" for maximum bHP for
EPA and SCAOMD permitting purposes.
EXHAUST
Exhaust Flow (Rated Output)
Max. Backpressure (Post Turbo)
Exhaust Temp (Rated Output -post silencer)
Exhaust Outlet Size (Open Set)
Standby
5797 (164.2)
26 (98)
6.0 (22.7)
390,000
122 (50)
0.5
elm (m 3/min)
inHg (Kpa)
OF (OC)
mm(in)
Deration -Operational characteristics consider maximum ambient conditions. Derate factors may apply under atypical site conditions.
Standby
866 (24.5)
1.5 (5.1)
1230 (666)
63.5 (2.5)
Please consult a Generac Power Systems Industrial Dealer for additional details. All pertormance ratings in accordance with IS03046, BS5514, IS08528
and DIN6271 standards.
Page F-256
Attachment F. Air Quality Permit Application Review Documents
S6100 I 9.0L I 100 kW
INDUSTRIAL SPARK-IGNITED GENERATOR SET
EPA Certified Stationary Emergency
DIMENSIONS AND WEIGHTS*
-----L-------'
L
IB
: i;--: · . .-c· ·u f&l · • '
;--------L -----
------L------
u
:·o'-61 .••..
a
.,,. . ·, �:-! _.. I
w
.. J --w-1
I.
H
t.I I 1----w---
GENERAC" I INDUSTRIAL IPOWER
OPEN SET (Includes Exhaust Flex)
LxW x Hin (mm) 94,2 (2394) X 40 (1016) X 47.5 (1206)
Weight lbs (kg) 2064 (936.2)
STANDARD ENCLOSURE
L x W x H in (mm) 111.79 (2839.5) x 40.46 (1027.8) x 56.18 (1427)
Weight lbs (kg) Steel: 2708 (1228) Aluminum: 2413 (1094)
LEVEL 1 ACOUSTIC ENCLOSURE
L x W x Hin (mm) 129 42 (3287.2) x 40.46 (1027.8) x 56.18 (1427)
Weight lbs (kg) Steel: 2798 (1269.2) Aluminum: 2355 (1068)
LEVEL 2 ACOUSTIC ENCLOSURE
L x W x H in (mm) 111.81 (2840) x 40.46 (1027.8) x 68.61 (17 42.8)
Weight lbs (kg) Steel: 3022 (1370.8) Aluminum: 2431 (1103)
* All measurements are approximate and for estimation purposes only.
YOUR FACTORY RECOGNIZED GENERAC INDUSTRIAL DEALER
Specification characteristics may change without notice Please consult a Generac Power Systems Industrial Dealer for detailed Installation drawings
Generac Power Systems, Inc. I P.O. Box 8 I Waukesha, WI 53187 P: [phone] © 2015 Generac Power Systems, Inc. All rights reserved. All specmcations are subject to change without notice. Part No 0K4291 Rev. D 07 /27/15
Page F-257
Attachment F. Air Quality Permit Application Review Documents
STATEMENT OF EXHAUST EMISSIONS
2015 SPARK-IGNITED, SCAQMD CERTIFIED
w
w
� l I
'i Ji
w � � ;r �
Model
QTA.25
QTA25
S0035
S0035
S0040
S0040
SG045
SG045
S0050
S0050
S0050
S0050
SGOSO
SGOSO
SG070
SG070
SGOBO
S0080
SGOSO
SGOBO
SG130(DF)
S0150 (OF)
50100
SG100(l.PF)
80100 (OF)
SG100(DF)
S0100
S0100
S0130,150
S0130, 150 (OF)
S0130, 150 (DF)
S0130, 150
SG130, 150
SG150
MG150
SG175
SG200
MG200
S0230
SG250
MG250
S0275
SG300
MGJOO
SG150, 175,200
SG230, 250
SG275, 300
MG150. 200
MG250
MG300
SG350, 400
MG350,400
S0350,400 (LPF
MG350,400 (LPF)
NR! Not Roqulntd
OF: Dual FUtll
EPA Engine Engine Family
24 FGNXBO:Z 42NN
2.4 FGN>ca02.42NL
54 FGN>la05.42L1
5.4 FGN>a:105 42L2
54 FGNXB05.42L 1
54 FGN)805.4212
5.4 FGN>CB05.42L 1
54 FGN)t805,4212
5,4 FGN>IB05,42L 1
54 FGNXB05 42L2
88 FGN)(BOB 82Ui
8.8 FGN>CSOB 82U!I
88 FGNXBOO 82Ui
88 FGN>IBOS 82UI
88 FGN)l808S2L3
88 FGN>808 82L4
80 FGN>1808 021. 1
oo FGN)l808 D2L2
o.o FGN>l80e 92L1
90 FGN>SOB 82L2
8.8 FGN>IS08,82C3
8,8 FGN>l8De.82C3
OD FGN>CS08 82C1
90 FGN>IB08 92C1
o.o FGN>IB08 92C1
9.0 FGN)C808 92C1
9.0 FGWe0882C2
DO FGN>G!oe92C2
DO FGN)CBOB 92C3
90 FGN>l808 02CJ
90 FGN)'SOB 82C3
9.0 FGN>l808.U2C4
90 FGN>l808.92C4
12 9 FGN)l812.92C2
12 D FGN)812.112C2
12 9 FGN>C812.92C2
12 9 FGN>l812.92C2
12 D FGN)(S12.92C2
12 D FGN>IS12 92C2
12 9 FGN)CB 12 82C2
12.9 FGN)CB12 92C2
12.9 FGN>l812,92C3
120 FGN.)C812 92CJ
12.9 FGNJl812 92CJ
14 2L FGN,G314 22C1
14 2L FGN>G314.22C1
14,2L FGN>IB14 22C1
14 2L FGN>IB 14 22C1
142L FGNXB14,22C1
14,2L FGNXB14,22C1
21 9 FGN>CB21 92C1
21 D FGN>821 82C1
21 D FGN>CB21 92C1
21 9 FGNm21 92C1
LPF· Unite with optional Low Pressuro Fuel syatom
Refar to pogo 2 fer datlnltlons and ed\llsory notes
CAT SCAQMD EPA Fuel Req'd CEP# Cert#
NG No NR FGN>802 42NN-005
LPG No NR FGN>e.02 42NL.�
NG Vea 530212 F�5.42L1-019
LPG Vos 530215 FGN)IS05.42l..2-020
NG Vos 530212 FGN>8 05.42L 1-019
LPG Vos 530215 FGNXB05.42l.2.Q20
NG Vos 530212 FGNXB05.42L1-019
LPG Vos 530215 FGNXB05.42l.2-020
NG Vos 530212 FGN)805.421..1-019
LPG Vos 530215 FGN)805.421..2-020
NG Voe 470347 FGNlCBDe.B2l.5-025
LPG Voe 470347 FGNll80e.82L.8-028
NG Voa 408721 FGN>l806 a2L5-025
LPG Vos 488721 FGNXB06 821..8-026
NG Vea 470208 FGN>SQ8_82L.3,-023
LPG Vos 470208 FGN>G:108 82L4-024
NG Vos 575822 FGN>m08,02L 1-027
LPG VH 575823 FGN>CB08 02L2-028
NG VH 543428 FGN>CBOB 92L 1�29
LPG Vos 543429 FGN:)808 921...2�30
NG&LP Vos 480473 FGNll808 82C3-033
NG&LP Vos 4800159 FGN)l806 82C3-033
NG Vos 543423 FGN>e08 til2C1--035
NG v .. 573274 FGl"OSOS Cl2C1-035
NGILPV Vos 543425 FGN>808 Cl2C1..Q:35
NG/LPL Voe 543424 FGN>IB 08 82C1--035
LPV v .. 543428 FGN>IBOS Cl2C2--038
LPL Vea 543427 FGN>l8 08 D2C2.Q38
NG Vos 573270 FGN>S08.92C3-053
NG/LPV VH 573273 FGN>S08 92C3-053
NG/LPL Ves 573271 FGN>l808 92C3-053
LPV Vos 573287 FGN>IB08 92C4--054
LPL Vos 573280 FGN)l808 9204-054
NG Vos 532838 FGNle12 92C2-042
NG v .. 532839 FGN>812 92C2-042
NG Vos 532831! FGNli812.82C2-042
NG Vos 532838 FGNli812 92C2-042
NG Vos 532839 FGN>IB12 92C2-042
NG Vea 538818 FGN>l812.02C2-042
NG Vea 538818 FGN)l812 92C2-042
NG Voa 538818 FGN>e12,92C2-042
NG Voa 557131 FGN>IB 12 9203-043
NG Voe 557131 FGN>IS 12.9203-043
NG Vea 557132 FGN)812..92C3-043
NG Vos 575824 FGNle14 22C1-047
NG Vos 575828 FGNle14 22C1-047
NG Yes 575828 FGN>814 22C1-047
NG Vos 575825 FGN>814 22C1-047
NG Vea 575827 FGN>814 22C1-047
NG Vea 575829 FGN>CB14 22C1-047
NG Yoe 5584n FGN>e21 92CH'.J37
NG Vos 558478 FCN>IB21 92C1-037
NG Vas 573288 FGN>821.92C1--037
NG Vea 573285 FGN>C821.92C1-037
GENERAc· 11NcusTR1AL I POWER
Grams/bhp•hr. Rated Fuel Flow RPM BHP (lb/hr) THC NOx co
2 14 2 37 93 95 1800 38 39 10 !52
1.43 4.31! 88.18 1800 43.29 17.Si
038 022 0.&4 1800 81115 24 91
0 04 0,10 070 1800 81 70 29 13
0 38 022 0.84 1800 81 95 24 g1
0.04 0.10 0,70 1800 81 70 29.13
0.31! 0.22 0,84 1800 81.85 24.91
0 04 0.10 0,70 1800 81.70 29 13
031! 022 0 84 1800 81 95 24 91
0 04 0.10 0.70 1800 81.70 29 13
021 002 0 10 1800 .... 33 10
001 0.00 0 50 1800 ..... 34,14
0 22 0.02 0 30 1800 .. 58 37 58
001 0.01 0 78 1800 EKl,15 31! oo
0.20 0.04 0.49 1800 110.&4 41.00
008 0.07 0 01 1000 112.42 42.35
0 42 0,51 D,07 1800 12569 39.71!1
0 04 013 0 30 1800 127 89 44,69
0 38 0,78 0 41 1800 128 31 39,71
0 06 0.88 030 1800 126.40 44,34
0 08 0 05 0 92 3000 193.49 72.31
0 18 0,14 1 54 3800 231 00 01 34
017 0003 008 11900 14800 4088
008 0 240 0 01 1800 158.00 4'3.83
030 0 400 0 79 1800 133 18 45.38
0.34 0 000 110 1800 135.75 45 47
003 0.08 0 13 1800 157 87 53.08
0 07 0 04 0.30 11100 158 15 54.•7
0.10 003 0,02 1800 23030 71 lil7
010 0.03 0.02 1800 23030 71,97
0.10 003 0 02 1800 23030 71 97
0,02 0 57 130 1000 230,30 75.43
0,02 0.57 1.30 1800 230,30 75.43
0 53 0 13 0 53 1800 307.87 107 99
0,53 0 13 0 53 1000 307 87 107 9Q
0.53 013 0.53 1800 307.87 107 99
0.53 0 13 0 53 1800 307 87 107,99
0 53 0 13 0.53 1800 307.87 107 99
0,31! 003 0 53 1800 379.10 125 30
031! 0 03 0 53 1800 379 10 125 30
0.38 0 03 0.53 1800 379.10 125 30
008 000 0,81 2150 4n.oo 164 2D
008 008 0 01 2150 4n.oo 164.20
0.08 0 00 0.81 2150 4noo 184 20
0 06 0 05 0,39 1800 304 00 0854
0.08 0.00 0.39 1800 304 00 0854
0 04 0 02 023 1800 374 00 120 84
0 04 0 02 0,23 1800 374 00 120,84
0.03 0 03 0.17 1800 480 00 142 87
0 03 003 0,17 1800 480 00 142 87
0.18 0 14 0.82 1800 838 00 201 17
018 0,14 0 82 1800 83800 201 17
0.18 0 14 0.82 1800 831! 00 201 17
0 18 0 14 0 02 1800 838 00 201 17
Page F-258
Attachment F. Air Quality Permit Application Review Documents
GENERAC" I INDUSTRIAL IPOWER
STATEMENT OF EXHAUST EMISSIONS
2015 SPARK-IGNITED, SCAQMD CERTIFIED
2015 EPA SPARK-IGNITED EXHAUST EMISSIONS DATA
Effective since 2009, the EPA has implemented exhaust emissions regulations on stationary spark-ignited (gaseous) engine generators for emergency applications.
All Generac spark-ignited gensets, including SG, MG, QTA and QT series gensets, that are built with engines manufactured in 2009 and later meet the requirements
of 40CFR part 60 subpart JJJJ and are EPA certified. These generator sets are labeled as EPA Certified with decals affixed to the engines'valve covers.
The attached documents summarize the general information relevant to EPA certification on these generator sets. This information can be used for submittal data and 101 permitting
purposes, if required. These documents include the following information:
EPA Engine Family
The EPA Engine Family is assigned by the Manufacturer under EPA guidelines for certification purposes and appears on the EPA certificate.
Catalyst Required
Indicates whether an exhaust catalyst and Air/Fuel Ratio control system are required on the generator set to meet EPA certification requirements.
Generally, units rated 80kW and smaller do not require a catalyst to meet EPA certification requirements. Please note that some units that do not
require a catalyst to meet EPA requirements do need a catalyst if the California SCAQMD option Is selected. Please see
'California SCAQMD' below for additional inf01mation on this option.
Combination Catalyst or Separate Catalyst
SG and MG series generator sets typically utilize a single combination catalyst/silencer as part of meeting EPA certification requirements. Many QT
and QTA series generator sets use the same engines as SG and MG series units, but have different exhaust configurations that require the use of
conventional silencers with additional separate catalysts installed.
EPA Certificate Number
Upon certification by the EPA, a Certificate Number is assigned by the EPA.
Emissions Actuals -Grams/bhp-hr
Actual exhaust emission data for Total Hydrocarbons (THC), Nitrogen Oxides (NOx) and Carbon Monoxide (CO) that were submitted to EPA and
are official data of record for certification. This data can be used for penmitting if necessary. Values are expressed In grams per brake horsepowerhour;
to convert to grams/kW-hr, multiply by 1.341. Please see advisory notes below for further Information.
California Units, SCAQMD CEP Number
A separate low-emissions option is available on many Generac gaseous-fueled generator sets to comply with the more stringent South Coast Air Quality
Management District requirements that are recognized in certain areas in California Gensets that include this option are also EPA Certified.
General Advisory Note to Dealers
The information provided here is proprietary to Generac and its' authorized dealers. This information may only be disseminated upon reques� to regulatory governmental bodies for
emissions permitting purposes 01 to specifying organizations as submittal data when expressly required by project specifications, and shall remain confidential and not open to public
viewing. This information is not intended for compilation or sales purposes and may not be used as such, nor may it be reproduced without the expressed written permission of
Generac Power Systems, Inc.
Advisory Notes on Emissions Actuals
• The stated values are actual exhaust emission test measurements obtained from units representative of the generator types and engines described.
• Values are official data of record as submitted to the EPA and SCAQMD for certification purposes. Testing was conducted in accordance with prevailing EPA
protocols, which are typically accepted by SCAQMD and other regional authorities.
• No emission values provided are to be construed as guarantees of emissions levels for any given Generac generator unit
• Generac Power Systems reserves the right to revise this information without prior notice.
• Consult state and local regulatory agencies for specific permitting requirements.
• The emissions performance data supplied by the equipment manufacturer is only one element required toward completion of the permitting and installation
process. State and local regulations may vary on a case-by-case basis and must be consulted by the permit applicant/equipment owner prior to equipment
purchase or Installation. The data supplied herein by Generac Power Systems cannot be construed as a guarantee of installability of the generator set
• The emission values provided are the result of molt�mode, weighted scale testing in accordance with EPA testing regulations, and may not be representative of
any specific load point
• The emission values provided are not to be construed as emission limits.
GeneracPowerSystems,lnc, I P.O.BoxS I Waukesha,Wl53187
P: [phone] e 2015 Generac Power Systems, Inc. All rights reserved. All specifications are subject to change without notice.
Bulletin 0L2042 Rev. B 07 n2115
Page F-259
Attachment F. Air Quality Permit Application Review Documents
THREE PASS FIRETUBE
HOT WATER BOILER ... �,,.���� .. �-.:.;:;.a ��,1�-------------------
LPWSERIES
THROUGH THE DOOR DESIGN!
1 HURST "PERFORMANCE" BOILERS I
Hot Water Applications
• Specifiable using the attributes of the LPW
design.
•Remains classified as a modified scotch, fire
tube type boiler.
•Efficiencies tested in our lab at >83% on nat­
ural gas.•Smaller foot print. As compared to the LPE,
can be installed in tighter places.
•Semi wet-back construction
.. Capacities From
30 to 125 HP
30 PSI Water
[60 PSI Water Optional]
UL Approved Forced Draft Burners HEAVIEST DESIGNED BOILER IN ITS CLASS
Designed, constructed and stamped
•
in accordance with the requirements €,.. s of the ASME Boiler Codes. '"' • Inspected and registered with
the National Board of Boiler &
Pressure Vessel Inspectors.
Page F-260
Attachment F. Air Quality Permit Application Review Documents
C
(APP!m W\ GAS TIIAIN)
E F
A
FRONTVIEW
BOILER SPECIFICATIONS
G
p
R D ---J (ltJBE REMOVAL) L __ J
1-
I
I
1 I 4
.. J. . •
Q
-- e ---------... --I'-====="td"_ !H IM
E
RIGHT SIDE VIEW
0
(ALL DIMENSIONS ARE IN INCHES) DIMENSIONS SUBJECT TO CHANGE WITHOUT NOTICE. CERTIFIED DRAWINGS AVAILABLE UPON
HEATING SURFACE FIRESIDE SO.FT. 120 160 200 240 280 320 400 500
MBH OUTPUT, HOT WATER 1004 1339 1674 2009 2343 2678 3348 4184
FIRING RATE, GAS 1,000 BTU CFH 1260 1680 21 00 2520 2940 3360 4200 5250
FIRING RATE, #2 OIL 140,000BTU GPH 9 12 15 18 21 24 30 37 1/2
WIDTH WITHOUT TRIM IN 31 31 31 341/2 341/2 3472 341/2 34 1/2
WIDTH WITH TRIM IN 38 38 38 42 42 42 42 42
WIDTH WITH GAS TRAIN IN 49 49 49 52 52 52 52 52
• BOILER LENGTH IN 37 49 61 55 67 79 91 106
OVERALL LENGTH STD. BURNER IN 86 98 114 111 123 140 152 169
SUPPLY HEIGHT IN 71 1/2 711/2 711/2 76 5/8 76 5/8 76 5/8 76 5/8 765/8
HEIGHT WITH TRIM IN 79 79 79 86 86 86 86 86
LENGTH OF SKID IN 54 66 7B 72 84 96 108 123
SUPPLY SIZE IN 4 4 4 6 6 6 6 6
SUPPLY LOCATION IN 1B 1/2 241/2 301/2 271/2 331/2 391/2 45 1/2 50 1/2
RETURN SIZE IN 4 4 4 4 4 4 4 4
RETURN LOCATION IN 27 1/4 271/4 27 1/4 32 32 32 32 36
BOILER DRAIN SIZE IN 1 1/4 11/4 1 1/4 1 1/2 11/2 1 1/2 11/2
STACK DIAMETER, O.D. IN 10 10 10 12 12 12 12 14
• STACK HEIGHT IN 601/4 60 1/4 601/4 671/4 671/4 ffT 1/4 67 1/4 671/4 •
• TO CENTER OF STACK IN 6 7/8 67/8 6 7/8 81/4 81/4 B 1/4 B 1/4 91/4
REAR SMOKEBOX DEPTH IN 13 3/4 13 3/4 13 3/4 15 3/4 15 3/4 15 3/4 15 3/4 17 3/4 •
TUBE PULL SPACE IN 38 50 62 56 68 BO 92 107
SHIPPING WEIGHT LBS 3150 3900 4500 4350 5100 6600
CONNECTIONS FOUR INCHES ANO SMALLER ARE FEMALE THREAD, 6" CONNECTIONS ARE 150 LB. FLANGES. • STUDDING Fl.ANGE.
Page F-261
Attachment F. Air Quality Permit Application Review Documents
I \
0
T urbolators in
3rd tube pass.
Bolt-On front
& rear smokeboxes
for easy tube
maintenance.
UL listed burner.
Compact design
Skid mounted for
easy installation.
THREE PASS FIRETUBE
Fully piped & control trimmed.
HOT WATER BOILER
5/16" boiler vessel.
Twin independent
tube sheets.
2" high density
ceram ic insullation.
2" water wall under furnace.
Turbulators inserted in 3rd pass
STANDARD EQUIPMENT
BOILER: Three pass design for 30 psi hot water (available for 60 psi water). Factory
assembled with trim and, tested in accorance with ASME code, UL, and CSD-1 codes.
Steel turbolators inserted in third pass for maximum heat-transfer control.
STANDARD BOILER TRIM: Kunkle safety relief valve, operating temperature control,
high limit temperature control with manual reset, 3 1/2" combination pressure & tempera­
ture gauge, M&M 750 low water cut-off control with manual reset.
BURNER: UL listed with pre-piped, wired and factory tested forced draft power burners
for:
I Natural Gas
I Propane (LP) Gas
I No. 2 (Diesel} Oil
I Combination Gas/Oil.
Page F-262
Attachment F. Air Quality Permit Application Review Documents
LPW SERIES THREE PASS FIRETUBE
COMPACT BOILERS
I HURST "PERFORMANCE" BOILER I
•Factory Assembled, Prewired and Tested
•No Field Assembly Required
•UL Listed Boiler/Burner Packages
•Fully Assembled, Pre-piped, Prewired, Pressure Te sted Gas Trains
•Complies with ASME, UL, CSD-1 and ASHRAE Standards
•High Efficiency, Low Stack Temperatures
•Customer Service Support Through National Network of Sales, Service, St
Training and Parts by Factory Representatives
LPW BOILER FEATURES
Modified Scotch designed to fit through a standard 36" x 80" door opening
Up to 125 HP (4,184 mbh output).
The Hurst LPW "Performance" boiler is America's most heavily designed and
built boiler in its class. Consider the features and specify the Hurst LPW Series.
1.A welded steel firetube boiler, the LPW has extra-heavy 13-gauge tubes for extended life.
All tubes are attached to the tube sheets by rolling and flaring. There are no welded tubes
in the LPW.
2.Thickest materials used in the industry ...
A.Boiler shell is 5/16" thick boiler plate 30-40 HP / 3/8" 50-125 HP.
B.Twin boiler tube sheets are 1/2" thick boiler plate.
C.Insulation is 2" ceramic wool and is lagged with 22-gauge boiler jacket.
D.Extra heavy 4" channel iron boiler skids.
3.Designed to last with special industrial grade features ...
A.Couplings are 3,000 psi.
B.Flanged, detachable front and rear smoke boxes.
C.Brass nuts on front access panels, brass plugs in factory pre-piped crosses and
tees on trim.
hurstboiler.com
P.0. Drawer 530
21971 Highway 319 N.
Coolidge, Georgia 31738
[phone] (Tel.)
[phone] (Fax.)
e-mail: [e-mail]
Revised 06/05
Page F-263
Attachment F. Air Quality Permit Application Review Documents
i'
Dominion Resources Services, Inc.
5000 Dominion Boulevard, Glen Allen, VA 23060
Web Address: www.dom.com
September 16, 2015
BY: OVERNIGHT MAil,
Patrick Butler
Regional Supervisor
b, .. J 1 7 'lfi • t.U,J
NCO a,e,gh Regional Office
• r •• � -. • ·�•"" ! -

,

.
.

-
�

' .� • r • \ ' 1 ' ' ! '.ji.
)
Raleigh Regional Office
NCDENR Division of Air Quality
Suite 101
3800 Barrett Drive
Raleigh, NC 27609
NC DENR Raleigh Ragional O'.fice
RE: Northampton Compressor Station
New Source Pennit
Dear Mr. Butler:
Atlantic Coast Pipeline, LLC proposes to construct and operate the Atlantic Coast Pipeline, an
approximately 556-mile-long interstate natural gas transmission pipeline system designed to meet growing
energy needs in Virginia and North Carolina. Enclosed is an application for a new natural gas compressor station to be located in Northampton County, North Carolina. The Northampton Compressor Station will include the following equipment:
•Solar Taurus 70 combustion turbine;•Solar Centaur SOL combustion turbine;•Solar Centaur 40 combustion turbine;•Caterpillar G3516 emergency generator;•Boiler rated at 6.3 MMBtu/hr;•Accumulator tank with a capacity of 2,500 gallons;•Hydrocarbon waste tank with a capacity of 1,500 gallons;•Aqueous ammonia storage tank with a capacity of 8,000 gallons;
SHADED AREA MUST GRADUALLY CHANGE FROM BLUE AT TOP TO GREEN AT BOTTOM
Atlantic Coast Pipeline
C/0 D011inion
P.O. BOX 25459
Richmond, VA 23260-5459
Pay Exactly **Fifty and 00/100 -US Dollars **
TOTHE NORTH AROLINA STATE OF
Atlantic Coast Pipeline ..
QBDER -...-=&MENT & NATURAL RESOURCES
oF DEPT OF RALEIGH REGIONAL OFFICE
WELLS FARGO BANK, N.A.
-------
11 1 0000000 • 2 •11• 1:0 5 3 •0 • 5 i; .,:ao •80 • 5 �8 Su•
66-156/531
Date:
Check#:
Vendor#:
Document#:
09/09/2015 000121 300159136 2000001303ACP1
Amount
$******50.00
VOID AFTER 90 DAYS
Page F-264
Attachment F. Air Quality Permit Application Review Documents
MAILED
North Carolina Department of Environmental Quality �"$
Pat McCrory
Governor
CERTIFIED MAIL
Donald R. van der Vaart
Secretary
( RETURN RECEIPT REQUESTED
[ September 22, 2015
U.S: Postal Service n.,CERTIFIED MAIL M RECEIPT(Domestic Mail Only; No Insurance Coverage Provi
Ms. Leslie Hartz
For dellvery Information visit our Webslite at www.us ps.co • I"-
VP Pipeline Construction
Northampton Compressor Station
707 E. Main Street
� --._cc_-=---=-,=�="��������
Richmond, VA 23219
co
Cl Cl
Postage $
Certified Fee
Cl Retum Receipt Fee
Cl (Endorsement Required)
RestrlctAr1 nAINArv l=AA t------_J
Postmark
Here
SUBJECT:
Cl (Endors MS LESL Cl · IE HARTZ, VP PIPELINE CONSTRUCTION Receipt of Permit Application ru 11 teJJ NORTHAMPTONCOMPREssoR STATION ...-'I O 707 E. MAIN ST. Greenfield Facility ;:,-ent O RICHMOND, VA 23219
Application No. 6600169.lSA ...-'I • •••••• DAQ-REC PERAPP-6600169-NHAMP-CM.o "siriiet,, REC: 7014-1200-0000-8627 4972 M 91 Northampton Compressor Station I'-o,PoE -28/15
Facility ID: 6600169, Pleasant Hill, Northampto1 citji"siare,.£,n4
Dear Ms. Hartz:
PS Form 3800, August 2006
Your air permit application (6600169.lSA) for Northampton Compressor Station, located in
Northampton County, North Carolina received by this Division on September 17, 2015 has been
deemed to be incomplete. Your air permit application request must include the following items:
Local zoning and subdivision ordinances consis tency determination:
See Reverse for Inst
Your application did not contain the complete request for consistency determination. Your
application must include a copy of your written request for a "determination of consistency" with
local government ordinances bearing the date of receipt entered by the clerk of each local
government having jurisdiction. The following is a detailed explanation of the determination of
consistency requirements, and includes a description of documentation that must be submitted with
your application.
a.The permit applicant shall submit a signed statement listing any and all loc al governments
having jurisdiction over any part of the land on which the facility and its appurtenances are
to be located.
Raleigh Regional Office -Division of Air Quality 3800 Barrett Drive, Raleigh, North Carolina 27609 Phone: [phone] / FAX: [phone] Internet: www.ncdenr.gov
An Equal Opportunity I Affirmative Aclion Employer -Made in part by recycled paper
Page F-265
Attachment F. Air Quality Permit Application Review Documents
? •Ms. Hartz ,1,..;.. September'n;-2015Page2
b.The applicant is reqevery local govemrr • Complete items 1, 2, and 3. Also complete
Item 4 If Restricted Delivery Is desired.
•Print your name and address on the reversec.The zoning consistei that we can return the card to you.
• ��ach this card to the back ?f the mallplece, shall include a copy or on the front If space permits. ���;:=�--,
( 1. Article Addressed to: d.The zoning consister
/ personally or by cert MS. LESLIE HARTZ, VP PIPELINE CONSTRUCTION \ 1 NORTHAMPTON COMPRESSOR STATION letter from the facilit 101 E. MAIN ST.. •' RICHMOND, VA 23219the official des1gnate1 DAQ-REC PER APP-6600169-NHAMP-CM received transmittal 1, REC: 7014-1200-0000-8627-4972 M 9/28/15
COMPLETE THIS SECTION ON DELIVERY
D Agent X D Addressee
B.
D.Is delivery address different from lte
If YES, enter delivery address below:
3.Service Type o Certified Mall D Express Mall o Registered D Return Receipt for MerchandiseDivision. D Insured Mall O c.o.o. ff / 18 4. Restricted Delivery? (Extra Fee)D Yese.The required zoning c-���;��;;;;;;;;;;.::-:1-:�����;��:�:�;:;-�;�o�a�a�a�j8�bj2�7��4�9�7�2�::::������; • 2 Arttcle Number must be Slgned by the . (rransferfromserv/ce/abeQ 102595-02.M-,540 d · · If th Domestic Return Receipt eterrrunatlon. e I PS Form 3811. February 2004 • -----�A�Wm VY Hll <1 �onmg or subdivision ordinarfoe, a copy of such a determination shall be submitted to the applicant.PE Seal Requirement: The technical portion(s) of your applic.ation was not sealed by a North Carolina registered professional engineer (PE) as required by 15A NCAC 2Q.Ol 12. You are required to re-submit the technical portion(s) of your application bearing the seal of a North Carolina PE. Additional Requirements: The Form Al does not include the site address (911 Address) or zip code. Please include them inyour response. In summary, this application did not contain all the required elements as indicated above and has not been accepted for processing. This information must be submitted and contain the above requested information. The requested information must be submitted to our Office within thirty (30)days or the application may be terminated.
Should you have any questions concerning this matter, please contact Charles McEachern at919-791-4200.
cc: Raleigh Regional Office Files
Sincerely,
,:��B�d� -r-� Division of Air Quality, NCDENR
Page F-266
Attachment F. Air Quality Permit Application Review Documents
,,
North Carolina Department of Environmental Quality
Pat McCrory
Governor
Kimberly Bose, Secretary
Donald R. van der Vaart
Secretary
October 8, 2015
Federal Energy Regulatory Commission (FERC)
888 First Street, NE
Washington, D.C. 20426 .
Docket#: CP15-554-000
SUBJECT: Preliminary Assessment of Air Permit Application
Atlantic Coast Pipeline, LLC-Northampton Compressor Station
Pleasant Hill, NC, Northampton County, Facility ID No. 6600169
Project Docket#: CP15-554-000
Dear Kimberly Bose:
This letter is written in response to an air permit application received from the Subject facility on September 17, 2015 and the consequent State responsibilities under 18 CPR 385.2013 -Notification of
requests for Federal authorizations and requests for further information (Rule 2013). The applicant has
applied for an air permit for a natural gas compressor station which will be subject to Federal rules (NSPS
Subparts JJJJ and KKKK, and NESHAP Subpart ZZZZ) for which the State of North Carolina has delegated
authority. Pursuant to 18 CPR 385.2013(a), following are the initial observations for this application:
1)The application has not been accepted for processing due to the lack of a request for local zoning
determination, a PE Seal, and site address. Please see the attached September 22, 2015
acknowledgment letter for further detail.
2)The attached acknowledgement letter requests the requested information be submitted within 30
days of receipt of the letter.
3)No studies are necessary in order to evaluate this request.
4)This application is processed under rule 15A NCAC 2Q .0312 which requires the North Carolina
Division of Air Quality (NC DAQ) to complete the technical review of the application within 90
days of receipt of a complete application. It is anticipated this will result in air permit issuance by
December 31, 2015.
5)There are no known Federal laws which set schedules for the NC DAQ to act.
If you have any questions or require further information please feel free to call me at 919-791-4276.
attachment
c: RRO files
Slllcerely, /11, !1�
� McEachem, III, P.E., Environmental Engineer
Division of Air Quality, NC DEQ
Raleigh Regional Office
3800 Barrett Drive, Raleigh, North Carolina 27609
Phone: [phone] \ FAX: [phone] \ Internet: www.ncdenr.gov
An Equal Opportunity I Affinnative Action Employer -Made In part by recycled paper
Page F-267
Attachment F. Air Quality Permit Application Review Documents
,. • . . ¥1tE
North Carolina Department of Environmental Quality 3¾-t,L �
Pat McCrory Governor
CERTIFIED MAil,
RETURN RECEIPT REQUESTED
• •• j
• . ' i'·
Ms. Leslie 'l��VP Pipeline. Constructi�n
Northampton Compressor Statioµ
707 E. Main Str�et .-
Richmond, VA 23219 . .
September 22, 2015
SUBJECT: Receipt of Permit Applicati(?n
Gre�nfield Facility
App���ti·o� No .. 6600 1_69.l�A
Northampton Compressor Station
·Facility ID: 66Q0169, Pleasant Hill, Northampton County
Dear Ms. Hartz: I '
Donald R. van der Vaart Secretary
' , '
·, � ,,.,
• I_ Yo� air permit applica�on (6600169.15A) forN�nh�pton Compress9r Station, locat�d in
Northampton County, North Carolina received by this Division on September 17, 2015 has been
deemed to be incomplete. Your air permit application request must include the following items:
'• I ... 1., '
Local zoning and subdivision ordinances consistency determination: I . . . . . . . .
Your appli�ation did ·not contain the complete request for cons�stency determination. Your
application must 'include a copy of your written request for a ''.determination of consistency" with
local government ordinances bearing the date of receipt entered by the clerk of each local
government having jurisdiction. The following is a detailed explanation of the determination of
consistency req1:1ll'ements, and includes a description of documentation that must be su�mitted with
your application.
a.The permit applicant shall submit a signed statement listing any and all local governments
having jurisdiction over any part of the land on which the facility and its appurtenances are
to be located.
Raleigh Regional Office -Division of Air Quality 3800 Barrett Drive, Raleigh, North Carolina 27609 Phone: [phone] / FAX: [phone] Internet: www.ncdenr.gov
An Equal Opportunity I Affinnatfva Action Employer -Mada In part by recycled paper
Page F-268
Attachment F. Air Quality Permit Application Review Documents
September-2'r,2015
Page 2
b.The applicant is required to send a zoning consistency request determination to each and
every lc>'cal government entity identified by the applicant as stated above.
c.The zoning consistency request determination from the applicant to the local government
s}lall include a �opy of th� draft permit applicati9�. . __ . _, . � � ' __ · ...._. .. ( . ' ... d.The zoning consistency request must be d�livered to the clerk of the local government
personally or by certified mail. Personal delivery should be evidenced by a transmittal
letter from the facility stamped received by the local government, dated, and signed by
the official designated by the government to make such a determination. The stamped
received transmittal letter must be included in the permit application submitted to the
Division, ·
' . e.The required zoning consistency determination in response to the request by the applicant
must be signed by the official designated by the local government to make 'such a
determination. If the local government states that the facility is inc�nsistent with a zoning
or subdivision ordinaµce, a copy of such a determinati6n shall be �b�tted t'? the applicant.. :.·-·,. PE Seal Requirement: ..\
The technical portion(s) of your application was not sealed by a North <;arolina registered
professional engineer (PE) as required by 15ANCAC 2Q.0112. You are required t� re-submit
the technical portion(s) of your application.bearing the seal of a North Carolina PE.
� .: I' I
Additional· Requirements:
The Form Al does not µiclude the site address (911 Address) or zip 'code. Please include them in
your response.
' . . ' 1 < 1 I · 1 In summary, this application did not contain all the required elements as indicated above and
has not been a��epted for proce·ssing. This informatio� must be submitted. and con� the above
requested information.' The requested information must be submitted to our Qffice wilhln; thirty
(3 0) days Or the °application tna� b� terminated, I
·'
, : • . •
' . Should you have any questions concerning this mlltter, please contact Charles McEachern at
919-791-4200..
cc: Raleigh Regional Office Files
. s;i�y, J1 '1�,-_ ,}l:,rtB'1.{, P'.l.legional Stip�so;
� Division of Air Quality, NCDENR
Page F-269
Attachment F. Air Quality Permit Application Review Documents
Facility Name
Facility Street Address
Facility City
Description of Process
SIC/NAICS Code
Facility Contact
Zoning Consistency Determination
Northampton Compressor Station
Northampton County Parcel 0500230 to be further defined by
survey. Address to be assigned asso ciated with structures.
Pleasant Hill Towns hip
zn. -JNatural gas transmission __ .........__ _____ o --
J4922/486210 �
William Scarpinato .,,
Phone Number 804-273-3019 l }
Mailing Address
Mailin g City, State Zip
5000 Dominion Bo ulevard
Glen Allen, VA 23060
Based on the information iven above:
/j(... I have received a copy of the air permit application (draft or final) AND ...
r There are no applicable zoning ordinances for this facility at this time
r The proposed operation IS consistent with applicable zoning ordinances r The proposed operation IS NOT consistent with applicable zoning ordinances
(please include a copy of the rules in the package sent to the air quality office)
)(. The determination is pending further information and can not be made at this time r Other:
Agency
Name of Designated Official
Title of Designated Official
Signature
Date
Northampton County
Kimberly L. Turner
Please forward to the facility mailing address listed above and the air quality office
at the a ro riate address as checked on the back of this form.
Courtesy of the Small Business Environmental Assistance Program
sb.ncdenr.gov 877-623-6748
o·
I ,_.
(!)
Page F-270
Attachment F. Air Quality Permit Application Review Documents
Dominion Resources Services, Inc,
5000 Dominion Boulevard, Glen Allen, VA 23060
Web Address: www.dom.com
October 20, 2015
BY: OVERNIGHT MAIL
Charles McEachern
Regional Supervisor
Raleigh Regional Office
NCDEQ Division of Air Quality
Suite 101
3800 Barrett Drive
Raleigh, NC 27609
RE: Northampton Compressor Station
New Source Permit Application
Professional Engineer Seal
Dear Mr. McEachern:
�; *'611 Dominion
As requested in letter from Patrick Butler dated September 22, 2015, enclosed is the professional engineer
(PE) sealed portion of the application for the above reference project.
Should you have any questions or need additional in the formation, please feel free to contact William
Scarpinato at [phone] or via email at [e-mail].
Sincerely,
�� �"' Robert M. Bisha
Project Director, Atlantic Coast Pipeline
Dominion Environmental Services
Page F-271
Attachment F. Air Quality Permit Application Review Documents
REVISED: 12/01/01
FORM D O"f 2
TECHNICAL ANALYSIS TO SUPPORT PERMIT APPLICATION
NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate
PROVIDE DETAILED TECHNICAL CALCULATIONS TO SUPPORT ALL EMISSION, CONTROL, AND REGULATORY
DEMONSTRATIONS MADE IN THIS APPLICATION. INCLUDE A COMPREHENSIVE PROCESS FLOW DIAGRAM AS
NECESSARY TO SUPPORT AND CLARIFY CALCULATIONS AND ASSUMPTIONS. ADDRESS THE
FOLLOWING SPECIFIC ISSUES ON SEPARATE PAGES:
05
A SPECIFIC EMISSIONS SOURCE (EMISSION INFORMATION) (FORM B) • SHOW CALCULATIONS USED, INCLUDING EMISSION FACTORS, MATERIAL BALANCES, AND/OR OTHER METHODS FROM WHICH THE POLLUTANT EMISSION RATES IN THIS APPLICATION WERE DERIVED. INCLUDE CALCULATION OF POTENTIAL BEFORE AND, WHERE APPLICABLE, AFTER CONTROLS. CLEARLY STATE ANY ASSUMPTIONS MADE AND PROVIDE ANY REFERENCES AS NEEDED TO SUPPORT MATERIAL BALANCE CALCULATIONS.
B SPECIFIC EMISSION SOURCE (REGULATORY INFORMATION)(FORM E2 • TITLE V ONL VJ· PROVIDE AN ANALYSIS OF ANY REGULATIONS APPLICABLE TO INDIVIDUAL SOURCES AND THE FACILITY AS A WHOLE. INCLUDE A DISCUSSION OUTING METHODS (e.g. FOR TESTING ANO/OR MONITORING REQUIREMENTS) FOR COMPLYING WITH APPLICABLE REGULATIONS, PARTICULARLY THOSE REGULATIONS LIMITING EMISSIONS BASED ON PROCESS RATES OR OTHER OPERATIONAL PARAMETERS. PROVIDE JUSTIFICATION FOR AVOIDANCE OF ANY FEDERAL REGULATIONS (PREVENTION OF SIGNIFICANT
DETERIORATION (PSO), NEW SOURCE PERFORMANCE STANDARDS (NSPS), NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS (NESHAPS), TITLE V), INCLUDING EXEMPTIONS FROM THE FEDERAL REGULATIONS WHICH WOULD OTHERWISE BE APPLICABLE TO THIS FACILITY. SUBMIT ANY REQUIRED TO DOCUMENT COMPLIANCE WITH ANY REGULATIONS. INCLUDE EMISSION RATES CALCULATED IN ITEM "A" ABOVE, DATES OF MANUFACTURE, CONTROL EQUIPMENT, ETC. TO SUPPORT THESE CALCULATIONS.
C CONTROL DEVICE ANALYSIS (FORM C) -PROVIDE A TECHNICAL EVALUATION WITH SUPPORTING REFERENCES FOR ANY CONTROL EFFICIENCIES LISTED ON SECTION C FORMS, OR USED TO REDUCE EMISSION RATES IN CALCULATIONS UNDER ITEM "A" ABOVE. INCLUDE PERTINENT OPERATING PARAMETERS (e.g.
OPERATING CONDITIONS, MANUFACTURING RECOMMENDATIONS, AND PARAMETERS AS APPLIED FOR IN THIS APPLICATION) CRITICAL TO ENSURING PROPER PERFORMANCE OF THE CONTROL DEVICES). INCLUDE AND LIMITATIONS OR MALFUNCTION POTENTIAL FOR THE PARTICULAR CONTROL DEVICES
AS EMPLOYED AT THIS FACILITY. DETAIL PROCEDURES FOR ASSURING PROPER OPERATION OF THE CONTROL DEVICE INCLUDING MONITORING SYSTEMS AND MAINTENANCE TO BE PERFORMED.
D PROCESS AND OPERATIONAL COMPLIANCE ANALYSIS· (FORM E3 • TITLE V ONL VJ -SHOWING HOW COMPLIANCE WILL BE ACHIEVED WHEN USING PROCESS, OPERATIONAL, OR OTHER DATA TO DEMONSTRATE COMPLIANCE. REFER TO COMPLIANCE REQUIREMENTS IN THE REGULATORY ANALYSIS IN ITEM "B" WHERE APPROPRIATE. LIST ANY CONDITIONS OR PARAMETERS THAT CAN BE MONITORED AND REPORTED TO DEMONSTRATE COMPLIANCE WITH
THE APPLICABLE REGULATIONS.
E PROFESSIONAL ENGINEERING SEAL· PURSUANT TO 15A NCAC 20 .0112 "APPLICATION REQUIRING A PROFESSIONAL ENGINEERING SEAL,"
A PROFESSIONAL ENGINEER REGISTERED IN NORTH CAROLINA SHALL BE REQUIRED TO SEAL TECHNICAL PORTIONS OF THIS APPLICATION FOR
NEW SOURCES AND MODIFICATIONS OF EXISTING SOURCES. (SEE INSTRUCTIONS FOR FURTHER APPLICABILITY).
I, __ T<_c�k-��,.Y"--=J���-w_Jli ___ l-_<.... ____ �, attest that this application for
1 ________________ has been reviewed by me and is accurate, complete and consistent with the information supplied
in the engineering plans, calculations, and all other supporting documentation to the best of my knowledge. I further attest that to the best of my
knowledge the proposed design has been prepared in accordance with the applicable regulations. Although certain portions of this submittal
package may have been developed °by other professionals, inclusion of these materials under my seal signifies that I have reviewed this material
and have judged it to be consistent with the proposed design. Note: In accordance with NC General Statutes 143-215.6A and 143-215.68, any
person who knowingly makes any false statement, representation, or certification in any application shall be guilty of a Class 2 misdemeanor which
may include a fine not to exceed $10,000 as well as civil penalties up to $25,000 per violation.
(PLEASE USE BLUE INK TO COMPLETE THE FOLLOWING)
NAME: Jeffrey H. Twaddle, P.E.
DATE: October 14, 2015
COMPANY: ERM Southeast, Inc.
ADDRESS: 5000 Meridian Blvd., Ste. 300, Franklin, TN 37067
TELEPHONE: [phone]
SIGNATURE:
PAGES CERTIFIED: Appendix A -Form C3 for CT-01-SCR & CT-01-0C,
CT-02-SCR & CT-02-0C, and
CT-03-SCR & CT-03-OC
Appendix C -Potential to Emit Calculations
(IDENTIFY ABOVE EACH PERMIT FORM AND ATTACHMENT
THAT IS BEING CERTIAED BY THIS SEAL)
PLACE! NORTH CAROLINA SEAL HERE
Page F-272
Attachment F. Air Quality Permit Application Review Documents
APPENDIX A
NC DENR PERMIT APPLICATION FORMS
ERM ,\CP, LLC -ACP-3STATJON ··--------------------------------------------
Page F-273
Attachment F. Air Quality Permit Application Review Documents
REVISED 12/01/01
FORM C3
CONTROL DEVICE (THERMAL OR CATALYTIC)
I"""' -I " 11 'it, I
NCDENR/Division of Air Quality -Application for Air Permit to Construct/Operate .. -I C3
AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGIHf.li,HP:E)fb�'iN 1NeiR-TH 6.RoilN'Ji:
CONTROL DEVICE ID NO: CT-01-SCR and CT-01-OC lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-01
EMISSION POINT (STACK) ID NO(S): EP-01 !POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1
MANUFACTURER: MODEL NO:
MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018
OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017
1 of 1
TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION
X CATALYTIC OXIDATION
EXPECTED LIFE OF CATALYST (YRS): TBD I METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL
TBD SULFUR COMPOUND OTHER NONE
TYPE OF CATALYST: TBD lcATAL YST VOL (FT3): TBD !VELOCITY THROUGH CATALYST (FPS): TBD
SCFM THROUGH CATALYST:
DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES ANO SOURCES, AND ATTACH DIAGRAM OF SYSTEM:
Selective Catalyst Reduction and Oxidation Catalyst
POLLUTANT(S) COLLECTED: NO, co voe Formaldehyde
BEFORE CONTROL EMISSION RATE (LB/HR):
CAPTURE EFFICIENCY: % % % %
CONTROL DEVICE EFFICIENCY: 44 % 80 % 50 % 50 %
OVERALL SYSTEM EFFICIENCY: % % % %
EFFICIENCY DETERMINATION CODE:
TOTAL EMISSION RATE (LB/HR):
PRESSURE DROP (IN. H2O): MIN MAX OUTLET TEMPERATURE (°F): MIN MAX
INLET TEMPERATURE (°F): MIN MAX RESIDENCE TIME (SECONDS):
INLET AIR FLOW RATE (ACFM): (SCFM): COMBUSTION TEMPERATURE (°F):
COMBUSTION CHAMBER VOLUME (FT3): INLET MOISTURE CONTENT (%):
% EXCESS AIR: CONCENTRATION (ppmv) INLET OUTLET
AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR):
MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS:
ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: UNITS:
DESCRIBE METHOD USED TO INCREASE MIXING:
DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE:
DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES:
STACK TESTING PORTS: l:i NO l:iYES (INLET AND OUTLET)
DESCRIBE MAINTENANCE PROCEDURES:
DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM:
ATTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):
Attach Additional Sheets As Necessary
Page F-274
Attachment F. Air Quality Permit Application Review Documents
FORM C3
CONTROL DEVICE (THERMAL OR CATALYTIC)
REVISED 12/01/01 NCDENR/Dlvislon of Air Quality -Application for Air Penni! to Construct/Operate I C3
AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA.
CONTROL DEVICE ID NO: CT-02-SCR and CT-02-OC lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-02
EMISSION POINT (STACK) ID NO(S): EP-02 !POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1
MANUFACTURER: MODEL NO:
MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018
OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017
1 of 1
TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION
X CATALYTIC OXIDATION EXPECTED LIFE OF CATALYST (YRS): TBD I METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL
TBD SULFUR COMPOUND OTHER NONE
TYPE OF CATALYST: TBD lcATALYST VOL (FT\ TBD I VELOCITY THROUGH CATALYST (FPS): TBD
SCFM THROUGH CATALYST:
DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM:
Selective Catalyst Reduction and Oxidation Catalyst
POLLUTANT(�) COLLECTED: NO, co voe Formaldehyde
BEFORE CONTROL EMISSION RATE (LB/HR):
CAPTURE EFFICIENCY: % % % %
CONTROL DEVICE EFFICIENCY: 44 % 80 % 50 % 50 %
OVERALL SYSTEM EFFICIENCY: % % % %
EFFICIENCY DETERMINATION CODE:
TOTAL EMISSION RATE (LB/HR):
PRESSURE DROP (IN. H2O): MIN MAX OUTLET TEMPERATURE (°F): MIN MAX
INLET TEMPERATURE (°F): MIN MAX RESIDENCE TIME (SECONDS}:
INLET AIR FLOW RATE (ACFM}: (SCFM): COMBUSTION TEMPERATURE (°F):
COMBUSTION CHAMBER VOLUME (FT3): INLET MOISTURE CONTENT (%):
% EXCESS AIR: CONCENTRATION (ppmv} INLET OUTLET
AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR}:
MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS:
ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: UNITS:
DESCRIBE METHOD USED TO INCREASE MIXING: '
DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE:
DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES:
STACK TESTING PORTS: l.:i NO l.:iYES (INLET AND OUTLET)
DESCRIBE MAINTENANCE PROCEDURES:
DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM:
ATTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):
Attach Additional Sheets As Necessary
Page F-275
Attachment F. Air Quality Permit Application Review Documents
FORM C3
CONTROL DEVICE (THERMAL OR CATALYTIC)
REVISED 12/01/01 NCDENR/Division of Air Quality. Application for Air Permit to Construct/Operate I C3
AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONALENGINNER (P.E.) LICENSED IN NORTH CAROUNA.
CONTROL DEVICE ID NO: CT-03-SCR and CT-03-OC lcoNTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): CT-03
EMISSION POINT (STACK) ID NO(S): EP-03 !POSITION IN SERIES OF CONTROLS 1 NO. OF UNITS 1
MANUFACTURER: MODEL NO:
MANUFACTURE DATE: PROPOSED OPERATION DATE: November 2018
OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: April 2017
1 of 1
TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION
X CATALYTIC OXIDATION
EXPECTED LIFE OF CATALYST (YRS): TBD I METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT: TBD CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL
TBD SULFUR COMPOUND OTHER NONE
TYPE OF CATALYST: TBD lcATAL YST VOL (FT3): TBD I VELOCITY THROUGH CATALYST (FPS): TBD
SCFM THROUGH CATALYST:
DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM:
Selective Catalyst Reduction and Oxidation Catalyst
POLLUTANT(S) COLLECTED: NO, co voe Formaldehyde
BEFORE CONTROL EMISSION RATE (LB/HR):
CAPTURE EFFICIENCY: % % % %
CONTROL DEVICE EFFICIENCY: 80 % 90 % 50 % 50 %
OVERALL SYSTEM EFFICIENCY: % % % %
EFFICIENCY DETERMINATION CODE:
TOTAL EMISSION RATE (LB/HR):
PRESSURE DROP (IN. H2O): MIN MAX OUTLET TEMPERATURE (°F): MIN MAX
INLET TEMPERATURE (°F): MIN MAX RESIDENCE TIME (SECONDS):
INLET AIR FLOW RATE (ACFM): (SCFM): COMBUSTION TEMPERATURE (°F):
COMBUSTION CHAMBER VOLUME (FT3): INLET MOISTURE CONTENT (%):
% EXCESS AIR: CONCENTRATION (ppmv) INLET OUTLET
AUXILIARY FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR):
MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS:
ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: UNITS:
DESCRIBE METHOD USED TO INCREASE MIXIN9:
DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE:
DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES:
STACK TESTING PORTS: G NO GYES (INLET AND OUTLET)
DESCRIBE MAINTENANCE PROCEDURES:
DESCRIBE ANY AUXILIARY MATERIALS INTRODUCED INTO THE CONTROL SYSTEM:
ATTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):
Attach Additional Sheets As Necessary
Page F-276
Attachment F. Air Quality Permit Application Review Documents
APPENDJXC
POTENTIAL TO EMIT CALCULATIONS
ACP, LLC • ACl'-3STA110N -----·---------------------------------------
Page F-277
Attachment F. Air Quality Permit Application Review Documents
Table C-2 Pote11ti11/ E111issio11s From Comb11stio11 Sources
ACP Nortli111npto11 Compressor St11tio11 -Nortl,11,npto11 Co,mhJ, Nortlr Caroli1111
Turbine Operational Parameters: Emergency Generator Qperiltional Hours:
Normal Hours or Opera.hon: 8,677 Normal Hours of Oeeration: 100
Hours • l Low Load ( <50%) 0
Hours of low Temo. (< 0 de2 F) 50
Hours of Start-un/Shut-down 33.3
Total Hours o( Operation {hr/ vr): 8,760
Pre-Control Potential to Emit
Power Crltorla Pollutant• (tn,
Combustion Sourcu Ratlno Unlta Fuel NOx co voe SO2 PMF
Solar Taurus 70 Turbine 10,915 ho Natural Gas 14.9 23.8 1.36 1.43 2.42
Solar Canlaur SOL Turbine 6,200 ho Nalural Gas 9.2 14.8 0.834 0.894 1.51
Solar Centaur 40 Turbine 4.700 ho Natural Ga, 22.0 25.6 0.702 0.760 1.29
Caleroillar G3516 Eaen 1.416 ho Natural Gas 0.312 0.295 0.0375 0.0003 0.0214
Boiler 6.3 MMBlu/hr Natural Ga, 1.35 2.27 0.149 0.0162 0.0514
Total/Ions vrJ 47.7 66.8 3.08 3.10 5.3
Turbine Control Efficiencies
Control TechnoloRV NOx co voe
Selective Catalvtic R�uction (C�ntaur 40) 80% .
Select1vo Catalyuc Reducllon (All Olhors) 44% .
Oxidation Catalvst (Centaur 40l 90% 50%
Ox1dallon Catalyst (All Others) 80'k 50%
Post-Control Potential to Emit
Power Criteria Pollutants ftnu
Combusllon Soun:n Ratlno Unlta Fuel NOx co
Solar Taurus 70 Turbine 10915 ho Natural Gas 8.25 4.76
Solar Centaur SOL Tur�ne 6200 ho Natural Gas 5.14 2.96
Solar Centaur 40 Turbine 4700 ho Natural Gas 4.39 2.56
Caterpillar G3516 Enan 1416 ho Natural Gas 0.312 0.295
Boiler 6.3 MMBlu/hr Natural Gas 1.35 2.27
Tola/(lons. vrl 19.4 12.8
Notes:
(1) Turbine emissions are calculated by the following formula. ER• Run Hours / 2000 • (1 • Control Efficiency)
ER = Emission Rate for particular equipment and pollutant (lbs/hr)
2000 = the amount of lbs in a ton
voe
0.680
0.417
0.351
0.0375
0.149
1.63
(2) Emergency Generator emissions are calculated by the follow,ng formula: Power Rating • Run Hours • EF / 20001
Power Rating= Engine hp rating (hp)
EF = Emission Factor from either manufacture(s data or AP-42 (lb/hp-hr)
2000 = the amount of lbs in a ton
(3) Boiler/Healer emissions calculated by the following formula. EF • Power Rating • Run Hours / HHV / 2000
EF = AP-42 Emission Factor (lb/MMSCF)
Power Rating s=.Boiler/Heatar Heal Capacjly (MMBlu/hr)
HHV = Nalurol Gas High Heating Value ('lb20 MMBtu/MMSCF)
SO2 PMF
1.43 2.42
0.894 1.51
0.760 1.29
0.0003 0.0214
0.0162 0.0514
3.10 5.3
Uoiler{Heatcr Operational Parameters:
8,760
PMF-10 PMF-2.S PMC CO2
2.42 2.42 5.99 49,980
1.51 1.51 3.74 31,295
1.29 1.29 3.18 26,718
0.0214 0.0214 0.006 77.9
0.0514 0.0514 0.154 3246
5.3 5.3 13.07 111,317
PMF-10 PMF-2.S PMC CO2
2.42 2.42 5.99 49,980
1.51 1.51 3.74 31.295
1.29 1.29 3.18 26,718
0.0214 0.0214 0.006 77.9
0.0514 0.0514 0.154 3,246
5.3 5.3 13.07 111,317
(4) Turbines are equipped with Selective Catalytic Reduction (SCR) and oxidation catalyst for control of NOx (44%), CO (80%), and VOC (50%)
(5) Taurus Centaur 40 oxidation catalyst has a control of 90% for CO
(6) Emergency generator engine hp taken from manufacturer data
(7) Boller assumed to have low-NO� burners
(8) See the ·HAP Emissions· worksheet for a more detailed breakdown of HAP emissions
(9) See Emissions Factors table for Em1ss1ons Factors for each operating scenario.
(10) Each start-up/shut-down event assumed to last 10 minutes
GHG Emissions (tp� Ammonia (tpy) HAP ftpy) CH4 N2O CO2• nnJ Total HAP
3.62 1.26 50,446 5.77 0.525
2.26 0.788 31 587 3.58 0.352
1.92 0.671 26.966 3.02 0.286
0.290 0 85.1 0 0.0143
0.0622 0.0595 3266 0 0.0511
8.15 2.78 112 350 12.4 1.23
GHG Emlsalona ltov Ammonia ltnvl HAP llnvl
CH4 N2O CO2• nn• I Ol81 �
3.62 1.26 50,446 5.77 0.525
2.26 0.788 31,587 3.58 0.352
1.92 0.671 26,966 3.02 0.286
0.290 0 85.1 0 0.0143
0.0622 0 0595 3 266 0 0.0511
8.15 2.78 112 350 12.4 1.229
Page F-278
Attachment F. Air Quality Permit Application Review Documents
Tnblt c-.1 F.pprf llns,,t PoftNliul E,nissiOl'fS From Cmlflmslf,m StnlrC'£S
ACP Nortl,mnplolf Compressor Station-Nortlum,plo" Co,mty, Nortl, Carolin11
S11d11P Ernl111Po1
Cltfflbu•lion Souru1 l ::=Units l Solar Tauru1 ,u urtiu,11 10 915 � SolarCanta...-50l Tutbina 6200 h• SolarContai,4u urbln11 4700 no ot•I Ion
SbMtdowo Emt11kK11
CCHMIU9UOfl&ou--I•-.....u. .. I Sobt Tourus 70 Tutbna 10915 ho Sd.atCunla...-SOl. Turbine 6200 =
.5olarC��OT� 4700 no .,., ....
i'ot.J !iEl> lm111Jon1 ''°"�
�i!!!li!!IIU! l!!il:dbm Em!11!2!!! -�'I
,hi
�
FUG-01
38000 sdlevool 385 ,cf.axno, 16 lb--bmol �i� I�
.... l llarl,up E,...nla NU•
Natural Gal ,�
Nalura!Gaa 100 0.0400
NaluralGaa 100
n.115
Fuel
I anuldown
Ewnll "'"
Naua!Gas 100 0.0550 ·--100 0.0200 ·-Gu 100 nn1,o ··-
I ilo!I
Dton•no Slud4awa ftrtb
,. ....... ... Mal•ul•r W11l9h1
C11¥1b--'1
(�;:' I w\:�t�;"r,1
Taul Stru• MMllnl.a, W11,gh1 N_.l'DC
Ctdu10iouN
-N,---......... , .. � �
n-a..ww
n-fmt.11,w ....,_�
n-Jlu-,1111 -.. ,--
Tot.alV�Pr�!I� Toul HAP Fr.at1h111
Plan4ffn• t:mm 5UdMP ErHM
Combuatfon loutcaa Solar Tauru• 70 T...-bine
Solar ContDIJI' 50L Tutbl'le SolarCenl....-.0Turtwae
Tot•I lonut,t
lhPw"9na fmn Sh1114owa Enrm
COMbuation loul'ICM So&ar Taurua 70 Turtiine So&arC....._.50l Turtw111 Sdar"Cantaur40 �
Tolal ton
, ........,..,,. ..,.., .....
5112
51.12
71.15 7'.15
7811
11D21
I Slal1-Up ......
100 100
100
,·-·-100 100 100
2 000000 3115 iii
93%
�Q
,brlup ......
I fo,a1 81awd0wn tmiuJo,u {fon!"r!J
1.0U'-' 0.99-11. �ll'S ,ms •=•
0.08'1. 0.0791.
0.0221. 0.0241.
O.OJ21.
0.1M9'-
voe 2.216 2.216 2.216
1.149
voe 3.675 3675 3.675
11.024
voe
1167 �,H!7
11.1
""" , .....'"""............·-,.,,,.--, .....
1.1� ,.,.,
CO2
2.293 2.293 2.293
I.NO
r.n,
3.00 300 J.B<I
1U1
U.5
nHr. , ... n• CH4 CO2•
75.634 1893
75.634 1893
75.634 1893
227 5171
ft OEmlaai..M CILI
l"539 3139 12539 3139
125.39 l 139
'7" .,,.
ffl it�Oll
Criari•'"olutants
OU
J.66 3.46 3.22
1D.3 3
Criterta Palutants
I
cu
4.67 177
1.51
7.950
11.21
63000 385-
To"
93%
26<13
HAPI
0.125 0.125
0.125
D.375
..,. ..0.207 0.207 0.207
D.12 2
HAP,
0066 @.Olfi
1.DI
I
0.
0.0400 003 70
0.119
0.0530
00200 0017D . ....
0.209
ld/eVWJI ,clbnol
M>mol
lblewnl
tn111'6n1' ... coz CH4 co2,
26.0 0.168 30.2
23.5 0.180 27.5 18.6 0.1<18 23.3
11.D 0,4715 IIU
m1 .. 1on.'"i.::':'l"
coz ""' cu2,
28.8 D.212 34 1
109 0.0800 12 9 ... n068()J_ 1Q.8 ... .. ,-
I 117.7 I Gill I 131
Page F-279
Attachment F. Air Quality Permit Application Review Documents
Table C-4 Combustion Source Criteria Pollutant Emission Factors
ACP Northampton Compressor Station -Northampton CormhJ, North Carolina
Solar Turbine Normal Operation Emission Factors (lb/hr)
Eaulomant Name Fuel Units NOx co voe SO2 PMF PMF-10 PMF-2.5 PMC CO2 CH4 N2O
Solar Centaur 40 Turbine Natural Gas lb/hr 4.70 5.70 0.160 0.173 0.294 0.294 0.294 0.727 6100 0.439 0.153
Solar Centaur SOL Turbine Natural Gas lb/hr 1.98 3.30 0.190 0.204 0.345 0.345 0.345 0.855 7145 0.516 0.180
Solar Taurus 70 Turbine Natural Gas lb/hr 3.18 5.30 0.310 0.326 0.553 0.553 0.553 1.37 11411 0.826 0.288
Noles
(1) Pre-Control Emission Rates for NOx, CO, VOC, PMF, PMC, and CO2 taken from Solar Turbine Data al 100% load and 0 degrees F
(2) Emission Factors for SO2, CH4, N2O taken from AP-42 in (lbs/MMBlu) and multiplied by turbine fuel throughput by Solar Turbine al 100% load and 0 degree F to gel Emission Rates
(3) Assume PMF=PMF-1 0=PMF-2.5: Filterable and Condensable based on Solar Turbine Emission Factor and ratio of AP-42 Table 3.1 factors
(4) NH3 emission rates based on a 10 ppm ammonia slip from the SCR based on manufacturer information
(5) CO2e emission rate calculated by multiplying each GHG (CO2, CH4, N2O) by its Global Warming Potential (GWP) and adding them together
(6) CO2 GWP = 1; CH4 GWP = 25; N2O GWP = 298 [40 CFR Part 98]
Solar Turbine Alternate Ooaratfon Emission Factors lb/hrl
< 0 daarees F Solar Turbine Low Load F
Enul�-ent Name Fuel Units NOx co voe NOx co voe
Solar Centaur 40 Turbine Natural Gas lb/hr 62.7 34.2 0.320 36.6 2,280 6.40
Solar Centaur SOL Turbine Natural Gas lb/hr 26.4 19.8 0.380 15.4 1,320 7.60
Solar Taurus 70 Turbine Natural Gas lb/hr 42.4 31.8 0.620 24.7 2,120 12.4
Notes
(1) Pre-Control low temperature Emission Rates for NOx, CO, VOC. Conservatively assume 120 ppm NOx, 150 ppm CO, and 5 ppm VOC (10% of UHC) per Table 2 of Solar PIL 167
(2) Pre-Control low load Emission Rates for NOx, CO, voe. Conservatively assume 70 ppm NOx, 10,000 ppm CO, and 100 ppm voe (10% of UHC) per Table 4 of Solar PIL 167
Solar Turbine Start-uo and Shutdown Emission Factors llb/eventl
Start-uo EFs Shutdown EFs
Eauloment Name Fuel Units NOx co voe CO2 CH4 CO2e NOx co voe CO2
Solar Centaur 40 Turbine Natural Gas lb/event 0.700 64.4 0.740 392 2.96 466 0.300 30.2 0.340 181
Solar Centaur SOL Turbine Natural Gas lb/event 0.800 69.1 0.800 469 3.20 549 0.400 35.4 0400 217
Solar Taurus 70 Turbine Natural Gas lb/event 0.800 73.1 0.840 519 3.36 603 1.10 93.4 1.06 575
Noles
(1) Start-up and Shutdown Emissions based on Solar Turbines Incorporated Product Information Leller 170: Emission Estimates al Start-up, Shutdown, and Commissioning for
SoLoNOx Combustion Products (13 June 2012). Emission Estimates do not include SO2, PM, N2O. or any HAPs.
(2) VOCs assumed to be 20% of UHC and CH4 assumed lo be 80% of UHC.
(3) CO2e emission rate calculated by multiplying each GHG (CO2, CH4) by its Global Warming Potential (GWP) and adding them together
(4) CO2 GWP = 1; CH4 GWP = 25; [40 CFR Part 98]
Engine and Boller Emission Factors
Eaulhment Tuna Fuel Units NOx co voe SO2 PMF PMF-10
Boiler< 100 MMBlu Natural Gas lb/MMscf 50 84 5.5 0.6 1.9 1.9
Space & Waler Healers Natural Gas lb/MMscf 100 84 5.5 0.6 1.9 1.9
Enoine 2 SLB Natural Gas lb/MMBtu 3.17 0.386 0.12 0.000588 0.0384 0.0384
1000 KW Caterpillar Eaen Natural Gas lb/hp-hr 0.004408 0.004166 0.000529 4.62E-06 0.0003018 0.00030179
Noles
(1) NOx, CO, VOC, and PMF-10 Emission Factors for Boilers < 100 MMBtu from ETI Combustion Analysis June 2015
(2) All other emission factors for natural gas boilers taken from AP-42 Tables 1.4-1 & 1.4-2
(3) Emission Factors for Space & Water Healers taken from AP-42 Tables 1.4-1 & 1.4-2
(4) Emission Factors for 2 SLB engme taken from AP-42 Table 3.2-1
(5) NOx, CO, VOC, CO2, and CH4 emission factors for Caterpillar Egens taken from Caterpillar Manufacturer data
PMF-2.5
1.9
1.9 •
0.0384
0.uut 302
PMC CO2
5.7 120000
5.7 120000
0.00991 110
7.79E-05 1.0998
(6) SO2, PMF, PMF-10. PMF-2.5, PMC, and N2O Emission factors for Caterpillar Egens taken Imm AP-42 Table 3.2-1 and converted using manufacturer fuel data
(7) Assume PMF=PMF-10=PMF-2.5
(8) CO2e emission rate calculated by multiplying each GHG (CO2, CH4, N2O) by its Global Warming Potential (GWP) and adding them together
(9) CO2 GWP = 1; CH4 GWP = 25; N2O GWP = 298 [40 CFR 98]
CH4
2.3
2.3
1.45
0.0041
CH4
1.36
1.60
4.24
N2O
2.2
2.2
0
0
CO2a NH3
6157 0.690
7212 0.818
11517 1.32
CO2e
215
257
681
CO2e NH3
120713 0.00
120713 0.00
146 0.00
1 0.00
Page F-280
Attachment F. Air Quality Permit Application Review Documents
Table C-6 Combustion Source HAP Emission Factors
ACP Northampton Compressor Station -Northampton County, North Carolina
Emission Factors
So[ar Centaur Solar Centaur Solar Taurus Boller< 100 1000 KW
Pollutant HAP? Caterpillar 40 Turbine SOL Turbine 70 Turbine MMBtu Egan
lb/MMBtu lb/MMBtu lb/MMBtu lb/MMscf lb/ho-hr
1, 1,2,2-Tetrachloroelhane Yes 1.7E-07
1, 1,2-Trichloroelhane Yes 1.3E-07
1 1-Dichloroelhane Yes 9.9E-OB
1,2,3-Trimethylbenzene No 9.0E-08
1,2,4-TrimelhY1benzene No 2.BE-07
1 2-Dlchloroelhane Yes 1.1E-07
1,2-Dichloroorooane Yes 1.1E-07
1,3,5-Trimethv!benzene No 4.6E-OB
1,3-Butadlene Yes 2.1E-06
1 3-Dichloroorooene Yes 1.1E-07
2,2 4-Trimethvloentane Yes 2.2E-06
2-Methvlnaohlhalene No 2.4E-05 5.4E-OB
3-Methvlchloranthrene No 1.BE-06
7, 12-Dimethylbenzlalanthracene No 1.6E-05 l
Acenaohthene No 1.BE-06 3.4E-09
Acenaohthvlene No 1.BE-OS B.1E-09
Acetaldehvde Yes 2.0E-05
Acrolein Yes 2.0E-05
Anthracene No 2.4E-06 1.BE-09
Benzi a lanthracene No 1.BE-06 8.SE-10
Benzene Yes 2.1E-03 4.9E-o6
Benzo alnvrene No 1.2E-06 1.4E-11
Benzo b lfl uoranthene No 1.BE-06 2.2E-11
Benzo elovrene No 6.0E-11
Benzo o,h,iloervlene No 1.2E-06 6.3E-11
Benzo k 111 uoranthene No 1.BE-06 1.1E-11
Biohenvf Yes 1.0E-08
Butane No 2.1E+OO 1.2E-05
Butvr/lsobutvraldehvde No 1.1E-06
Carbon Tetrachloride Yes 1.SE-07
Chlorobenzene Yes 1.1E-07
Chloroethane Yes
Chloroform Yes 1.2E-07
Chrvsene No 1.BE-06 1.7E-09
C'lciohexane No 7.BE-07
Cvclooentane No 2.4E-07
Dibenzo(a,h)anthracene No 1.2E-06
Oichlorobenzene Yes 1.2E-03
Ethane No 3.1E+OO 1.BE-04
Elhv!benzene Yes 2.7E-07
Elhvlene Dlbromide Yes 1.9E-07
Fluoranthene No 3.0E-06 9.2E-10
Fluorene No 2.BE-06 4.3E-09
Formaldehvde Yes 2.9E-03 2.9E-03 2.9E-03 7.SE-02 1.4E-04
Hexane (or n-Hexane l Yes 1.BE+OO 1.1E-06
lndeno(1,2 3-<: dlovrene No 1.BE-06 2.SE-11
lsobutane No 9.SE-06
Methanol Yes 6.3E-o6
Methvlr.vclohexane No B.6E-07
Melhvlene Chlonde Yes 3.7E-07
n-Nonane No 7.BE-08
n-Octane No 1.9E-07
Naohthalene Yes 6.1E-04 2.SE-07
PAH Yes 3.4E-07
Pentane /or n-Pentanel No 2.6E+OO 3.9E-06
Pervlene No 1.3E-11
Phenanthrene No 1.7E-05 9.0E-09
Phenol Yes 1.1E-07
Propane No 1.6E+OO 7.3E-05
Proovlene Oxide Yes
Pvrene No 5.0E-06 1.SE-09
Stvrene Yes 1.4E-07
Tetrachloroethane No
Toluene Yes 3.4E-03 2.SE-OS
Vlnvt Chloride+A32 Yes 6.3E-OB
Xvfene Yes 6.BE-07
Arsenic Yes 2.0E-04
Banum No 4.4E-03
Bervlllum Yes 1.2E-05
Cadmium Yes 1.1E-03
Page F-281
Attachment F. Air Quality Permit Application Review Documents
Table C-6 Comb11stion S011rce HAP Emission Factors
ACP Northampton Compressor Station -Northampton Co11nty, North Carolina
Emission Factors
Solar Centaur Solar Centaur Solar Taurus Pollutant HAP? 40 Turbine SOL Turbine 70 Turbine
lb/MMBtu lb/MMBtu lb/MMBtu
Chromium Yes
Cobalt Yes
Coooer No
Manoanese Yes
Mercurv Yes
IV1olvbdenum No
Nickel Yes
Selenium Yes
Vanadium No
Zinc No
Lead Yes
Total HAPs 3.1E-03 3.1E-03 3.1E-03
Hazardous Air Pollulant
Notes:
(1) Emission factors for Solar and Capstone natural gas turbines from AP-42 Table 3.1-3
(2) Emission factors for natural gas boilers from AP-42 Tables 1.4-2, 1.4-3, and 1.4-4
Boller< 100
MMBtu
lb/MMscf
1.4E-03
8.4E-05
8.SE-04
3.BE-04
2.6E-04
1.1E-03
2.1E-03
2.4E-05
2.3E-03
2.9E-02
5.0E-04
1000 KW
Catarplllar
Egen --
lb/ho-hr
(3) Emission factors for 2 SLB natural gas engines and Caterpillar natural gas emergency generators taken from AP-42 Table 3.2-1
(4) Emission factors for Solar natural gas turbines and Caterpillar natural gas emergency generators converted using 1 KWh= 3412 Btu and 1 kw= 1.341 hp
(5) Emission Factors (lb/MMBtu) for Formaldehyde and Total HAPs for Solar Turbines from Solar PIL 168
Page F-282
Attachment F. Air Quality Permit Application Review Documents
' . -
I
Mceachern, Charles
From:
Sent: Laurence A Labrie <[e-mail]>
Wednesday, August 02, 2017 9:24 AM To: Mceachern, Charles Cc:
Subject: Andrew Woerner ([e-mail]); [e-mail]
FW: Northampton Compressor Station Attachments: Northampton Application 07.31.17 -Updated Pages.pdf
Charles,
Attached pages from the application correct the emission factor error. Please let me know if you need any additional
information.
Thanks,
Larry Labrie
Phone: [phone]
Mobile: [phone]
5j;. Dominion:;iiiiiii"' Energy·
From: Robert Sawyer [mailto:[e-mail]]
Sent: Tuesday, August 01, 2017 9:44 PM
To: Laurence A Labrie (Services - 6
)
Cc: Andrew Woerner
Subject: [External] RE: Northampton Compressor Station
Larry,
Please note that we have fixed the fugitive leaks emissions factor error in Table C-7.
The attached document includes the following replacement pages associated with this correction:
Form B -Fugitive Leaks -Piping Source Information
Form D1 -Facility-wide Emissions Summary
Table C-7 -Potential Emissions from Fugitive Leaks
Table C-9 -Project Potential Emissions
Let me know if you have any questions.
Robert Sawyer
Maryland & DC Area Manager
ERM
180 Admiral Cochrane Drive, Suite 400 I Annapolis, MD I 21401
T +1 410.266.0006 I M +1 848.219.1707
E [e-mail] I W www.erm.com
� ERM The business of sustainabililY
1
Page F-283
Attachment F. Air Quality Permit Application Review Documents
From: Laurence A Labrie [mailto:[e-mail]]
Sent: Friday, July 28, 2017 10:45 AM
To: Andrew Woerner; Robert Sawyer
Subject: Northampton Compressor Station
------------
Got a question from Charles McEachern at NCDEQ about fugitive emission calculations. He said he check the source of
the emission calculation procedure and determined that the emission factor units are in kilograms not pounds, which
would increase emission value.
Larry Labrie
Phone: [phone]
Mobile: [phone]
� Dominion� Energy·
CONFIDENTIALITY NOTICE: This electronic message contains information which may be legally
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relating thereto which binds the sender without an additional express written confirmation to that effect. The
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unauthorized. If you are not the intended recipient, any disclosure, copying, distribution, or use of the contents
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system. Thank you,
Please visit ERM's web site: http://www.erm.com
CONFIDENTIALITY NOTICE: This electronic message contains information which may be legally
confidential and or privileged and does not in any case represent a firm ENERGY COMMODITY bid or offer
relating thereto which binds the sender without an additional express written confirmation to that effect. The
information is intended solely for the individual or entity named above and access by anyone else is
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please reply immediately to the sender that you have received the message in error, and delete it. Thank you.
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I
Page F-284
Attachment F. Air Quality Permit Application Review Documents
FORM B
SPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)
REVISED 12/01101 NCDENR/Dlvlslon of Air Quality-Application for Alr Permit to Construct/Operate B
EMISSION SOURCE DESCRIPTION; EMISSION SOURCE ID NO: Fug-02
Fugitive Leaks -Piping CONTROL DEVICE ID NO(S): NA
OPERATING SCENARIO 1 of 1 EMISSION POINT (STACK) ID NO(S): NA
DESCRIBE IN DETAJLTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):
Fugitive Emissions from station piping leaks.
TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):
[)coal,wood,oil, gas, other burner (Form B 1) OWoodworking (Form B4) O Manufact. of chemicals/coatings/inks (Form B7)
Dint.combustion engine/generator (Form B2) 0 Coating/finishing/printing (Form B5) 0 Incineration (Form B8) 0 Liquid storage tanks (Form B3) O Storage silos/bins (Form B6) 0 Other (Form B9)
START CONSTRUCTION DAT April 2017IOPERATION DATE: November 2018 DATE MANUFACTURED: 2016 or Later
MANUFACTURER / MODEL NO.: NA EXPECTED OP. SCHEDULE: 24 HR/DAY 7 DAY/WK 52 WK/YR
IS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): No NESHAP (SUBPART?): No MACT (SUBPART?): No
PERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25
EXPECTED ANNUAL HOURS OF OPERATION: 8,760 VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: %OPACITY
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS/ LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS / LIMITS)
AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
PARTICULATE MATTER (PM) -- -----
PARTICULATE MATTER<10 MICRONS (PM,0) -------
PARTICULATE MA TTER<2.5 MICRONS (PM2 5) -------
SULFUR DIOXIDE (SO2) ---- ---
NITROGEN OXIDES (NOx) -------
CARBON MONOXIDE (CO) -------
VOLATILE ORGANIC COMPOUNDS (VOC) EPA 0.177 0.776 0.177 0.776 0.177 0.776
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
SOURCE OF EXPECTED ACTUAL POTENTIAL EMSSIONS
EMISSION (AFTER CONTROLS I LIMITS) (BEFORE CONTROLS/ LIMITS) (AFTER CONTROLS/ LIMITS)
HAZARDOUS AJR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr
Hexane 110-54-3 Mass Balance 0.010 0.044 0.010 0.044 0.010 0.044
TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE
INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS
TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr lb/day lb/yr
Hexane 110-54-3 Mass Balance 0.010 0.241 88.0
Attachments: (1) emissions calculations and supporting documentation; (2) indicate all requested state and federal enforceable permit limits (e.g. hours of operation, emission rates) and describe how these are monitored and with what frequency; and (3) describe any monitoring devices, gauges, or test ports for this source.
COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE 81 THROUGH 89 FORM FOR EACH SOURCE
Attach Additional Sheets As Necessary
Page F-285
Attachment F. Air Quality Permit Application Review Documents
FORM D1
FACILITY-WIDE EMISSIONS SUMMARY
REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION· FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS/
LIMITATIONS) LIMITATIONS)
AIR POLLUTANT EMITTED tons/yr tons/yr
PARTICULATE MATTER (PM) 18.3 18.3
PARTICULATE MATTER< 10 MICRONS (PM,0) 18.3 18.3
PARTICULATE MATTER< 2.5 MICRONS (PM25) 18.3 18.3
SULFUR DIOXIDE (SO2) 3.10 3.10
NITROGEN OXIDES (NOx) 19.2 47.5
CARBON MONOXIDE (CO) 31.0 84.9
VOLATILE ORGANIC COMPOUNDS (VOC) 21.7 23.1
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION· FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS
(AFTER CONTROLS / (BEFORE CONTROLS/
LIMITATIONS) LIMITATIONS)
HAZARDOUS AIR POLLUTANT EMITTED CAS NO. tons/yr tons/yr
1, 1,2,2-Tetrachloroethane 79-34-5 1.66E-05 1.66E-05
1, 1,2-Tnchloroethane 79-00-5 1.32E-05 1.32E-05
1, 1-Dich loroethane 75-34-3 9.78E-06 9.78E-06
1,2-0ichloroethane 107-06-2 1.06E-05 1.06E-05
1,2-Dichloropropane 78-87-5 1.12E-05 1.12E-05
1,3-Butadiene 106-99-0 3.69E-04 5.33E-04
1,3-Dichloropropene 542-75-6 1.10E-05 1.10E-05
2,2,4-Tnmethylpentane 540-84-1 2.12E-04 2.12E-04
Acetaldehyde 106-99-0 0.017 0.032
Acrolein 75-07-0 0.004 0.007
Benzene 71-43-2 0.005 0.010
Biphenyl 92-52-4 9.88E-07 9.88E-07
Carbon Tetrachlonde 56-23-5 1.52E-05 1.52E-05
TOXIC AIR POLLUTANT EMISSIONS INFORMATION· FACILITY-WIDE
01
POTENTIAL EMISSIONS
(AFTER CONTROLS/
LIMITATIONS)
tons/yr
18.3
18.3
18.3
3.10
19.2
31.0
21.7
POTENTIAL EMISSIONS
(AFTER CONTROLS /
LIMITATIONS)
tons/yr
1.66E-05
1.32E-05
9.78E-06
1.06E-05
1.12E-05
3.69E-04
1.10E-05
2.12E-04
0.017
0.004
0.005
9.88E-07
1.52E-05
INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS/ LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RA TE (TPER) IN 15A NCAC
20 .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY.
Modeling Required ? Note
TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No 1
1, 1 ,2,2-Tetrachloroethane 79-34-5 3.32E-04 0.008 0.033 X 1
1,2-Dichloroethane 107-06-2 1.97E-04 0.005 0.021 X 1
1,3-Butadiene 106-99-0 0.004 0.099 0.739 X 1
Acetaldehyde 75-07-0 0.042 1.02 34.4 X 1
Acrolein 75-07-0 0.039 0.948 8.78 X 1
Ammonia 7664-41-7 2.83 67.9 24,773 X 1
Benzene 71-43-2 0.011 0.258 10.2 X 1
Benzo(a)pyrene 50-32-8 2.84E-08 6.82E-07 2.84E-06 X 1
Carbon Tet rachlonde 56-23-5 5.62E-04 0.013 0.030 X 1
Chlorobenzene 108-90-7 2.22E-04 0.005 0.022 X 1
Chloroform 67-66-3 2.36E-04 0.006 0.024 X 1
Dichlorobenzene 106-46-7 6.18E-06 1.48E-04 0.054 X 1
Ethylene Dib romide 106-93-4 6.79E-04 0.016 0.037 X 1
Formaldehyde 50-00-0 0.528 12.7 2,229 X 1
Hexane (or n-Hexane) 110-54-3 0.264 6.3 2,289 X 1
COMMENTS:
Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A NCAC
02Q.D7D2(a)(25), as the aggregate allowable natural gas heat Input value for these sources Is less than 450 MM Btu/hr, and they will be the only source of benzene
at the facility.
Page F-286
Attachment F. Air Quality Permit Application Review Documents
FORM D1
FACILITY-WIDE EMISSIONS SUMMARY
REVISED 12/01/01 NCDENR/Dlvlslon of Air Quality -Application for Air Permit to Construct/Operate
CRITERIA AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS
{AFTER CONTROLS / (BEFORE CONTROLS /
LIMITATIONS) LIMITATIONS)
AIR POLLUTANT EMITTED tons/yr tons/yr
PARTICULATE MATTER (PM)
PARTICULATE MATTER< 10 MICRONS (PM10)
PARTICULATE MATTER< 2.5 MICRONS (PM2 5)
SULFUR DIOXIDE (SO2)
D1
POTENTIAL EMISSIONS
(AFTER CONTROLS /
LIMITATIONS)
tons/yr
NITROGEN OXIDES (NOx) See Form D1, Page 1, for criteria pollutant totals.
CARBON MONOXIDE (CO)
VOLATILE ORGANIC COMPOUNDS (VOC)
LEAD
OTHER
HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS
{AFTER CONTROLS / (BEFORE CONTROLS / {AFTER CONTROLS I
LIMITATIONS) LIMITATIONS) LIMITATIONS)
HAZARDOUS AIR POLLUTANT EMITTED CAS NO. tons/yr tons/yr tons/yr
Chlorobenzene 108-90-7 1.11E-05 1.11E-05 1.11E-05
Chloroform 67-66-3 1.18E-05 1.18E-05 1.18E-05
Dichlorobenzene 106-46-7 2.71E-05 2.71E-05 2.71E-05
Ethylbenzene 100-41-4 0.012 0.024 0.012
Ethylene Dibromide 106-93-4 1.84E-05 1.84E-05 1.84E-05
Formaldehyde 75-07-0 1.11 2.21 1.11
Hexane (or n-Hexane) 110-54-3 1.14 1.14 1.14
Methanol 67-56-1 6.21E-04 6.21E-04 6.21E-04
Methylene Chloride 75-09-2 3.68E-05 3.68E-05 3.68E-05
Napthalene 91-20-3 5.34E-04 0.001 5.34E-04
PAH 8.73E-04 0.002 8.73E-04
Phenol 108-95-2 1.05E-05 1.05E-05 1.05E-05
Propylene oxide 75-56-9 0.011 0.022 0.011
Styrene 100-42-5 1.37E-05 1.37E-05 1.37E-05
Toluene 108-88-3 0.050 0.100 0.050
TOXIC AIR POLLUTANT EMISSIONS INFORMATION -FACILITY-WIDE
INDICATE REQUESTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS. EMISSIONS ABOVE THE TOXIC PERMIT EMISSION RATE {TPER) IN 15A
NCAC 2Q .0711 MAY REQUIRE AIR DISPERSION MODELING. USE NETTING FORM D2 IF NECESSARY.
Modeling Required ? Note
TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No 1
Methylene Chloride 75-09-2 7.36E-04 0.018 0.074 X 1
Phenol 108-95-2 2.11E-04 0.005 0.021 X 1
Styrene 100-42-5 2.74E-04 0.007 0.027 X 1
Toluene 108-88-3 0.016 0.388 99.8 X 1
Vinyl Chloride 75-01-4 1.24E-04 0.003 0.012 X 1
Xylene 1330-20-7 0.007 0.166 49.0 X 1
COMMENTS:
Note 1: The combustion sources proposed for the Northampton Compressor Station are exempt from NC DENR Air Toxics permitting requirements per 15A
NCAC 02Q.0702(a)(25), as the aggregate allowable natural gas heat input value for these sources Is less than 450 MM Btu/hr, and they wlll be the only source
of benzene at the facility.
Page F-287
Attachment F. Air Quality Permit Application Review Documents
Table C-7 Potential Emissio1rs From F11giti1•e Leaks
ACP Compressor Statio11 3 -Nort/,ampto11 Co1111ty, Nort/1 Caroli11a
Fugitive Emissions (RJG}
Saun·L' Dl."!>1�nat10n. FUC-tl2
Opn•Uo,wl P•r�metnc
[ Ann�I Hnut> ui 0,....'f'llllun (hr/_,vr) "�
PIP!linl' N.ahm1l G.u Fuglllu £mi•lon•
e.n!Mlon f,1dorl11 SovceCeur#' Tot.al HC Pottttwl £miuio• £.,.1,,.. .. 5-k• kg/1,q',outte ll,/lot
V11'1,l0, C..s -ISUE-m ..,. n.-11
Pump5'-ul> G.,, 241IE-OJ 11.IXlU
OlhL-n (l umpn."!l!>Or.. unJ uthcn,) c.,, tUiOE-0.1 ' 11.toH
Conrw,1on c... !.t'IOE-CI-I 1 -'i.-UE-(14
Fl.11n1;l."!I c.,, J'JUE-ll-l "lll tl.�2
01''",..,nJ,.,Jlinc> c •• :?.fl.IE-OJ lllXM
Tol..ll o7n
1 fJ'A Prnl,1tul fur l-.lju1pmcnl l.c.i� t:m�,.K>ll5 b.linwlt• (l-.l'A45VR-IJ5-tll7) T.ahl,_, 2--i. (1il dnJ C..i,. l'mJo,11.1i.in llp,.•r.alKlfl� l·mMJ•in t.i,h•r..
2 Cumpono.•nt ,uonl �,J ,in H.J>11. ',y:r,tcrm l-.n1�tlll"l'rll'J� bJim.ilt•
....... ,rt..c.,1,,,,..,.,,,.
l'uknlwl f.miw.i,,IO!> (lh/hr) • F.mt>'>Kln f .. 1.,, (LtVhr/,..,ur.t.') '�,uru:C,,um' (?.21\.ln:? lh/1 lrJ
l\>1entldl f.mn&ilon!o (1110�/yr) • (lh/hi)f'w_,.,. • Hl,ur., 1,(ll11t·f.ilil•n flu/yr)• (I tm/l.1111 lh)
lpJ
2"1
IHXXI
tl.255
tUlU2
1.2"
0.0.)1.)
?'lo
VOCWeigllt voc&daae .. CO,Wdghl co,-... Ol4 Weipl CU.EaboloM IIAPWdgbt HAPe.tulan11
Fnmoa &Mlloa Fr•ctl .. PrMdoa lpJ ,,, lpJ lpJ
"1126 tl.7ln O.l1Z7 ll7nl 01!'15 251 1,-1116-W 0.tl-12
0.021, IH'lfltl 0.027 o.mo D.1!95 0.IXXJ \.-&8&03 0.fl)I.)
D.ll'.l6 o.n)7 U027 tll"U7 .. .., ll.:?1K 1.-&8E-lD lnE-04
o.1126 StlnE-10 11027 5.2�E-C6 01!'15 11.t).)2 1 .... &"3 :?.Nh�ln
11026 11.tl� 0.027 IUl.15 0.895 115 1,..SE,03 11.lll.12
O.IT.!t, u.mo ll021 11.tXXI ·o.lf'IS tl.lXIO 1,.JttE-tD IHXXI
071n ll.Mll:1 211.5 ll.ll-U
Page F-288
Attachment F. Air Quality Permit Application Review Documents
Table C-9 Proiect Pote11tial E111issio11s
ACP Compressor Statio11 3 -Nortlta111pto11 Co1111hJ, Nortlt Caroli11a
Criteria Pollutants (to, GHG Emissions (to, Ammonia ltpvl HAP ltnv•
Combustion Sourcas ID NOx co voe 502 PMF PMF-10 PMF-2.5 PMC CO2 CH4 N20 CO2e NM.> Total HAP
Solar Taurus 70 Turbine CT-01 8.35 13.1 0.775 1.43 2.42 2.42 2.42 5.99 50,035 4.00 1.26 50,511 5.77 0.525
Solar Centaur SOL Turbine CT-02 5.20 8.19 0.477 0.894 1.51 1.51 1.51 3.74 31,329 2.50 0.788 31,627 3.58 0.352
Solar Centaur 40 Turbine CT-03 4.44 7.29 0.405 0.760 1.29 1.29 1.29 3.18 26,747 2.14 0.671 27,000 3.02 0.286
Caterpillar G3516B Egan EG-01 0.100 0.499 0.108 3.88E-04 0.025 0.025 0.025 0.007 101 0.859 0 122 0 0.018
Generac SG100 Egan EG-02 4.92E-05 0.001 0.003 3.18E-05 0.002 0.002 0.002 0.001 759 0.015 0 759 0 0.002
Boller WH-01 1.13 1.89 0.124 0.014 0.043 0.043 0.043 0.129 2,705 0.052 0.050 2,721 0 0.043
Fugitive Leaks -Blowdowns FUG-01 -. 18.8 -. . --19.5 643 16,092 . 1.06
Fugitive Leaks· Piping FUG-02 --0.776 -----0.803 26.5 -663 -0.044
Pipeline LIQuids Tank TK-1 -. 0.145 -----------
Hvdrocarbon !Waste 0111 Tank TK-2 --2 19E-05 ------. ----
Total (tons/yr) 19.2 31.0 21.7 3.10 5.29 5.29 5.29 13.1 111,697 679 2.77 129,495 12.4 2.33
Page F-289
Attachment F. Air Quality Permit Application Review Documents

Attachment G – Notice of Public Hearing

PUBLIC NOTICE
N.C. DEPARTMENT OF ENVIRONMENTAL QUALITY, DIVISION OF AIR QUALITY INTENT
TO ISSUE AIR QUALITY PERMIT #10466R00 for the Northampton Compressor Station Facility ID
6600169.
Public comment on the draft permit is invited. All comments received no later than Nov. 20, 2017 will
be considered in the final determination regarding permit issuance and permit conditions.
PERMIT APPLICATION
Associated with the Atlantic Coast Pipeline LLC’s proposed pipeline project, Northampton Compressor
Station, 707 E. Main Street, Richmond, Va. 23219, has applied for a permit to construct and operate a
new compressor station at 718 Forest Rd., Pleasant Hill, N.C. in Northampton County (Northampton
County GIS parcel number 0500230).
The draft permit, application and related documents are available online at:
https://deq.nc.gov/about/divisions/energy-mineral-land-resources/acp. Printed copies of these documents
may be reviewed at the department’s Raleigh Regional Office. To obtain additional information or make
an appointment to review documents at the Raleigh Regional Office, please contact Charles McEachern
at 919-791-4200.
Public comments on the draft permit should be mailed to: Division of Air Quality, Attn: Charles
McEachern, 3800 Barrett Dr., Raleigh, N.C., 27609. Public comments may also be submitted by email
to: [e-mail]. Please be sure to include “ACP/DAQ” in the email’s subject line.
PUBLIC HEARING
The N.C. Department of Environmental Quality will hold a public hearing on the draft permit at 6 p.m.
Wed., Nov. 15 at Garysburg Town Hall, 504 Old Highway Rd., Garysburg, N.C. 27831. Registration for
those who wish to speak will begin at 5 p.m.
Page G-2
Attachment G. Public Notice Documents