files.nc.gov Quality/permits/psd/docs... · 2018-06-19 · REVISED 12/01/01 A2 U6 Unit 6 Boiler...

REVISED 12/01/01 A2

U6 Unit 6 Boiler CD19-22 SCR, dry ESP, wet FGD, and WESPU7 Unit 7 Boiler CD23-26 SCR, dry ESP, wet FGD, and WESPAux Auxiliary Boiler NACT1 & CT2 Cooling Towers (2) NAC19 Unit 6 & 7 Coal Reclaim HoppersC20-23 Coal Reclaim ConveyorsC24-C26 Unit 6 & 7 Crusher House and Reclaim Conveyors CD27 BaghouseC27-30 Unit 6 Boilerhouse Coal Handling CD28 BaghouseC31-34 Unit 7 Boilerhouse Coal Handling CD29 BaghouseA1-A6 Ash Handling Point Source Unit 6 CD30 BaghouseA8-A11, & A13 Ash Handling Point Source Unit 7 CD31, 33 BaghouseA7, A12, A14 Ash Handling Fugitive Source Units 6 & 7 NAVF1 - VF32 Coal Reclaim FeedersLSBM3 Limestone Ball Mill Train No. 3LS13-3 Limestone Silo No. 3 CD32-3 Bin Vent Filter (on silo)LS15 Limeston Reclaim ConveyorGS10 Gypsum - Belt Filter

FVehicle Fugitive Vehicle EmissionsC1 Coal UnloadingC2, C4, C6, C8 Coal Handling ConveyorsC3, C5, C7, C9 Coal Stacking TubesC13 Coal Handling - Reclaim ConveyorsGS3, GS4 Gypsum Handling - Stockout Conveyor and Radial StackerGS7, GS9 Gypsum Truck LoadingG8 Gypsum Rail Car LoadingLS1 Limestone Rail Car UnloadingLS2, LS3 Limestone Stockout Conveyor and Transfer House (existing)LS6, LS7 Limestone Stockout Conveyor and Radial StackerFLandfill Landfill Activities - Active Cell

U1 Unit 1 Boiler CD1 ESPU2 Unit 2 Boiler CD2 ESPU3 Unit 3 Boiler CD3 ESPU4 Unit 4 Boiler CD4 ESP

Is your facility subject to 40 CFR Part 68 "Prevention of Accidental Releases" - Section 112(r) of the Federal Clean Air Act? Yes / NoIf No, please specify in detail how your facility avoided applicability:

If your facility is Subject to 112(r), please complete the following: A. Have you already submitted a Risk Management Plan (RMP) to EPA Pursuant to 40 CFR Part 68.10 or Part 68.150?

Yes No Specify required RMP submittal date: _____________ If submitted, RMP submittal date: _ 6/8/2004 B. Are you using administrative controls to subject your facility to a lesser 112(r) program standard?

Yes No If yes, please specify:

Facility Name: Duke Cliffside Steam StationMailing Address Line 573 Duke Power Road Mailing Address Line 2:City: Cliffside State: NC Zip Code: 28114 County: Rutherford & ClevelandPhone No. (828) 657-2339 Fax No. (828) 657-2060 Email Address:

SO2 51,742,000 35,130,000 C19-U5 WFGDSO2 10,918,000 C19-U1-4 RetireNOx 2,816,000 C19-U1-4 RetirePM 698,000 C19-U1-4 RetireCO 130,000 C19-U1-4 Retire

Attach Additional Sheets As Necessary

For assistance with Section A4, please contact the North Carolina Division of Pollution Prevention and Environmental Assistance at 1-800-763-0136 or [email protected]

112(r) APPLICABILITY INFORMATION

SURVEY OF FACILITY REDUCTION & RECYCLING ACTIVITIES

Planned Source ReductionActivities (Enter Code)Activities (Enter Code) Reduction (lb/yr) Reduction (lb/yr)

Pollutant Ongoing Source Reduction Qty. Emitted Before Qty. Emitted After

Equipment To Be ADDED By This Application (New, Previously Unpermitted, or Replacement)

Existing Permitted Equipment To Be MODIFIED By This Application

Equipment To Be DELETED By This Application

ID NO. DESCRIPTION ID NO. DESCRIPTIONEMISSION SOURCE EMISSION SOURCE CONTROL DEVICE CONTROL DEVICE

FORMs A2, A3, A4

SURVEY OF FACILITY REDUCTION & RECYCLING ACTIVITIES - A4 NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate

EMISSION SOURCE LISTING: New, Modified, Previously Unpermitted, Replaced, Deleted

EMISSION SOURCE LISTING FOR THIS APPLICATION - A2112r APPLICABILITY INFORMATION - A3

A 3

A 4

REVISED 12/01/01 BEMISSION SOURCE ID NO: U6CONTROL DEVICE ID NO(S): CD 19-22EMISSION POINT (STACK) ID NO(S): EP-U6

DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):

X Coal,wood,oil, gas, other burner (Form B1) Woodworking (Form B4) Manufact. of chemicals/coatings/inks (Form B7)

Int.combustion engine/generator (Form B2) Coating/finishing/printing (Form B5) Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) Other (Form B9)

START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: TBDIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Da, HHHH NESHAP (SUBPART?):________ MACT (SUBPART?):__________

EXPECTED ANNUAL HOURS OF OPERATIO 8760

SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) Vendor 117.8 515.7 2 2 117.8 515.7PARTICULATE MATTER<10 MICRONS (PM10) Vendor 188.4 825.2 2 2 188.4 825.2PARTICULATE MATTER<2.5 MICRONS (PM2.5) NA NA NA NA NA NASULFUR DIOXIDE (SO2) Vendor 1178 5157.5 2 2 1178 5157.5NITROGEN OXIDES (NOx) Vendor 628 2750.6 2 2 628 2750.6CARBON MONOXIDE (CO) Vendor 1177.5 5157.5 2 2 1177.5 5157.5VOLATILE ORGANIC COMPOUNDS (VOC) Vendor 31.4 137.5 2 2 31.4 137.5

Vendor 0.2 0.8 2 2 0.2 0.8OTHER

SOURCE OFEMISSION

HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrHydrogen Chloride Mass Balance 6.53E+01 1.72E+02 - - 6.53E+01 1.72E+02Hydrogen Fluoride Mass Balance 1.16E+01 2.24E+01 - - 1.16E+01 2.24E+01Antimony AP-42 7.54E-03 3.30E-02 - - 7.54E-03 3.30E-02Arsenic AP-42 1.72E-01 7.52E-01 - - 1.72E-01 7.52E-01Beryllium AP-42 8.79E-03 3.85E-02 - - 8.79E-03 3.85E-02Cadmium AP-42 2.13E-02 9.35E-02 - - 2.13E-02 9.35E-02Chromium AP-42 1.09E-01 4.77E-01 - - 1.09E-01 4.77E-01Cobalt AP-42 4.19E-02 1.83E-01 - - 4.19E-02 1.83E-01Lead AP-42 1.76E-01 7.70E-01 - - 1.76E-01 7.70E-01Manganese AP-42 2.05E-01 8.98E-01 - - 2.05E-01 8.98E-01Mercury 1 NSPS Da 3.36E-02 1.47E-01 - - 3.36E-02 1.47E-01Nickel AP-42 1.17E-01 5.13E-01 - - 1.17E-01 5.13E-01Selenium AP-42 5.44E-01 2.38E+00 - - 5.44E-01 2.38E+00Acetaldehyde AP-42 2.39E-01 1.05E+00 - - 2.39E-01 1.05E+00Acetophenone AP-42 6.28E-03 2.75E-02 - - 6.28E-03 2.75E-02Acrolein AP-42 1.21E-01 5.32E-01 - - 1.21E-01 5.32E-01Anthracene AP-42 8.79E-05 3.85E-04 - - 8.79E-05 3.85E-04Benzene AP-42 5.44E-01 2.38E+00 - - 5.44E-01 2.38E+00Benzo(g,h,i)perylene AP-42 1.13E-05 4.95E-05 - - 1.13E-05 4.95E-05Benzyl Chloride AP-42 2.93E-01 1.28E+00 - - 2.93E-01 1.28E+00Biphenyl AP-42 7.12E-04 3.12E-03 - - 7.12E-04 3.12E-03Bis(2-ethylhexyl)phthalate AP-42 3.06E-02 1.34E-01 - - 3.06E-02 1.34E-01Bromoform AP-42 1.63E-02 7.15E-02 - - 1.63E-02 7.15E-02Carbon Disulfide AP-42 5.44E-02 2.38E-01 - - 5.44E-02 2.38E-012-Chloroacetophenone AP-42 2.93E-03 1.28E-02 - - 2.93E-03 1.28E-02Chlorobenzene AP-42 9.21E-03 4.03E-02 - - 9.21E-03 4.03E-02Chloroform AP-42 2.47E-02 1.08E-01 - - 2.47E-02 1.08E-01Cumene AP-42 2.22E-03 9.72E-03 - - 2.22E-03 9.72E-03Cyanide AP-42 1.05E+00 4.58E+00 - - 1.05E+00 4.58E+00

EXPECTED OP. SCHEDULE: _24__ HR/DAY __7_ DAY/WK _52__ WK/YR

VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: _<20___ % OPACITYPERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25

FORM BSPECIFIC EMISSIONS SOURCE INFORMATION (REQUIRED FOR ALL SOURCES)

NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate

TYPE OF EMISSION SOURCE (CHECK AND COMPLETE APPROPRIATE FORM B1-B9 ON THE FOLLOWING PAGES):

EMISSION SOURCE DESCRIPTION: Unit 6 Boiler

Nominal 800 MW pulverized coal (PC) boiler fired with bituminous coal or a blend of bituminous and sub-bituminous coals. The boiler will be equipped with the following control devices to reduce air emissions during normal operations: low NOx burners, SCR, dry ESP, wet FGD, and WESP. See Appendix G for process diagram.

OPERATING SCENARIO ______1___________OF ________1__________

CRITERIA AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE

(BEFORE CONTROLS / LIMITS)

POTENTIAL EMSSIONSEXPECTED ACTUAL(AFTER CONTROLS / LIMITS) (AFTER CONTROLS / LIMITS)

HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE

(AFTER CONTROLS / LIMITS)

LEAD

EXPECTED ACTUAL POTENTIAL EMSSIONS(BEFORE CONTROLS / LIMITS) (AFTER CONTROLS / LIMITS)

2,4-Dinitrotoluene AP-42 1.17E-04 5.13E-04 - - 1.17E-04 5.13E-04Dimethyl Sulfate AP-42 2.01E-02 8.80E-02 - - 2.01E-02 8.80E-02Ethyl benzene AP-42 3.94E-02 1.72E-01 - - 3.94E-02 1.72E-01Ethyl Chloride (Chloroethane) AP-42 1.76E-02 7.70E-02 - - 1.76E-02 7.70E-02Ethylene Dichloride AP-42 1.67E-02 7.33E-02 - - 1.67E-02 7.33E-02Ethylene Dibromide AP-42 5.02E-04 2.20E-03 - - 5.02E-04 2.20E-03Formaldehyde AP-42 1.00E-01 4.40E-01 - - 1.00E-01 4.40E-01Hexane AP-42 2.80E-02 1.23E-01 - - 2.80E-02 1.23E-01Isophorone AP-42 2.43E-01 1.06E+00 - - 2.43E-01 1.06E+00Methyl Bromide (Bromomethane) AP-42 6.70E-02 2.93E-01 - - 6.70E-02 2.93E-01Methyl Chloride (Chloromethane) AP-42 2.22E-01 9.72E-01 - - 2.22E-01 9.72E-01Methyl Ethyl Ketone AP-42 1.63E-01 7.15E-01 - - 1.63E-01 7.15E-01Methyl Hydrazine AP-42 7.12E-02 3.12E-01 - - 7.12E-02 3.12E-01Methyl Methacrylate AP-42 8.37E-03 3.67E-02 - - 8.37E-03 3.67E-02Methyl tert-butyl ether AP-42 1.47E-02 6.42E-02 - - 1.47E-02 6.42E-02Methylene Chloride AP-42 1.21E-01 5.32E-01 - - 1.21E-01 5.32E-01Naphthalene AP-42 5.44E-03 2.38E-02 - - 5.44E-03 2.38E-02Phenanthrene AP-42 1.13E-03 4.95E-03 - - 1.13E-03 4.95E-03Phenol AP-42 6.70E-03 2.93E-02 - - 6.70E-03 2.93E-02Propionaldehyde AP-42 1.59E-01 6.97E-01 - - 1.59E-01 6.97E-01Styrene AP-42 1.05E-02 4.58E-02 - - 1.05E-02 4.58E-02Tetrachloroethylene AP-42 1.80E-02 7.88E-02 - - 1.80E-02 7.88E-02Toluene AP-42 1.00E-01 4.40E-01 - - 1.00E-01 4.40E-011,1,1-Trichloroethane AP-42 8.37E-03 3.67E-02 - - 8.37E-03 3.67E-02Vinyl Acetate AP-42 3.18E-03 1.39E-02 - - 3.18E-03 1.39E-02Xylene AP-42 1.55E-02 6.78E-02 - - 1.55E-02 6.78E-02Total PCDD/PCDF AP-42 7.37E-07 3.23E-06 - - 7.37E-07 3.23E-06

TOXIC AIR POLLUTANT AND CAS NO. EF SOURCEHydrogen Chloride Mass Balance 65.29 1566.85 571898.56Hydrogen Fluoride Mass Balance 11.63 279.20 101907.58Arsenic AP-42 0.17 4.12 1503.52Beryllium AP-42 0.01 0.21 77.01Cadmium AP-42 0.02 0.51 187.02Chromium AP-42 0.11 2.61 953.45Manganese AP-42 0.21 4.92 1796.89Mercury AP-42 0.03 0.81 294.34Nickel AP-42 0.12 2.81 1026.80Acetaldehyde AP-42 0.24 5.73 2090.26Acrolein AP-42 0.12 2.91 1063.47Benzene AP-42 0.54 13.06 4767.27Benzyl Chloride AP-42 0.29 7.03 2566.99Carbon Disulfide AP-42 0.05 1.31 476.73Chlorobenzene AP-42 0.01 0.22 80.68Chloroform AP-42 0.02 0.59 216.36Ethylene Dichloride AP-42 0.02 0.40 146.69Ethylene Dibromide AP-42 0.00 0.01 4.40Formaldehyde AP-42 0.10 2.41 880.11Hexane AP-42 0.03 0.67 245.70Methyl Ethyl Ketone AP-42 0.16 3.92 1430.18Methylene Chloride AP-42 0.22 5.32 1943.58Phenol AP-42 0.01 0.16 58.67Styrene AP-42 0.01 0.25 91.68Toluene AP-42 0.10 2.41 880.11Xylene AP-42 0.02 0.37 135.68Sulfuric Acid Vendor 47.10 1130.40 412596.00Ammonia Vendor 31.40 753.60 275064.00

1 Calculated based on NSPS Subpart Da, Sub-bituminous units w/ wet FGD - see emission calculation notes2 Emissions provided are based on preliminary design. Information based on final design will be provided to NC DAQ.

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.

lb/dayINDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONS

lb/yr

TOXIC AIR POLLUTANT EMISSIONS INFORMATION FOR THIS SOURCE

lb/hr

REVISED 12/01/01 B1EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: U6

CONTROL DEVICE ID NO(S): CD 19-22

OPERATING SCENARIO: ______1________ OF ______1________ EMISSION POINT (STACK) ID NO(S): EP-U6

DESCRIBE USE: PROCESS HEAT SPACE HEAT X ELECTRICAL GENERATION

CONTINUOUS US STAND BY/EMERGENCY OTHER (DESCRIBE): _________

HEATING MECHANISM: X INDIRECT DIRECT

MAX. FIRING RATE (MMBTU/HOUR): 7850

BARK WOOD/BARK WET WOOD DRY WOOD OTHER (DESCRIBE): __________

PERCENT MOISTURE OF FUEL:_________________

UNCONTROLLED CONTROLLED WITH FLYASH REINJECTION CONTROLLED W/O REINJECTION

FUEL FEED METHOD: HEAT TRANSFER MEDIA: STEAM AIR OTHER

METHOD OF TUBE CLEANING: CLEANING SCHEDULE:

TYPE OF BOILER IF OTHER DESCRIBE:

PULVERIZED

WET BED UNCONTROLLED UNCONTROLLED UNCONTROLLED CIRCULATING

X DRY BED CONTROLLED CONTROLLED FLYASH REINJECTION RECIRCULATING

NO FLYASH REINJECTION

METHOD OF LOADING: CYCLONE HANDFIRED TRAVELING GRATE X OTHER (DESCRIBE): Supercritical PC Unit

METHOD OF TUBE CLEANING: TBD CLEANING SCHEDULE: As needed

TYPE OF BOILER: UTILITY INDUSTRIAL COMMERCIAL RESIDENTIAL

TYPE OF FIRING: NORMAL TANGENTIAL LOW NOX BURNERS NO LOW NOX BURNER


TYPE OF FUEL: ____________________________ PERCENT MOISTURE: _____________ TYPE OF BOILER: UTILITY INDUSTRIAL COMMERCIAL RESIDENTIAL

TYPE OF FIRING: _______________ TYPE OF CONTROL (IF ANY): ___________________________ FUEL FEED METHOD: ________


No. 2 Fuel Oil (Start-up) mmBTU 2747.5 NA

Coal mmBTU 7850 NA

No. 2 Fuel Oil (Start-up) 137000 BTU/gal 0.05 NA

Coal 9376 BTU/lb 3 11.29

COMMENTS:

SAMPLING PORTS, COMPLIANT WITH EPA METHOD 1 WILL BE INSTALLED ON THE STACKS: X YES NO


ASH CONTENT

(% BY WEIGHT)

SULFUR CONTENT

FUEL TYPE

SPECIFIC

BTU CONTENT (% BY WEIGHT)

Fuel oil will be combusted along with coal for start-up, up to 35% of maximum capacity, where the fuel will be switched to coal. Fuel oil may also be used when the pulverizer is brought into service. Coal will be a blend from various regions and coal specs. given ore conservative.

LIMITATION (UNIT/HR)

FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE)

MAXIMUM DESIGN

CAPACITY (UNIT/HR)

REQUESTED CAPACITY

FUEL TYPE UNITS

COAL-FIRED BURNER

OIL/GAS-FIRED BURNER

WOOD TYPE:

FORM B1EMISSION SOURCE (WOOD, COAL, OIL, GAS, OTHER FUEL-FIRED BURNER)


WOOD-FIRED BURNER

Nominal 800 MW pulverized coal (PC) boiler fired with bituminous coal or a blend of bituminous and sub-bituminous coals. Boiler is controlled by SCR system, a dry electrostatic precipitator (ESP), a wet-flue gas desulfurization unit, and a wet ESP.

FUEL USAGE (INCLUDE STARTUP/BACKUP FUELS)

SPREADER STOKER FLUIDIZED BEDOVERFEED STOKER UNDERFEED STOKER

OTHER FUEL-FIRED BURNER

REVISED 12/01/01

CONTROL DEVICE ID NO: CD19 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S)U6

EMISSION POINT (STACK) ID NO(S) EP-U6 POSITION IN SERIES OF CONTROLS NO. 1 OF 4 UNITS

MANUFACTURER: TBD MODEL NO: TBD

MANUFACTURE DATE: TBD PROPOSED OPERATION DATE: 2011

PROPOSED CONSTRUCTION DATE: 2007

TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION

CATALYTIC OXIDATIONEXPECTED LIFE OF CATALYST (YRS): METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT:CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL

SULFUR COMPOUND OTHER_________________ NONE

TYPE OF CATALYST: Vanadium pentoxide CATALYST VOL (FT3): TBD VELOCITY THROUGH CATALYST (FPS): TDB

SCFM THROUGH CATALYST:

DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM:

POLLUTANT(S) COLLECTED: NOx

BEFORE CONTROL EMISSION RATE (LB/HR): 2355 lb/hr(to SCR; 0.30 lb/mmbtu)

CAPTURE EFFICIENCY: % % % %

CONTROL DEVICE EFFICIENCY: % % % %

OVERALL SYSTEM EFFICIENCY: % % % %

EFFICIENCY DETERMINATION CODE:

TOTAL EMISSION RATE (LB/HR) : 628 lb/hr (after SCR; 0.08 lb/mmbtu)

PRESSURE DROP (IN. H2O OUTLET TEMPERATURE (oF):

INLET TEMPERATURE (oF RESIDENCE TIME (SECONDS):

INLET AIR FLOW RATE (ACFM):4,500,000 to SCR COMBUSTION TEMPERATURE (oF):

COMBUSTION CHAMBER VOLUME (FT3): INLET MOISTURE CONTENT (%):

% EXCESS AIR: CONCENTRATION (ppmv) ______INLET ______OUTLET

AUXILIARY FUEL USED: No. 2 Fuel Oil TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): 7850 lb/mmbtu

MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS:

ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: 418.6 UNITS: ton/hr design coal

DESCRIBE METHOD USED TO INCREASE MIXING:

DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE:

DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES:

STACK TESTING PORTS: NO YES (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):See Appendix G

FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC)

NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate C3AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA.

OPERATING SCENARIO:

_____1__ OF __1_____

NOx emissions from the boiler will be controlled using a combination of low-NOx burners, over-fire air and a selective catalytic reduction (SCR) system. The combustion system applies air-staging in combination with low-NOx burners to minimize NOx formation in the furnace to minimze the amount of SCR catalyst required and reduce the consumption of reagent.

The Selective Catalytic Reduction (SCR) system catalytically reduces boiler flue gas nitrogen oxide (NOx) emissions to nitrogen and water using anydrous ammonia (NH3) as a reducing agent. Flue gas exiting the ecomonizer outlet flows through two flow paths prior to entering the ammonia / air injection zone. Each flue has a dedicated ammonia injection grid fed by a manifold valve station. Following the ammonia injection the gas enters the SCR reactor were the NOx reacts with the ammonia and is converted to nitrogen and water. The flue gas exiting the reactor is directed into the air heater.

MIN MAX AVE:4.3 across SCR MIN MAX 750 at SCR outlet


MIN 600 MAX 750 at econ. Outlet

The ammonia injection grid has multiple zones for injecting ammonia across the flue gas path. Each injection pipe has numerous injection orifices for optimim ammonia-flue gas mixing.

Steam coil air heaters are designed to preheat the combustion air during initial firing. Ammonia is injected once the catalst bed temperature has been elevated above the estimated minimum injection temperature of 600 F. Temp. to be confirmed by SCR supplier.

REVISED 12/01/01 C2CONTROL DEVICE ID NO: CD 20 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE U6

EMISSION POINT (STACK) ID NO(S)EP-U6 POSITION IN SERIES OF CONTROL NO. 2 OF 4 UNITS

MANUFACTURER: TBD MODEL NO. TBD


PROPOSED START CONSTRUCTION DATE: 2007

GAS DISTRIBUTION GRIDS: YES NO

TYPE: WET DRY SINGLE-STAGE TWO-STAGE

TOTAL COLLECTION PLATE AREA (FT2): 1,130,000 NO. FIELDS5 NO. COLLECTOR PLATE PER FIELD:

COLLECTOR PLATES SIZE (FT): LENGTH: 50 WIDTH: SPACING BETWEEN COLLECTOR PLATES (INCHES): 16

TOTAL DISCHARGE ELECTRODE LENGTH(FT): GAS VISCOSITY (POISE):

NUMBER OF DISCHARGE ELECTRODES: NUMBER OF COLLECTING ELECTRODE RAPPERS:

MAXIMUM INLET AIR FLOW RATE (ACFM): 3,000,000 ave. PARTICLE MIGRATION VELOCITY (FT/SEC):

MINIMUM GAS TREATMENT TIME (SEC): 15

FIELD STRENGTH (VOLTS) CHARGING: COLLECTING: CORONA POWER (WATTS/1000 CFM):

ELECTRICAL USAGE (kw/HOUR): 1400 kW

CLEANING PROCEDURES: RAPPING PLATE VIBRATING WASHING OTHER____________

PRESSURE DROP (IN. H20): MIN MAX AVE:.2 WARNING ALARM? YES NO

RESISTIVITY OF POLLUTANT (OHM-CM): GAS CONDITIONING: YES NO TYPE OF AGENT (IF YES):

INLET GAS TEMPERATURE (oF): MIN MAX AV 300 OUTLET GAS TEMPERATURE (oF): MIN MAX AVE: 298

VOLUME OF GAS HANDLED (ACFM 3,000,000 INLET MOISTURE PERCENT: MIN MAX

TBD TBD TBD TBD TBD

filterable PM10

BEFORE CONTROL EMISSION RATE (LB/HR):



CORRESPONDING OVERALL EFFICIENCY: 99.1 % % % %


TOTAL EMISSION RATE (LB/HR): 118 lb/hr (0.015 lb/mmbtu)

DESCRIBE STARTUP PROCEDURES:



DESCRIBE ANY MONITORING DEVICES, GAUGES, OR TEST PORTS AS ATTACHMENTS:

SIZE

POLLUTANT(S) COLLECTED:

POWER REQUIREMENTS

CUMULATIVE

10-25

PARTICLE SIZE DISTRIBUTION

IS AN ENERGY MANAGEMENT SYSTEM USED? YES NO

WEIGHT %

0-11-10

(MICRONS)

OPERATING PARAMETERS

EQUIPMENT SPECIFICATIONS

OPERATING SCENARIO:

BULK PARTICLE DENSITY (LB/FT3):

25-50


OF TOTAL

50-100

and indicate the electrode type), AND THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):

ATTACH A DIAGRAM OF THE TOP VIEW OF THE ESP WITH DIMENSIONS (include at a minimum the plate spacing and wire spacing

%

>100TOTAL = 100

FORM C2CONTROL DEVICE (Electrostatic Precipitator)

NO. OF SETS CHARGING EACH TRANSFORMER (kVA) EACH RECTIFIER Kv Ave/Peak Ma DcFIELD NO.


____1___ OF ___1___ P.E. SEAL REQUIRED (PER 2Q .0112)? YES NO

N

FORM C8CONTROL DEVICE (WET PARTICULATE SCRUBBER)

REVISED 12/01/01 NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate C8CONTROL DEVICE ID NO: CD21 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): U6

EMISSION POINT ID NO(S): EP-U6 POSITION IN SERIES OF CONTROLS: NO. 3 OF 4 UNITS


DATE MANUFACTURED: PROPOSED OPERATION DATE: 2011OPERATING SCENARIO: PROPOSED CONSTRUCTION DATE: 2007

_______ OF _______ P.E. SEAL NEEDED (PER 2Q .0112)? YES NO

DESCRIBE CONTROL SYSTEM:

The proposed flue gas desulfurization (FGD) system is a wet limestone, forced oxidation, system with a vertical, countercurrent, spray tower absorber. The flue gas enters the spray tower near the bottom through the absorber inlet nozzle. Once in the absorber, the hot flue gas is immediately quenched as it travels upward countercurrent to a continuous spray of process/recycle slurry produced by multiple spray banks. The recycle slurry extracts the sulfur dioxide from the flue gas and collects it in the bottom of the absorber where it is oxidized to calcium sulfate. The proposed system will treat 100% of the flue gas from the unit. The unit will be designed for 99% removal efficiency.

POLLUTANT(S) COLLECTED: SO2

BEFORE CONTROL EMISSION RATE (LB/HR): 39,238

CAPTURE EFFICIENCY: % % %

CONTROL DEVICE EFFICIENCY: % % %

CORRESPONDING EFFICIENCY: 99 % % %


TOTAL EMISSION RATE (LB/HR): 1178 lb/hr (0.15 lb/mmbtu - 30 day average)

PRESSURE DROP (IN. H20): MIN MAX AVE: 11 WARNING ALARM? YES NO

INLET TEMPERATURE (oF): MIN MAX AVE: 300 OUTLET TEMPERATURE (oF): MIN MAX AVE: 120

INLET AIR FLOW RATE (ACFM): 2,550,000 MOISTURE CONTENT : INLET % OUTLET %

THROAT VELOCITY (FT/SEC): THROAT TYPE: FIXED VARIABLE

TYPE OF SYSTEM: Wet Limestone, forced oxidation TYPE OF PACKING USED IF ANY: n/aADDITIVE LIQUID SCRUBBING MEDIUM: limestone slurry PERCENT RECIRCULATED:

MINIMUM LIQUID INJECTION RATE (GAL/MI 313 FLOW RATE GAUGE INSTALLED? YES NO

MAKE UP RATE (GAL/MIN): 1300 FOR ADDITIVE (GAL/MIN):DESCRIBE MAINTENANCE PROCEDURES: PARTICLE SIZE DISTRIBUTION

SIZE WEIGHT % CUMULATIVE(MICRONS) OF TOTAL %

0-1

DESCRIBE ANY MONITORING DEVICES, GAUGES, TEST PORTS, ETC: 1-1010-2525-50

50-100>100

TOTAL = 100

ATTACH A DIAGRAM OF THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):


REVISED 12/01/01 C2CONTROL DEVICE ID NO: Unit 6 Wet ESP CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE U6

EMISSION POINT (STACK) ID NO(S) EP-U6 POSITION IN SERIES OF CONTROL NO. 4 OF 4 UNITS






TOTAL COLLECTION PLATE AREA (FT2): 612,000 NO. FIELDS3 NO. COLLECTOR PLATE PER FIELD:

COLLECTOR PLATES SIZE (FT): LENGTH: 29.53 WIDTH: SPACING BETWEEN COLLECTOR PLATES (INCHES): 9.75




MINIMUM GAS TREATMENT TIME (SEC):


ELECTRICAL USAGE (kw/HOUR):




INLET GAS TEMPERATURE (oF): MIN MAX AVE: 128 OUTLET GAS TEMPERATURE (oF): MIN MAX AVE: 128


TBD TBD TBD TBD TBD

Total PM10 Filterable PM10 H2SO4




CORRESPONDING OVERALL EFFICIENCY: % % % %


TOTAL EMISSION RATE (LB/HR): 188 lb/hr(0.024lb/mmbtu) 117.8 lbhr(0.015 lb/mmbtu) 47.1 lb/hr (0.006lb/mmbtu)







OPERATING SCENARIO:

____1___ OF ___1___ P.E. SEAL REQUIRED (PER 2Q .0112)? YES NO




POWER REQUIREMENTS IS AN ENERGY MANAGEMENT SYSTEM USED? YES NO

FIELD NO. NO. OF SETS CHARGING EACH TRANSFORMER (kVA) EACH RECTIFIER Kv Ave/Peak Ma Dc




0-11-1010-2525-5050-100



>100TOTAL = 100


REVISED 12/01/01 BEMISSION SOURCE ID NO: U7CONTROL DEVICE ID NO(S): CD 23-26EMISSION POINT (STACK) ID NO(S): EP-U7




START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: TBDIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Da, HHHH NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) Vendor 117.8 515.7 2 2 117.8 515.7PARTICULATE MATTER<10 MICRONS (PM10) Vendor 188.4 825.2 2 2 188.4 825.2PARTICULATE MATTER<2.5 MICRONS (PM2.5) NA NA NA NA NA NASULFUR DIOXIDE (SO2) Vendor 1178 5157.5 2 2 1178 5157.5NITROGEN OXIDES (NOx) Vendor 628 2750.6 2 2 628 2750.6CARBON MONOXIDE (CO) Vendor 1177.5 5157.5 2 2 1177.5 5157.5VOLATILE ORGANIC COMPOUNDS (VOC) Vendor 31.4 137.5 2 2 31.4 137.5

Vendor 0.2 0.8 2 2 0.2 0.8OTHER

SOURCE OFEMISSION

HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrHydrogen Chloride Mass Balance 6.53E+01 1.72E+02 - - 6.53E+01 1.72E+02Hydrogen Fluoride Mass Balance 1.16E+01 2.24E+01 - - 1.16E+01 2.24E+01Antimony AP-42 7.54E-03 3.30E-02 - - 7.54E-03 3.30E-02Arsenic AP-42 1.72E-01 7.52E-01 - - 1.72E-01 7.52E-01Beryllium AP-42 8.79E-03 3.85E-02 - - 8.79E-03 3.85E-02Cadmium AP-42 2.13E-02 9.35E-02 - - 2.13E-02 9.35E-02Chromium AP-42 1.09E-01 4.77E-01 - - 1.09E-01 4.77E-01Cobalt AP-42 4.19E-02 1.83E-01 - - 4.19E-02 1.83E-01Lead AP-42 1.76E-01 7.70E-01 - - 1.76E-01 7.70E-01Manganese AP-42 2.05E-01 8.98E-01 - - 2.05E-01 8.98E-01Mercury 1 NSPS Da 3.36E-02 1.47E-01 - - 3.36E-02 1.47E-01Nickel AP-42 1.17E-01 5.13E-01 - - 1.17E-01 5.13E-01Selenium AP-42 5.44E-01 2.38E+00 - - 5.44E-01 2.38E+00Acetaldehyde AP-42 2.39E-01 1.05E+00 - - 2.39E-01 1.05E+00Acetophenone AP-42 6.28E-03 2.75E-02 - - 6.28E-03 2.75E-02Acrolein AP-42 1.21E-01 5.32E-01 - - 1.21E-01 5.32E-01Anthracene AP-42 8.79E-05 3.85E-04 - - 8.79E-05 3.85E-04Benzene AP-42 5.44E-01 2.38E+00 - - 5.44E-01 2.38E+00Benzo(g,h,i)perylene AP-42 1.13E-05 4.95E-05 - - 1.13E-05 4.95E-05Benzyl Chloride AP-42 2.93E-01 1.28E+00 - - 2.93E-01 1.28E+00Biphenyl AP-42 7.12E-04 3.12E-03 - - 7.12E-04 3.12E-03Bis(2-ethylhexyl)phthalate AP-42 3.06E-02 1.34E-01 - - 3.06E-02 1.34E-01Bromoform AP-42 1.63E-02 7.15E-02 - - 1.63E-02 7.15E-02Carbon Disulfide AP-42 5.44E-02 2.38E-01 - - 5.44E-02 2.38E-012-Chloroacetophenone AP-42 2.93E-03 1.28E-02 - - 2.93E-03 1.28E-02Chlorobenzene AP-42 9.21E-03 4.03E-02 - - 9.21E-03 4.03E-02Chloroform AP-42 2.47E-02 1.08E-01 - - 2.47E-02 1.08E-01Cumene AP-42 2.22E-03 9.72E-03 - - 2.22E-03 9.72E-03Cyanide AP-42 1.05E+00 4.58E+00 - - 1.05E+00 4.58E+00

LEAD

EXPECTED ACTUAL POTENTIAL EMSSIONS(BEFORE CONTROLS / LIMITS) (AFTER CONTROLS / LIMITS)











EMISSION SOURCE DESCRIPTION: Unit 7 Boiler

Nominal 800 MW pulverized coal (PC) boiler fired with bituminuous or a blend of bituminous and sub-bituminous coals. The boiler will be equipped with the following control devices to reduce air emissions during normal operations: low NOx burners, SCR, dry ESP, wet FGD, and WESP. See Appendix G for process diagram.


2,4-Dinitrotoluene AP-42 1.17E-04 5.13E-04 - - 1.17E-04 5.13E-04Dimethyl Sulfate AP-42 2.01E-02 8.80E-02 - - 2.01E-02 8.80E-02Ethyl benzene AP-42 3.94E-02 1.72E-01 - - 3.94E-02 1.72E-01Ethyl Chloride (Chloroethane) AP-42 1.76E-02 7.70E-02 - - 1.76E-02 7.70E-02Ethylene Dichloride AP-42 1.67E-02 7.33E-02 - - 1.67E-02 7.33E-02Ethylene Dibromide AP-42 5.02E-04 2.20E-03 - - 5.02E-04 2.20E-03Formaldehyde AP-42 1.00E-01 4.40E-01 - - 1.00E-01 4.40E-01Hexane AP-42 2.80E-02 1.23E-01 - - 2.80E-02 1.23E-01Isophorone AP-42 2.43E-01 1.06E+00 - - 2.43E-01 1.06E+00Methyl Bromide (Bromomethane) AP-42 6.70E-02 2.93E-01 - - 6.70E-02 2.93E-01Methyl Chloride (Chloromethane) AP-42 2.22E-01 9.72E-01 - - 2.22E-01 9.72E-01Methyl Ethyl Ketone AP-42 1.63E-01 7.15E-01 - - 1.63E-01 7.15E-01Methyl Hydrazine AP-42 7.12E-02 3.12E-01 - - 7.12E-02 3.12E-01Methyl Methacrylate AP-42 8.37E-03 3.67E-02 - - 8.37E-03 3.67E-02Methyl tert-butyl ether AP-42 1.47E-02 6.42E-02 - - 1.47E-02 6.42E-02Methylene Chloride AP-42 1.21E-01 5.32E-01 - - 1.21E-01 5.32E-01Naphthalene AP-42 5.44E-03 2.38E-02 - - 5.44E-03 2.38E-02Phenanthrene AP-42 1.13E-03 4.95E-03 - - 1.13E-03 4.95E-03Phenol AP-42 6.70E-03 2.93E-02 - - 6.70E-03 2.93E-02Propionaldehyde AP-42 1.59E-01 6.97E-01 - - 1.59E-01 6.97E-01Styrene AP-42 1.05E-02 4.58E-02 - - 1.05E-02 4.58E-02Tetrachloroethylene AP-42 1.80E-02 7.88E-02 - - 1.80E-02 7.88E-02Toluene AP-42 1.00E-01 4.40E-01 - - 1.00E-01 4.40E-011,1,1-Trichloroethane AP-42 8.37E-03 3.67E-02 - - 8.37E-03 3.67E-02Vinyl Acetate AP-42 3.18E-03 1.39E-02 - - 3.18E-03 1.39E-02Xylene AP-42 1.55E-02 6.78E-02 - - 1.55E-02 6.78E-02Total PCDD/PCDF AP-42 7.37E-07 3.23E-06 - - 7.37E-07 3.23E-06

TOXIC AIR POLLUTANT AND CAS NO. EF SOURCEHydrogen Chloride Mass Balance 65.29 1566.85 571898.56Hydrogen Fluoride Mass Balance 11.63 279.20 101907.58Arsenic AP-42 0.17 4.12 1503.52Beryllium AP-42 0.01 0.21 77.01Cadmium AP-42 0.02 0.51 187.02Chromium AP-42 0.11 2.61 953.45Manganese AP-42 0.21 4.92 1796.89Mercury AP-42 0.03 0.81 294.34Nickel AP-42 0.12 2.81 1026.80Acetaldehyde AP-42 0.24 5.73 2090.26Acrolein AP-42 0.12 2.91 1063.47Benzene AP-42 0.54 13.06 4767.27Benzyl Chloride AP-42 0.29 7.03 2566.99Carbon Disulfide AP-42 0.05 1.31 476.73Chlorobenzene AP-42 0.01 0.22 80.68Chloroform AP-42 0.02 0.59 216.36Ethylene Dichloride AP-42 0.02 0.40 146.69Ethylene Dibromide AP-42 0.00 0.01 4.40Formaldehyde AP-42 0.10 2.41 880.11Hexane AP-42 0.03 0.67 245.70Methyl Ethyl Ketone AP-42 0.16 3.92 1430.18Methylene Chloride AP-42 0.22 5.32 1943.58Phenol AP-42 0.01 0.16 58.67Styrene AP-42 0.01 0.25 91.68Toluene AP-42 0.10 2.41 880.11Xylene AP-42 0.02 0.37 135.68Sulfuric Acid Vendor 47.10 1130.40 412596.00Ammonia Vendor 31.40 753.60 275064.00

1 Calculated based on NSPS Subpart Da, Sub-bituminous units w/ wet FGD - see emission calculation notes2 Emissions provided are based on preliminary design. Information based on final design will be provided to NC DAQ.

INDICATE EXPECTED ACTUAL EMISSIONS AFTER CONTROLS / LIMITATIONSlb/yr


lb/hr

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) de

lb/day

REVISED 12/01/01 B1EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: U7

CONTROL DEVICE ID NO(S): CD 23-26

OPERATING SCENARIO: ______1________ OF ______1________ EMISSION POINT (STACK) ID NO(S): EP-U7

DESCRIBE USE: PROCESS HEAT SPACE HEAT X ELECTRICAL GENERATION

CONTINUOUS US STAND BY/EMERGENCY OTHER (DESCRIBE): _________









PULVERIZED


X DRY BED CONTROLLED CONTROLLED FLYASH REINJECTION RECIRCULATING


METHOD OF LOADING: CYCLONE HANDFIRED TRAVELING GRATE X OTHER (DESCRIBE): Supercritical PC Unit

METHOD OF TUBE CLEANING: TBD CLEANING SCHEDULE: As needed

TYPE OF BOILER: UTILITY INDUSTRIAL COMMERCIAL RESIDENTIAL

TYPE OF FIRING: NORMAL TANGENTIAL LOW NOX BURNERS NO LOW NOX BURNER





No. 2 Fuel Oil (Start-up) mmBTU 2747.5 NA

Coal mmBTU 7850 NA


Coal 9376 BTU/lb 3.0 11.29

COMMENTS:

Fuel oil will be combusted along with coal for start-up, up to 35% of maximum capacity, where the fuel will be switched to coal. Fuel oil may also be usedwhen the pulverizer is brought into service. Coal will be a blend from various regions and coal specs. given are conservative.




COAL-FIRED BURNER


WOOD TYPE:



WOOD-FIRED BURNER

Nominal 800 MW pulverized coal (PC) boiler fired with bituminous or a blend of bituminous and sub-bituminous coals. Boiler is controlled by SCR system, a dry electrostatic precipitator (ESP), a wet-flue gas desulfurization unit, and a wet ESP.



MAXIMUM DESIGN

CAPACITY (UNIT/HR)

REQUESTED CAPACITY

FUEL TYPE UNITS

SAMPLING PORTS, COMPLIANT WITH EPA METHOD 1 WILL BE INSTALLED ON THE STACKS: X YES NO


ASH CONTENT

(% BY WEIGHT)

SULFUR CONTENT

FUEL TYPE

SPECIFIC


REVISED 12/01/01

CONTROL DEVICE ID NO: CD23 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S U7

EMISSION POINT (STACK) ID NO(S)EP-U7 POSITION IN SERIES OF CONTROLS NO. 1 OF 4 UNITS



PROPOSED CONSTRUCTION DATE 2007

TYPE: AFTERBURNER REGENERATIVE THERMAL OXIDATION RECUPERATIVE THERMAL OXIDATION

CATALYTIC OXIDATIONEXPECTED LIFE OF CATALYST (YRS): METHOD OF DETECTING WHEN CATALYST NEEDS REPLACMENT:CATALYST MASKING AGENT IN AIR STREAM: HALOGEN SILICONE PHOSPHOROUS COMPOUND HEAVY METAL

SULFUR COMPOUND OTHER_________________ NONE

TYPE OF CATALYST: Vanadium pentoxide CATALYST VOL (FT3): TBD VELOCITY THROUGH CATALYST (FPS): TDB

SCFM THROUGH CATALYST:

DESCRIBE CONTROL SYSTEM, INCLUDING RELATION TO OTHER CONTROL DEVICES AND SOURCES, AND ATTACH DIAGRAM OF SYSTEM:

POLLUTANT(S) COLLECTED: NOx

BEFORE CONTROL EMISSION RATE (LB/HR): 2355 lb/hr(to SCR; 0.30 lb/mmbtu)



OVERALL SYSTEM EFFICIENCY: % % % %


TOTAL EMISSION RATE (LB/HR) : 628 lb/hr (after SCR; 0.08 lb/mmbtu)

PRESSURE DROP (IN. H2 OUTLET TEMPERATURE (oF):

INLET TEMPERATURE (oF RESIDENCE TIME (SECONDS):

INLET AIR FLOW RATE (ACFM):4,500,000 to SCR COMBUSTION TEMPERATURE (oF):

COMBUSTION CHAMBER VOLUME (FT3): INLET MOISTURE CONTENT (%):

% EXCESS AIR: CONCENTRATION (ppmv) ______INLET ______OUTLET

AUXILIARY FUEL USED: No. 2 Fuel Oil TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): 7850 lb/mmbtu

MAXIMUM ANNUAL FUEL USE: UNITS: MAXIMUM HOURLY FUEL USE: UNITS:

ACTUAL ANNUAL FUEL USE: UNITS: ACTUAL HOURLY FUEL USE: 418.6 UNITS:ton/hr design coal

DESCRIBE METHOD USED TO INCREASE MIXING:

DESCRIBE METHOD TO INSURE ADEQUATE START-UP TEMPERATURE:

DESCRIBE TEMPERATURE MONITORING DEVICES AND PROCEDURES:

STACK TESTING PORTS: NO YES (INLET AND OUTLET)




C3

___1____ OF __1_____

AS REQUIRED BY 15A NCAC 2Q .0112, THIS FORM MUST BE SEALED BY A PROFESSIONAL ENGINNER (P.E.) LICENSED IN NORTH CAROLINA.

OPERATING SCENARIO:


MIN 600 MAX 750 at econ.

MIN MAX AVE:4.3 across SCR MIN MAX 750 at SCR outlet

The Selective Catalytic Reduction (SCR) system catalytically reduces boiler flue gas nitrogen oxide (NOx) emissions to nitrogen and water using anydrous ammonia (NH3) as a reducing agent. Flue gas exiting the ecomonizer outlet flows through two flow paths prior to entering the ammonia / air injection zone. Each flue has a dedicated ammonia injection grid fed by a manifold valve station. Following the ammonia injection the gas enters the SCR reactor were the NOreacts with the ammonia and is converted to nitrogen and water. The flue gas exiting the reactor is directed into the air heater.

NOx emissions from the boiler will be controlled using a combination of low-NOx burners, over-fire air and a selective catalytic reduction (SCR) system. The combustion system applies air-staging in combination with low-NOx burners to minimize NOx formation in the furnace to minimze the amount of SCR catalyst required and reduce the consumption of reagent.


FORM C3 CONTROL DEVICE (THERMAL OR CATALYTIC)

Steam coil air heaters are designed to preheat the combustion air during initial firing. Ammonia is injected once the catalst bed temperature has been elevated above the estimated minimum injection temperature of 600o. Temp. to be confirmed by catalyst supplier.

The ammonia injection grid has multiple zones for injecting ammonia across the flue gas path. Each injection pipe has numerous injection orifices for optimim ammonia-flue gas mixing.

REVISED 12/01/01 C2CONTROL DEVICE ID NO: CD24 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): U7

EMISSION POINT (STACK) ID NO(S)EP-U7 POSITION IN SERIES OF CONTROL NO. 2 OF 4 UNITS






TOTAL COLLECTION PLATE AREA (FT2): 1,130,000 NO. FIELDS5 NO. COLLECTOR PLATE PER FIELD:

COLLECTOR PLATES SIZE (FT): LENGTH: 50 WIDTH: SPACING BETWEEN COLLECTOR PLATES (INCHES): 16TOTAL DISCHARGE ELECTRODE LENGTH(FT): GAS VISCOSITY (POISE):



MINIMUM GAS TREATMENT TIME (SEC): 15


ELECTRICAL USAGE (kw/HOUR): 1400 kW


PRESSURE DROP (IN. H20): MIN MAX AVE:.2 WARNING ALARM? YES NO


INLET GAS TEMPERATURE (oF): MIN MAX AV300 OUTLET GAS TEMPERATURE (oF): MIN MAX AVE: 298


TBD TBD TBD TBD TBD

filterable PM10






TOTAL EMISSION RATE (LB/HR): 118 lb/hr (0.015 lb/mmbtu)







OPERATING SCENARIO:

_____1__ OF ___1____ P.E. SEAL REQUIRED (PER 2Q .0112)? YES NO




POWER REQUIREMENTS IS AN ENERGY MANAGEMENT SYSTEM USED? YES NO

FIELD NO. NO. OF SETS CHARGING EACH TRANSFORMER (kVA) EACH RECTIFIER Kv Ave/Peak Ma Dc




0-11-1010-2525-5050-100>100

TOTAL = 100


EMISSION POINT ID NO(S): EP-U7 POSITION IN SERIES OF CONTROLS: NO. 3 OF 4 UNITS


DATE MANUFACTURED: TBD PROPOSED OPERATION DATE: 2011

PROPOSED CONSTRUCTION DATE: 2007


POLLUTANT(S) COLLECTED: SO2

BEFORE CONTROL EMISSION RATE (LB/HR): 39,250

CAPTURE EFFICIENCY: % % %

CONTROL DEVICE EFFICIENCY: % % %

CORRESPONDING EFFICIENCY: 99 % % %


TOTAL EMISSION RATE (LB/HR): 1178 lb/hr (0.15 lb/mmbtu - 30 day average)

PRESSURE DROP (IN. H20): MIN MAX AVE: 11 YES NO

INLET TEMPERATURE (oF): MIN MAX AVE: 300 OUTLET TEMPERATURE (oF): MIN MAX AVE: 120

INLET AIR FLOW RATE (ACFM): MOISTURE CONTENT : INLET % OUTLET %

THROAT VELOCITY (FT/SEC): THROAT TYPE: FIXED VARIABLE

TYPE OF SYSTEM: Wet Limestone, forced oxidation TYPE OF PACKING USED IF ANY: n/aADDITIVE LIQUID SCRUBBING MEDIUM: limestone slurry PERCENT RECIRCULATED:

MINIMUM LIQUID INJECTION RATE (GAL/MIN 313 FLOW RATE GAUGE INSTALLED? YES NO

MAKE UP RATE (GAL/MIN): FOR ADDITIVE (GAL/MIN):DESCRIBE MAINTENANCE PROCEDURES:

WEIGHT %OF TOTAL

DESCRIBE ANY MONITORING DEVICES, GAUGES, TEST PORTS, ETC:


____1___ OF ___1____ P.E. SEAL NEEDED (PER 2Q .0112)? YES NO

The proposed flue gas desulfurization (FGD) system is a wet limestone, forced oxidation, system with a vertical, countercurrent, spray tower absorber. The flue gas enters the spray tower near the bottom through the absorber inlet nozzle. Once in the absorber, the hot flue gas is immediately quenched as it travels upward countercurrent to a continuous spray of process/recycle slurry produced by multiple spray banks. The recycle slurry extracts the sulfur dioxide from the flue gas and collects it in the bottom of the absorber where it is oxidized to calcium sulfate. The proposed system will treat 100% of the flue gas from the unit. The unit will be designed for 99% removal efficiency.

FORM C8CONTROL DEVICE (WET PARTICULATE SCRUBBER)

OPERATING SCENARIO:


2,550,000

1300


>100TOTAL = 100

50-100

CUMULATIVE%

0-1

25-50

WARNING ALARM?


1-1010-25

SIZE(MICRONS)


EMISSION POINT (STACK) ID NO(S) EP-U7 POSITION IN SERIES OF CONTROL NO. 4 OF 4 UNITS






TOTAL COLLECTION PLATE AREA (FT2): 612,000 NO. FIELDS3 NO. COLLECTOR PLATE PER FIELD:

COLLECTOR PLATES SIZE (FT): LENGTH: 29.53 WIDTH: SPACING BETWEEN COLLECTOR PLATES (INCHES): 9.75




MINIMUM GAS TREATMENT TIME (SEC):


ELECTRICAL USAGE (kw/HOUR):




INLET GAS TEMPERATURE (oF): MIN MAX AVE: 128 OUTLET GAS TEMPERATURE (oF): MIN MAX AVE: 128


TBD TBD TBD TBD TBD

Total PM10 Filterable PM10 H2SO4




CORRESPONDING OVERALL EFFICIENCY: % % % %


TOTAL EMISSION RATE (LB/HR): 188 lb/hr(0.024lb/mmbtu) 117.8 lbhr(0.015 lb/mmbtu) 47.1 lb/hr (0.006lb/mmbtu)






NO. OF SETS CHARGING EACH TRANSFORMER (kVA) EACH RECTIFIER Kv Ave/Peak Ma DcFIELD NO.


_____1__ OF ___1____ P.E. SEAL REQUIRED (PER 2Q .0112)? YES NO

25-50


OF TOTAL

50-100



%

>100TOTAL = 100


OPERATING SCENARIO:


CUMULATIVE

10-25


IS AN ENERGY MANAGEMENT SYSTEM USED? YES NO

WEIGHT %

0-11-10

(MICRONS)


SIZE


POWER REQUIREMENTS

REVISED 12/01/01 BEMISSION SOURCE ID NO: Aux 6&7CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Aux 6&7




START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: TBDIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Db NESHAP (SUBPART?):________ MACT (SUBPART?):DDDDD_


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) BACT 1 2.66 3.33 2.66 11.67 2.66 3.33PARTICULATE MATTER<10 MICRONS (PM10) BACT 1 4.56 5.70 4.56 19.97 4.56 5.70PARTICULATE MATTER<2.5 MICRONS (PM2.5) NA NA NA NA NA NASULFUR DIOXIDE (SO2) AP-42 9.85 12.31 9.85 43.13 9.85 12.31NITROGEN OXIDES (NOx) BACT 1 19.00 23.75 19.00 83.22 19.00 23.75CARBON MONOXIDE (CO) BACT 1 6.84 8.55 6.84 29.96 6.84 8.55VOLATILE ORGANIC COMPOUNDS (VOC) BACT 1 0.46 0.57 0.46 2.00 0.46 0.57

AP-42 0.00 0.00 0.00 0.01 0.00 0.00SULURIC ACID AP-42 0.17 0.21 0.17 0.74 0.17 0.21

SOURCE OFEMISSION

HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrBenzene AP-42 2.97E-04 3.71E-04 2.97E-04 1.30E-03 2.97E-04 3.71E-04Ethylbenzene AP-42 8.82E-05 1.10E-04 8.82E-05 3.86E-04 8.82E-05 1.10E-04Formaldehyde AP-42 8.46E-02 1.06E-01 8.46E-02 3.71E-01 8.46E-02 1.06E-01Naphthalene AP-42 1.57E-03 1.96E-03 1.57E-03 6.86E-03 1.57E-03 1.96E-031,1,1-Trichloroethane AP-42 3.27E-04 4.09E-04 3.27E-04 1.43E-03 3.27E-04 4.09E-04Toluene AP-42 8.60E-03 1.07E-02 8.60E-03 3.77E-02 8.60E-03 1.07E-02o-Xylene AP-42 1.51E-04 1.89E-04 1.51E-04 6.62E-04 1.51E-04 1.89E-04Acenaphthene AP-42 2.93E-05 3.66E-05 2.93E-05 1.28E-04 2.93E-05 3.66E-05Acenaphthylene AP-42 3.51E-07 4.39E-07 3.51E-07 1.54E-06 3.51E-07 4.39E-07Anthracene AP-42 1.69E-06 2.11E-06 1.69E-06 7.41E-06 1.69E-06 2.11E-06Benz(a)anthracene AP-42 5.56E-06 6.95E-06 5.56E-06 2.44E-05 5.56E-06 6.95E-06Benzo(b.k)fluoranthene AP-42 2.05E-06 2.57E-06 2.05E-06 8.99E-06 2.05E-06 2.57E-06Benzo(g,h,i)perylene AP-42 3.13E-06 3.92E-06 3.13E-06 1.37E-05 3.13E-06 3.92E-06Chrysene AP-42 3.30E-06 4.13E-06 3.30E-06 1.45E-05 3.30E-06 4.13E-06Dibenzo(a,h)anthracene AP-42 2.32E-06 2.90E-06 2.32E-06 1.01E-05 2.32E-06 2.90E-06Fluoranthene AP-42 6.71E-06 8.39E-06 6.71E-06 2.94E-05 6.71E-06 8.39E-06Fluorene AP-42 6.20E-06 7.75E-06 6.20E-06 2.72E-05 6.20E-06 7.75E-06Indo(1,2,3-cd)pyrene AP-42 2.97E-06 3.71E-06 2.97E-06 1.30E-05 2.97E-06 3.71E-06Phenanthrene AP-42 1.46E-05 1.82E-05 1.46E-05 6.38E-05 1.46E-05 1.82E-05Pyrene AP-42 5.89E-06 7.37E-06 5.89E-06 2.58E-05 5.89E-06 7.37E-06OCDD AP-42 4.30E-09 5.37E-09 4.30E-09 1.88E-08 4.30E-09 5.37E-09

TOXIC AIR POLLUTANT AND CAS NO. EF SOURCEBenzene AP-42 2.97E-04 7.12E-03 2.60Formaldehyde AP-42 8.46E-02 2.03E+00 741.08Toluene AP-42 8.60E-03 2.06E-01 75.32Arsenic AP-42 7.60E-04 1.82E-02 6.66Beryllium AP-42 5.70E-04 1.37E-02 4.99Cadmium AP-42 5.70E-04 1.37E-02 4.99Chromium AP-42 5.70E-04 1.37E-02 4.99Lead AP-42 1.71E-03 4.10E-02 14.98Mercury AP-42 5.70E-04 1.37E-02 4.99Manganese AP-42 1.14E-03 2.74E-02 9.99Nickel AP-42 5.70E-04 1.37E-02 4.99Selenium AP-42 2.85E-03 6.84E-02 24.97

1 Emission factor based on the proposed BACT emission rates for distillate oil-fired boilers.



lb/hr






EMISSION SOURCE DESCRIPTION: Auxiliary Boiler

Distillate fuel oil-fired 190mmBTU/hr auxiliary steam boiler will meet the steam demand during start up of the main steam generators.

OPERATING SCENARIO _______1__________OF ________1__________




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) de

lb/day

LEAD



POTENTIAL EMSSIONS(BEFORE CONTROLS / LIMITS)

EXPECTED ACTUAL


REVISED 12/01/01 B1EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Aux 6&7

CONTROL DEVICE ID NO(S):

OPERATING SCENARIO: ______1________ OF ________1______ EMISSION POINT (STACK) ID NO(S): Aux 6&7

DESCRIBE USE: PROCESS HEAT SPACE HEAT ELECTRICAL GENERATION

CONTINUOUS US STAND BY/EMERGENCY X OTHER (DESCRIBE): _Process Steam__









PULVERIZED


DRY BED CONTROLLED CONTROLLED FLYASH REINJECTION RECIRCULATING


METHOD OF LOADING: CYCLONE HANDFIRED TRAVELING GRATE OTHER (DESCRIBE): _________________


TYPE OF BOILER: UTILITY X INDUSTRIAL COMMERCIAL RESIDENTIAL

TYPE OF FIRING: NORMAL TANGENTIAL X LOW NOX BURNERS NO LOW NOX BURNER

METHOD OF TUBE CLEANING: NA CLEANING SCHEDULE: NA




No. 2 Fuel Oil mmBTU 190 NA


COMMENTS:




COAL-FIRED BURNER


WOOD TYPE:



WOOD-FIRED BURNER

Distillate fuel oil-fired 190mmBTU/hr auxiliary steam boiler will meet the steam demand during start up of the main steam generators.



MAXIMUM DESIGN

CAPACITY (UNIT/HR)

REQUESTED CAPACITY

FUEL TYPE UNITS

SAMPLING PORTS, COMPLIANT WITH EPA METHOD 1 WILL BE INSTALLED ON THE STACKS: YES NO


ASH CONTENT

(% BY WEIGHT)

SULFUR CONTENT

FUEL TYPE

SPECIFIC


Emissions will be controlled by the following: only burning low sulfur (0.05 percent sulfur) distillate oil using low-NOx burners, good combustion, and limiting operation to 2500 hours/year. Propane used for initial light-off.

REVISED 12/01/01 BEMISSION SOURCE ID NO: CT1 & CT 2CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): CT1 & CT 2


Coal,wood,oil, gas, other burner (Form B1) Woodworking (Form B4) Manufact. of chemicals/coatings/inks (Form B7)

Int.combustion engine/generator (Form B2) Coating/finishing/printing (Form B5) Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) X Other (Form B9)

START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: TBDIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):_


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) AP-42 2.61 11.43 2.61 11.43PARTICULATE MATTER<10 MICRONS (PM10) AP-42 2.61 11.43 2.61 11.43PARTICULATE MATTER<2.5 MICRONS (PM2.5)

SULFUR DIOXIDE (SO2)NITROGEN OXIDES (NOx)CARBON MONOXIDE (CO)VOLATILE ORGANIC COMPOUNDS (VOC)

OTHER

SOURCE OFEMISSION

HAZARDOUS AIR POLLUTANT AND CAS NO. FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yr

TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE

COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURC

LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Two Multi-Cell Cooling Towers

Two multi-cell (up to 24 cells each) mechanical draft cooling towers will be installed as part of a wet cooling system for proposed Units 6 & 7. Emission Provided below are for one cooling tower.

OPERATING SCENARIO ______1___________OF _________1_________







lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPT Two Multi-Cell Cooling Towers EMISSION SOURCE ID NO: CT1 & CT2


EMISSION POINT (STACK) ID NO(S): CT1 & CT2

DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM):

Two multi-cell (up to 24 cells each) mechanical draft cooling towers will be installed as part of a wet cooling system for proposed Units 6 & 7

UNITS

Cooling Tower Water Gallons 347,434 NA

UNITS

MAXIMUM DESIGN (BATCHES / HOUR):

REQUESTED LIMITATION (BATCHES / HOUR): (BATCHES/YR):

FUEL USED: NA TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR): NA

MAX. CAPACITY HOURLY FUEL USE: NA REQUESTED CAPACITY ANNUAL FUEL USE: NACOMMENTS:

FORM B9EMISSION SOURCE (OTHER)


LIMITATION(UNIT/HR)

MAX. DESIGN

TYPE CAPACITY (UNIT/HR)

OPERATING SCENARIO: ____1__________ OF _____1_________

MATERIALS ENTERING PROCESS - CONTINUOUS PROCESS

Attach Additional Sheets as Necessary

TYPE CAPACITY (UNIT/BATCH) LIMITATION (UNIT/BATCH)

MATERIALS ENTERING PROCESS - BATCH OPERATION

REQUESTED CAPACITY

The cooling towers will be equipped with specially designed drift eliminators that will act to remove droplets from the cooling tower plume, which will both conserve water and reduce drift and resultant particulate emissions.

MAX. DESIGN REQUESTED CAPACITY

REVISED 12/01/0 BEMISSION SOURCE ID NO: C19CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive



Int.combustion engine/generator (Form B2 Coating/finishing/printing (Form Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) X Other (Form B9)

START CONSTRUCTION DATE:January 2007 OPERATION DATE: 2011 DATE MANUFACTURE 2007MANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):___Y____ NESHAP (SUBPART?):________ MACT (SUBPART?):__________

EXPECTED ANNUAL HOURS OF OPERATIO< 8760

SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) AP-42 0.65 5.73 0.65 5.73PARTICULATE MATTER<10 MICRONS (PM10) AP-42 0.32 2.79 0.32 2.79PARTICULATE MATTER<2.5 MICRONS (PM2.5)SULFUR DIOXIDE (SO2)NITROGEN OXIDES (NOx)CARBON MONOXIDE (CO)VOLATILE ORGANIC COMPOUNDS (VOC)

OTHER

SOURCE OFEMISSION



PLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SO

LEAD

EXPECTED ACTUAL



lb/day


BEFORE CONTROLS / LIMITS


EXPECTED OP. SCHEDULE: __24__ HR/DAY __7_ DAY/WK ___52_

VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: ___<20__ % OPACPERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25




EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Unit 6&7 Reclaim Hopper Emissions

See Appendix G for process diagrams. Fugitive emissions include bulldozing coal to hoppers. (Emissions were already provided in Unit 5 Application for Bulldozing and Unit 5 Reclaim Hopper C11 and C12). Assumptions for coal bulldozing are as follows : 2 Bulldozers operating 24 hrs/day each and 365 days/yr. Dust suppression agents will be used to control fugitive emissions.

OPERATING SCENARIO __________1_______OF __________1________



POTENTIAL EMSSIONSBEFORE CONTROLS / LIMITS




lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: C19


EMISSION POINT (STACK) ID NO(S):


UNITS

tons

UNITS








OPERATING SCENARIO: _______1_______ OF ________1______



REQUESTED CAPACITY

Fugitive

Coal (Reclaim Hoppers) 500



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagrams. Fugitive coal handling emissions include material handling from bulldozing. (Emissions were already provided in Unit 5 Application for Bulldozing and Unit 5 Reclaim Hopper). Assumptions for coal bulldozing are as follows : 2 Bulldozers operating 24 hrs/day each and 365 days/yr. Dust suppression agents will be used to control fugitive emissions.

EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Reclaim Hopper Emissions

REVISED 12/01/01 BEMISSION SOURCE ID NO: C20-C23CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive




START CONSTRUCTION DATEJanuary 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):___Y____ NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) NA NA NA NAPARTICULATE MATTER<10 MICRONS (PM10) NA NA NA NAPARTICULATE MATTER<2.5 MICRONS (PM2.5)


OTHER

SOURCE OFEMISSION






lb/hr




EXPECTED OP. SCHEDULE: __24__ HR/DAY __7_ DAY/WK ___52__ WK/YR

VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: ___<20__ % OPACITYPERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25




EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Reclaim Conveyors (4)

See Appendix G for process diagrams. Fugitive emissions from reclaim conveyors to the transfer house. The reclaim conveyors to the transfer house are located underground. No emissions are expected from these sources. The length of each of the conveyors is as follows: C20 : Reclaim Conveyor RC5 - U6&7 - 700 ft C21 : Reclaim Conveyor RC6 - U6&7 - 700 ft C22 : Reclaim Conveyor RC7 - U6&7 - 1100 ft C23 : Reclaim Conveyor RC8 - U6&7 - 1100 ftBelt Widths are 48 inches.





COMPLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SOURCE

LEAD

EXPECTED ACTUAL



lb/day

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: C20-C23

Fugitive Coal Handling - Reclaim Conveyors (4) CONTROL DEVICE ID NO(S):



UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN






REQUESTED CAPACITY

Fugitive

See Appendix G for process diagrams. Fugitive emissions from reclaim conveyors to the transfer house. The reclaim conveyors to the transfer house are located underground. No emissions are expected from these sources. The length of each of the conveyors is as follows: C20 : Reclaim Conveyor RC5 - U6&7 - 700 ft C21 : Reclaim Conveyor RC6 - U6&7 - 700 ft C22 : Reclaim Conveyor RC7 - U6&7 - 1100 ft C23 : Reclaim Conveyor RC8 - U6&7 - 1100 ftBelt Widths are 48 inches.

Coal 1500



REVISED 12/01/01 BEMISSION SOURCE ID NO: C24-C26CONTROL DEVICE ID NO(S): CD27EMISSION POINT (STACK) ID NO(S): EP-C26




START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): Y NESHAP (SUBPART?):________ MACT (SUBPART?):_


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) 1 2.57 11.26 2.57 11.26PARTICULATE MATTER<10 MICRONS (PM10)

1 2.57 11.26 2.57 11.26PARTICULATE MATTER<2.5 MICRONS (PM2.5)


OTHER

SOURCE OFEMISSION



1 Emissions are based on control device outlet concentration design and exhaust fan parameters.

LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Coal Reclaim Conveyors (2) & Unit 6&7 Crusher House

See Appendix G for process diagram. Emissions include Unit 6&7 Crusher House and the following reclaim conveyors controlled by a partially enclosed hood:C24: Reclaim Conveyor RC9 to U6& Crusher House (750 ft)C25: Reclaim Conveyor RC10 to U6&7 Crusher House (750 ft)Belt Widths are 48 inches.

OPERATING SCENARIO _________1________OF ________1__________



POTENTIAL EMSSIONS(BEFORE CONTROLS / LIMITS) (AFTER CONTROLS / LIMITS)


lb/hr


Coal Reclaim Conveyors (2) & Unit 6&7 Crusher House CONTROL DEVICE ID NO(S): CD27

EMISSION POINT (STACK) ID NO(S): EP-C26


UNITS

Coal tons 1500 NA

UNITS






OPERATING SCENARIO: _______1_______ OF ______1________





REQUESTED CAPACITY



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagram. Emissions include Unit 6&7 Crusher House and the following reclaim conveyors controlled by a partially enclosed hood:C24: Reclaim Conveyor RC9 to U6& Crusher House (750 ft)C25: Reclaim Conveyor RC10 to U6&7 Crusher House (750 ft)Belt Widths are 48 inches.

REVISED 12/01/01 BEMISSION SOURCE ID NO: C27-C30CONTROL DEVICE ID NO(S): C28EMISSION POINT (STACK) ID NO(S): EP-C27-C30






SOURCE OFEMISSION




OTHER

SOURCE OFEMISSION



LEAD

EXPECTED ACTUAL



lb/day




EMISSION SOURCE DESCRIPTION: Unit 6 Boiler House Coal Handling: Reclaim Conveyors (2) & Tripper Conveyors (2)

See Appendix G for process diagram. Emissions represent the following coal reclaim conveyors controlled by partially enclosed hood/filter and tripper conveyors that are controlled by enclosed room/filter:C27: Reclaim Conveyor RC11 to Unit 6 Boiler Building (600 ft)C28: Reclaim Conveyor RC12 to Unit 6 Boiler Building (600 ft)Belt Widths are 48 inches.C29: Unit 6 Tripper Conveyor TR2 (300 ft)C30: Unit 6 Tripper Conveyor TR3 (300 ft)Belt Widths are 54 inches.




VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: _< 20___ % OPACITYPERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25







lb/hr


Unit 6 Boiler House Coal Handling: Reclaim Conveyors (2) & Tripper Conveyors (2) CONTROL DEVICE ID NO(S): C28

EMISSION POINT (STACK) ID NO(S): EP-C27-C30


UNITS

Coal tons 1500 NA

UNITS











REQUESTED CAPACITY



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagram. Emissions represent the following coal reclaim conveyors controlled by partially enclosed hood/filter and tripper conveyors that are controlled by enclosed room/filter:C27: Reclaim Conveyor RC11 to Unit 6 Boiler Building (600 ft)C28: Reclaim Conveyor RC12 to Unit 6 Boiler Building (600 ft)Belt Widths are 48 inches.C29: Unit 6 Tripper Conveyor TR2 (300 ft)C30: Unit 6 Tripper Conveyor TR3 (300 ft)Belt Widths are 54 inches.

REVISED 12/01/01 BEMISSION SOURCE ID NO: C31-C34CONTROL DEVICE ID NO(S): C29EMISSION POINT (STACK) ID NO(S): EP-C31-C34






SOURCE OFEMISSION




OTHER

SOURCE OFEMISSION


TOXIC AIR POLLUTANT AND CAS NO. EF SOURCE lb/hr













EMISSION SOURCE DESCRIPTION: Unit 7 Boiler House Coal Handling: Transfer Conveyors (2) & Tripper Conveyors (2)

See Appendix G for process diagram. Emissions represent the following coal transfer conveyors controlled by partially enclosed hood/filter and tripper conveyors that are controlled by enclosed room/filter:C31: Reclaim Conveyor RC13 to Unit 7 Boiler Building (300 ft)C32: Reclaim Conveyor RC14 to Unit 7 Boiler Building (300 ft)Belt Widths are 48 inches.C33: Unit 7 Tripper Conveyor TR4 (300 ft)C34: Unit 7 Tripper Conveyor TR5 (300 ft)Belt Widths are 54 inches.


LEAD

EXPECTED ACTUAL



lb/day


Unit 7 Boiler House Coal Handling: Transfer Conveyors (2) & Tripper Conveyors (2) CONTROL DEVICE ID NO(S): C29

EMISSION POINT (STACK) ID NO(S): EP-C31-C34


UNITS

Coal tons 1500 NA

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagram. Emissions represent the following coal transfer conveyors controlled by partially enclosed hood/filter and tripper conveyors that are controlled by enclosed room/filter:C31: Reclaim Conveyor RC13 to Unit 7 Boiler Building (300 ft)C32: Reclaim Conveyor RC14 to Unit 7 Boiler Building (300 ft)Belt Widths are 48 inches.C33: Unit 7 Tripper Conveyor TR4 (300 ft)C34: Unit 7 Tripper Conveyor TR5 (300 ft)Belt Widths are 54 inches.







REQUESTED CAPACITY

REVISED 12/01/01 BEMISSION SOURCE ID NO: A1-A6CONTROL DEVICE ID NO(S): C30EMISSION POINT (STACK) ID NO(S): EPA1-A6



Int.combustion engine/generator (Form B2) Coating/finishing/printing (Form B5) Incineration (Form B8) Liquid storage tanks (Form B3) X Storage silos/bins (Form B6) Other (Form B9)

START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):_


SOURCE OFEMISSION




OTHER

SOURCE OFEMISSION








VISIBLE STACK EMISSIONS UNDER NORMAL OPERATION: _20___ % OPACITYPERCENTAGE ANNUAL THROUGHPUT (%): DEC-FEB 25 MAR-MAY 25 JUN-AUG 25 SEP-NOV 25







EMISSION SOURCE DESCRIPTION: Unit 6 Fly Ash Handling (Controlled)

See Appendix G for process diagram. Sources include the following:A1: Wet Botton Ash Transfer and Pickup - Botton ash has consistency of wet sand - no emissions expected.A2: Wet Botton Ash Transfer and Pickup - Botton ash has consistency of wet sand - no emissions expected.A3: Dry Fly Ash Pickup at Boiler Economizer - Fly ash pneumatically conveyed to silo A4: Dry Fly Ash Pickup at Precipitator - Fly ash pneumatically conveyed to silo A5: Dry Fly Ash Piping to Fly Ash Silo - Fly ash pneumatically conveyed to siloA6: Fly Ash Silo


LEAD

EXPECTED ACTUAL



lb/day

REVISED 12/01/01 B6EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: A1-A6

Unit 6 Fly Ash Silo and conveyors CONTROL DEVICE ID NO(S): CD30

OPERATING SCENARIO: ________1______ OF ______1_________ EMISSION POINT(STACK) ID NO(S): EP-A1-A6


See Appendix G for process diagram.

MATERIAL STORED: Fly Ash DENSITY OF MATERIAL (LB/FT3): 80

CUBIC FEET: TONS:

HEIGHT: 100 DIAMETER: 30 (OR) LENGTH: WIDTH: HEIGHT:

ACTUAL: ~284,000/each MAXIMUM DESIGN CAPACITY:

BLOWER SCREW CONVEYOR RAILCAR

COMPRESSOR BELT CONVEYOR TRUCK

OTHER: BUCKET ELEVATOR STORAGE PILE

OTHER: OTHER:

NO. FILL TUBES:

MAXIMUM ACFM:

MATERIAL IS FILLED TO:

BY WHAT METHOD IS MATERIAL UNLOADED FROM SILO?

Material is mixed with water and dropped into an open bed truck. The truck is then tarpped for transport.

Material can also be withdrawn through a dustless unloader into an enclosed pneumatic tank truck for shipment.

MAXIMUM DESIGN FILLING RATE OF MATERIAL (TONS/HR): 20

MAXIMUM DESIGN UNLOADING RATE OF MATERIAL (TONS/HR): 200

COMMENTS:

MOTOR HP:


FORM B6EMISSION SOURCE (STORAGE SILO/BINS)


FILLED FROMPNEUMATICALLY FILLED MECHANICALLY FILLEDANNUAL PRODUCT THROUGHPUT (TONS)

CAPACITY

DIMENSIONS (FEET)

REVISED 12/01/01 C1CONTROL DEVICE ID NO: C30 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): A3-A6

EMISSION POINT (STACK) ID NO(S): EPA3-A6 POSITION IN SERIES OF CONTROLS NO. 1 OF 1 UNITS




___1____ OF ___1____

Bin Vent fabric filter to control emissions from the Unit #6 fly ash silo

POLLUTANT(S) COLLECTED: Particulates

BEFORE CONTROL EMISSION RATE (LB/HR): 1.3





TOTAL EMISSION RATE (LB/HR): 0.0013

PRESSURE DROP (IN. H20): MIN: 4 MAX: 7 GAUGE?

BULK PARTICLE DENSITY (LB/FT3): 50 - 60 INLET TEMPERATURE (oF): MIN MAX ambient

POLLUTANT LOADING RATE: 10 LB/HR GR/FT3 OUTLET TEMPERATURE (oF): MIN MAX ambientINLET AIR FLOW RATE (ACFM): N/A FILTER MAX OPERATING TEMP. (oF): 275

NO. OF COMPARTMENTS: 1 NO. OF BAGS PER COMPARTMENT: 124 LENGTH OF BAG (IN.): 144

DIAMETER OF BAG (IN.): 3"x6" oval DRAFT: INDUCED/NEG. FORCED/POS. FILTER SURFACE AREA (FT2): 1911

AIR TO CLOTH RATIO: 5.2 : 1 FILTER MATERIAL: 16 oz polyester felt WOVEN FELTED

DESCRIBE CLEANING PROCEDURES Either Air Pulse or Reverse Flow AIR PULSE SONIC

REVERSE FLOW SIMPLE BAG COLLAPSE

MECHANICAL/SHAKER RING BAG COLLAPSE - OTHER 20

DESCRIBE INCOMING AIR STREAM: 25Pnumatic transfer to cyclone seperator that drops the ash out of the air stream 25and into the silo. Air is displaced from the silo throught the filter as it fills with ash. 30Air is drawn into the silo through the filter as ash is removed from the silo. -

METHOD FOR DETERMINING WHEN TO CLEAN: Ether Automatic or Timed

AUTOMATIC TIMED MANUAL

METHOD FOR DETERMINING WHEN TO REPLACE THE BAGS:

ALARM INTERNAL INSPECTION VISIBLE EMISSION OTHER

SPECIAL CONDITIONS: MOISTURE BLINDING CHEMICAL RESISTIVITY OTHER

EXPLAIN: N/A

>100

TOTAL = 100

1-10

10-25

25-50



CUMULATIVE

(MICRONS)

50-100

OF TOTAL %WEIGHT %

0-1

ON A SEPARATE PAGE, ATTACH A DIAGRAM SHOWING THE RELATIONSHIP OF THE CONTROL DEVICE TO ITS EMISSION SOURCE(S):

FORM C1CONTROL DEVICE (FABRIC FILTER)


OPERATING SCENARIO:

SIZE

P.E. SEAL REQUIRED (PER 2Q .0112)? YES NO

YES NO WARNING ALARM? YES NO

DESCRIBE MAINTENANCE PROCEDURES: Check Filter Bag, Bag Cage and Housing Condition. Replace worn or teared bags. Replace and repair defective components.


REVISED 12/01/01 BEMISSION SOURCE ID NO: A8-A11& A13CONTROL DEVICE ID NO(S): C31, C33EMISSION POINT (STACK) ID NO(S): EPA8-A11




START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):_


SOURCE OFEMISSION




OTHER

SOURCE OFEMISSION



LEAD

EXPECTED ACTUAL



lb/day




EMISSION SOURCE DESCRIPTION: Unit 7 Fly Ash Handling (Controlled)

See Appendix G for process diagram. Sources include the following:A8: Dry Fly Ash Pickup at Boiler Economizer - Fly ash pneumatically conveyed to silo A9: Dry Fly Ash Pickup at Precipitator - Fly ash pneumatically conveyed to silo A10: Dry Fly Ash Piping to Fly Ash Silo - Fly ash pneumatically conveyed to siloA11: Fly Ash Silo to truck loadingA13: Fly Ash Silo to rail car loading











lb/hr

REVISED 12/01/01 B6EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: A8-A11 & A13

Unit 7 Fly Ash Silo and conveyors CONTROL DEVICE ID NO(S): CD31

OPERATING SCENARIO: ________1______ OF ______1_________ EMISSION POINT(STACK) ID NO(S): EP-A8-A11


See Appendix G for process diagram. Sources include the following:

A8: Dry Fly Ash Pickup at Boiler Economizer - Fly ash pneumatically conveyed to silo

A9: Dry Fly Ash Pickup at Precipitator - Fly ash pneumatically conveyed to silo

A10: Dry Fly Ash Piping to Fly Ash Silo - Fly ash pneumatically conveyed to silo

A11: Fly Ash Silo to truck loading

A13: Fly Ash Silo to rail car loading

MATERIAL STORED: Fly Ash DENSITY OF MATERIAL (LB/FT3): 80

CUBIC FEET: TONS:


ACTUAL: ~284,000/each MAXIMUM DESIGN CAPACITY:


COMPRESSOR BELT CONVEYOR TRUCK

OTHER: BUCKET ELEVATOR STORAGE PILE

OTHER: OTHER:

NO. FILL TUBES:

MAXIMUM ACFM:

MATERIAL IS FILLED TO:


Material is mixed with water and dropped into an open bed truck. The truck is then tarpped for transport.

Material can also be withdrawn through a dustless unloader into an enclosed pneumatic tank truck or rail car for shipment.


MAXIMUM DESIGN UNLOADING RATE OF MATERIAL (TONS/HR): 200

COMMENTS:




CAPACITY

DIMENSIONS (FEET)

MOTOR HP:


REVISED 12/01/01 C1CONTROL DEVICE ID NO: C31 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): A8-A11

EMISSION POINT (STACK) ID NO(S): EPA8-A11 POSITION IN SERIES OF CONTROLS NO. 1 OF 1 UNITS




___1____ OF __1_____

Bin Vent fabric filter to control emissions from the Unit #7 fly ash silo.










POLLUTANT LOADING RATE: 10 LB/HR GR/FT3 OUTLET TEMPERATURE (oF): MIN MAX ambientINLET AIR FLOW RATE (ACFM): NA FILTER MAX OPERATING TEMP. (oF): 275












SPECIAL CONDITIONS:

MOISTURE BLINDING CHEMICAL RESISTIVITY OTHER

EXPLAIN: N/A




OPERATING SCENARIO:

SIZE







CUMULATIVE

(MICRONS)

50-100

OF TOTAL %WEIGHT %

0-1

>100

TOTAL = 100

1-10

10-25

25-50

REVISED 12/01/01 C1CONTROL DEVICE ID NO: C33 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): A13

EMISSION POINT (STACK) ID NO(S): EP- A13 POSITION IN SERIES OF CONTROLS NO. 1 OF 1 UNITS




___1____ OF __1_____

Bin Vent fabric filter to control emissions from the rail car fly ash silo.










POLLUTANT LOADING RATE: 10 LB/HR GR/FT3 OUTLET TEMPERATURE (oF): MIN MAX ambientINLET AIR FLOW RATE (ACFM): NA FILTER MAX OPERATING TEMP. (oF): 275












SPECIAL CONDITIONS:


EXPLAIN: N/A

>100

TOTAL = 100

1-10

10-25

25-50



CUMULATIVE

(MICRONS)

50-100

OF TOTAL %WEIGHT %

0-1




OPERATING SCENARIO:

SIZE





REVISED 12/01/01 BEMISSION SOURCE ID NO: A7, A12, A14CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive




START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: TBDMANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):_


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION



LEAD

EXPECTED ACTUAL


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;

lb/day




EMISSION SOURCE DESCRIPTION: Two Fly Ash Discharges to Truck

See Appendix G for process diagram. Emissions provided below are for one truck discharge or one rail discharge. Only one dischage point will be used at any one time.











lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: A7, A12, A14

Two Fly Ash Discharges to Truck CONTROL DEVICE ID NO(S):

EMISSION POINT (STACK) ID NO(S): Fugitive

DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM): See Appendix G for process diagram. Process rates for one truck discharge.

UNITS

Fly Ash tons 200 NA

UNITS











REQUESTED CAPACITY



LIMITATION(UNIT/HR)

MAX. DESIGN


REVISED 12/01/01 BEMISSION SOURCE ID NO: VF1-VF32CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): NA






SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION



LEAD

EXPECTED ACTUAL



lb/day




EMISSION SOURCE DESCRIPTION: Coal Reclaim Feeders for Coal Stacking Tubes

See Appendix G for process diagram. No emissions are expected from the reclaim feeders as they are enclosed devices that discharge to a belt that is enclosed underground in a tunnel. The following feeders service the following stacking tubes:VF1-VF8: Reclaim Feeder for Stacking Tube 1 (ST1)VF9-VF16: Reclaim Feeder for Stacking Tube 2 (ST2)VF17-VF24: Reclaim Feeder for Stacking Tube 3 (ST3)VF25-VF32: Reclaim Feeder for Stacking Tube 4 (ST4)











lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: VF1-VF32

Coal Reclaim Feeders for Coal Stacking Tubes CONTROL DEVICE ID NO(S):

EMISSION POINT (STACK) ID NO(S): NA


UNITS

Coal tons 500 NA

UNITS











REQUESTED CAPACITY



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagram. No emissions are expected from the reclaim feeders as they are enclosed devices that discharge to a belt that is enclosed underground in a tunnel. The following feeders service the following stacking tubes:VF1-VF8: Reclaim Feeder for Stacking Tube 1 (ST1)VF9-VF16: Reclaim Feeder for Stacking Tube 2 (ST2)VF17-VF24: Reclaim Feeder for Stacking Tube 3 (ST3)VF25-VF32: Reclaim Feeder for Stacking Tube 4 (ST4)

REVISED 12/01/01 BEMISSION SOURCE ID NO: LSBM-3CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): NA




START CONSTRUCTION DATEJanuary 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):_OOO______ NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION






lb/hr




EXPECTED OP. SCHEDULE: __24__ HR/DAY __7_ DAY/WK ___52__ WK/Y





EMISSION SOURCE DESCRIPTION: Limestone Handling - Limestone Ball Mill Train No 3

See Appendix G for process diagram. Two ball mill trains will be installed with the Unit 5 modification. An additional ball mill train will be added for the Unit 6&7 project. No emissions are expected from the ball mill trains.






LEAD

EXPECTED ACTUAL



lb/day

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: LSBM-3

Limestone Handling - Limestone Ball Mill Train No 3 CONTROL DEVICE ID NO(S):

EMISSION POINT (STACK) ID NO(S): NA


UNITS

Limestone tons 60 NA

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagram. Two ball mill trains will be installed with the Unit 5 modification. An additional ball mill train will be added for the Unit 6&7 project. No emissions are expected from the ball mill trains.







REQUESTED CAPACITY

REVISED 12/01/01 BEMISSION SOURCE ID NO: LS13-3CONTROL DEVICE ID NO(S): CD32-3EMISSION POINT (STACK) ID NO(S): LS13-3






SOURCE OFEMISSION




OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Limestone Silo No. 3

See Appendix G for process diagram. Emissions from one limestone silo equiped with a bin vent filter.





1 Emissions are based on material charge rate and density of material charged.Attach Additional Sheets As Necessary



lb/hr

REVISED 12/01/01 B6EMISSION SOURCE ID NO: LS13-3

CONTROL DEVICE ID NO(S): CD32-3

OPERATING SCENARIO: _______1_______ OF ______1_________ EMISSION POINT(STACK) ID NO(S): LS13-3


MATERIAL STORED: Limestone DENSITY OF MATERIAL (LB/FT3): 85

CUBIC FEET: TONS: 1,100


ACTUAL: #### MAXIMUM DESIGN CAPACITY:


COMPRESSOR X BELT CONVEYOR TRUCK

OTHER: BUCKET ELEVATOR X STORAGE PILE

OTHER: OTHER:

NO. FILL TUBES:

MAXIMUM ACFM:

MATERIAL IS FILLED TO: Limestone Prep System


Gravity


MAXIMUM DESIGN UNLOADING RATE OF MATERIAL (TONS/ 80

COMMENTS:

MOTOR HP:





EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Limestone Silo No. 3

CAPACITY

See Appendix G for process diagram. Emissions from one limestone silo equiped with a bin vent filter.

DIMENSIONS (FEET)

REVISED 12/01/01 C1CONTROL DEVICE ID NO: CD32-3 CONTROLS EMISSIONS FROM WHICH EMISSION SOURCE ID NO(S): LS13-3

EMISSION POINT (STACK) ID NO(S): LS13-3 POSITION IN SERIES OF CONTROLS NO. 1 OF 1 UNITS


DATE MANUFACTURED 2007 PROPOSED OPERATION DATE:2011

PROPOSED START CONSTRUCTION DATE: January 2007

___1___ OF ____1___

One bin vent fabric filter to control emissions from the limestone silo.










POLLUTANT LOADING RATE: 10 LB/HR GR/FT3 OUTLET TEMPERATURE (oF): MIN MAX ambientINLET AIR FLOW RATE (ACFM): 10,000 FILTER MAX OPERATING TEMP. (oF): 275




DESCRIBE CLEANING PROCEDURES:

AIR PULSE OR SONIC



DESCRIBE INCOMING AIR STREAM: 25

Remove particles from LS Prep Bldg prior to exhausting building air to atmosphere. 25

30

-


AUTOMATIC OR TIMED MANUAL



SPECIAL CONDITIONS:


EXPLAIN: N/A

>100

TOTAL = 100

1-10

10-25

25-50



CUMULATIVE

(MICRONS)

50-100

OF TOTAL %WEIGHT %

0-1




OPERATING SCENARIO:

SIZE





REVISED 12/01/01 BEMISSION SOURCE ID NO: LS15CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive






SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Hydraulic Conveyor to FGD Area Emissions

See Appendix G for process diagrams. Fugitive emissions from hydraulic conveyor to FGD area. Limestone is transferred in a slurry. No emissions are expected from process.








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: LS15




UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

Limestone 300



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagrams. Fugitive limestone handling emissions include material handling from hydraulic conveyor to FGD area. Limestone is transferred in a slurry.

EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Hydraulic Conveyor to FGD Area Emissions

REVISED 12/01/01 BEMISSION SOURCE ID NO: GS10CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive




START CONSTRUCTION DATEJanuary 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):_______ NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION






lb/hr









EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Belt Filter Discharge

See Appendix G for process diagrams. Fugitive emissions from discharge of the two gypsum belt filters. Gypsum is transferred using screw conveyors. No emissions are expected from this source.






LEAD

EXPECTED ACTUAL



lb/day

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: GS10




UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Belt Filter Discharge





REQUESTED CAPACITY

Fugitive

See Appendix G for process diagrams. Fugitive emissions from discharge of the two gypsum belt filters. Gypsum is transferred using screw conveyors. No emissions are expected from this source.

Gypsum 142



REVISED 12/01/01 BEMISSION SOURCE ID NO: FvehicleCONTROL DEVICE ID NO(S): NAEMISSION POINT (STACK) ID NO(S): Fugitive

DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):All roads are currently assumed to be paved. Facility is assumed to have a road washing/cleaning program.Coal and limestone are provided via rail. Fugitive dust emissions from these deliveries are assumed insignificant.For delivery vehicles of fuel oil, acid/caustic, and ammonia, the number of deliveries (per substance) was estimated at 2 deliveries per day.



START CONSTRUCTION DATE NA OPERATION DATE: NA DATE MANUFACTURED: NAMANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):______


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION















EMISSION SOURCE DESCRIPTION: Fugitive Vehicle Emissions


LEAD

EXPECTED ACTUAL


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;

lb/day

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: Fvehicle

Fugitive Vehicle Emissions CONTROL DEVICE ID NO(S): NA


DESCRIBE IN DETAIL THE PROCESS (ATTACH FLOW DIAGRAM):All roads are currently assumed to be paved. Facility is assumed to have a road washing/cleaning program.Coal and limestone are provided via rail. Fugitive dust emissions from these deliveries are assumed insignificant.For delivery vehicles of fuel oil, acid/caustic, and ammonia, the number of deliveries (per substance) was estimated at 2 deliveries per day.

UNITS

UNITS



FUEL USED: TOTAL MAXIMUM FIRING RATE (MILLION BTU/HR):

MAX. CAPACITY HOURLY FUEL USE: REQUESTED CAPACITY ANNUAL FUEL USE:COMMENTS:



LIMITATION(UNIT/HR)

MAX. DESIGN








REQUESTED CAPACITY



Coal,wood,oil, gas, other burner (Form Woodworking (Form B4) Manufact. of chemicals/coatings/inks (Form B7)

Int.combustion engine/generator (Form Coating/finishing/printing (Form Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) X Other (Form B9)

START CONSTRUCTION DAJanuary 2007 OPERATION DATE: 2011 DATE MANUFACTURE 2007MANUFACTURER / MODEL NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):___Y____ NESHAP (SUBPART?):________ MACT (SUBPART?):_______

EXPECTED ANNUAL HOURS OF OPER< 8760

SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/hr









EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Unloading Emissions

See Appendix G for process diagrams. Fugitive emissions from rail car unloading.





ETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH S

LEAD

EXPECTED ACTUAL


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

lb/day

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTIOFugitive Coal Handling - Unloading Emissions EMISSION SOURCE ID NO: C1




UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagrams. Fugitive emissions from rail car unloading.





REQUESTED CAPACITY

Coal 5000



REVISED 12/01/0 BEMISSION SOURCE ID NO: C2, C4, C6, C8CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NOFugitive






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Conveyor Emissions

See Appendix F for process diagrams. Fugitive emissions from coal handling conveyors. The length of each of the conveyors is as follows: C2 : Stockout conveyor SC1 - 900 ft C4 : Stockout conveyor SC2 - 400 ft C6 : Stockout conveyor SC3 - 450ft C8 : Stockout conveyor SC4 - 550 ft








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTIOFugitive Coal Handling - Conveyor Emissions EMISSION SOURCE ID NO: C2, C4, C6, C8




UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

Coal 5000



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix F for process diagrams. Fugitive emissions from coal handling conveyors. The length of each of the conveyors is as follows: C2 : Stockout conveyor SC1 - 900 ft C4 : Stockout conveyor SC2 - 400 ft C6 : Stockout conveyor SC3 - 450ft C8 : Stockout conveyor SC4 - 550 ft

REVISED 12/01/0 BEMISSION SOURCE ID NO: C3, C5, C7, C9CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO Fugitive






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/hr









EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Stacking Tube Emissions

See Appendix F for process diagrams. Fugitive emissions from coal stacking tubes. Each stacking tube is 130 ft high and the capacities are as follows : C3 : Stacking Tube ST1 - 98, 000 ton @ 50 PCF (conical pile) C5 : Stacking Tube ST2 - 98, 000 ton @ 50 PCF (conical pile) C7 : Stacking Tube ST3 - 98,000 ton @ 50 PCF (conical pile) C9 : Stacking Tube ST4 - 98, 000 ton @ 50 PCF (conical pile)






LEAD

EXPECTED ACTUAL



lb/day

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: C3, C5, C7, C9

Fugitive Coal Handling - Stacking Tube Emissions CONTROL DEVICE ID NO(S):



UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix F for process diagrams. Fugitive emissions from coal stacking tubes. Each stacking tube is 130 ft high and the capacities are as follows : C3 : Stacking Tube ST1 - 98, 000 ton @ 50 PCF (conical pile) C5 : Stacking Tube ST2 - 98, 000 ton @ 50 PCF (conical pile) C7 : Stacking Tube ST3 - 98, 000 ton @ 50 PCF (conical pile) C9 : Stacking Tube ST4 - 98, 000 ton @ 50 PCF (conical pile)





REQUESTED CAPACITY

Fugitive

Coal 5,000









SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) NA NA NA NAPARTICULATE MATTER<10 MICRONS (PM10) NA NA NA NAPARTICULATE MATTER<2.5 MICRONS (PM2.5)SULFUR DIOXIDE (SO2)NITROGEN OXIDES (NOx)CARBON MONOXIDE (CO)VOLATILE ORGANIC COMPOUNDS (VOC)

OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Coal Handling - Reclaim Conveyor Emissions

See Appendix F for process diagrams. Fugitive emissions from reclaim conveyor to the transfer house. The reclaim conveyor to the transfer house is located underground. No emissions are expected from this source.








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: C13

Fugitive Coal Handling - Reclaim Conveyor Emissions CONTROL DEVICE ID NO(S):



UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

See Appendix F for process diagrams. Fugitive emissions from reclaim conveyor to the transfer house. The reclaim conveyor to the transfer house is located underground. No emissions are expected from this source.

Coal 1000



LIMITATION(UNIT/HR)

MAX. DESIGN


REVISED 12/01/01 BEMISSION SOURCE ID NO: GS3, GS4CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive






SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Stockout Conveyor and Radial Stacker Emissions

See Appendix G for process diagrams. Fugitive emissions from gypsum stockout conveyor and radial stacker. The stockout conveyor (GSC1) is 850 ft in length. The radial stacker is 70 ft high and has capacity of 10, 000 tons @ 70 PCF. Belt width is 30 inches.








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: GS3, GS4




UNITS

tons

UNITS











REQUESTED CAPACITY

Gypsum 300



LIMITATION(UNIT/HR)

MAX. DESIGN


EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Stockout Conveyor and Radial Stacker Emissions

See Appendix G for process diagrams. Fugitive emissions from gypsum stockout conveyor and radial stacker. The stockout conveyor (GSC1) is 850 ft in length. The radial stacker is 70 ft high and its capacity is 10, 000 tons @ 70 PCF. Belt width is 30 inches.







SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION






lb/hr









EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Truck Loading Emissions

See Appendix G for process diagrams. Fugitive emissions from gypsum truck loading.






LEAD

EXPECTED ACTUAL



lb/day





UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


EMISSION SOURCE DESCRIPTION:Fugitive Gypsum Handling - Truck Loading Emissions





REQUESTED CAPACITY

Fugitive

See Appendix G for process diagrams. Fugitive emissions from gypsum truck loading.

Gypsum 300







START CONSTRUCTION DATEJanuary 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):___Y____ NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Gypsum to Rail Car Emissions

See Appendix G for process diagrams. Fugitive emissions from gypsum loading to rail car.








lb/hr





UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

Gypsum 300



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagrams. Fugitive emissions from gypsum loading to rail car.

EMISSION SOURCE DESCRIPTION: Fugitive Gypsum Handling - Gypsum to Rail Car Emissions

REVISED 12/01/01 BEMISSION SOURCE ID NO: LS1CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive






SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION




LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Rail Car Unloading Emissions

See Appendix G for process diagrams. Fugitive emissions from limestone rail car unloading.








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: LS1




UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

See Appendix G for process diagrams. Fugitive emissions from limestone rail car unloading.

Limestone 2800



LIMITATION(UNIT/HR)

MAX. DESIGN


EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Rail Car Unloading Emissions

REVISED 12/01/01 BEMISSION SOURCE ID NO: LS2, LS3 (existing)CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive






SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION






lb/hr









EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Stockout Conveyor and existing Transfer House

See Appendix G for process diagrams. Fugitive emissions from limestone stockout conveyor and existing transfer house. The stockout conveyor LSC1 is 250 ft in length. Belt width is 54 inches.






LEAD

EXPECTED ACTUAL



lb/day

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: LS2, LS3




UNITS

tons

UNITS







LIMITATION(UNIT/HR)

MAX. DESIGN


EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Stockout Conveyor and Transfer House

See Appendix G for process diagrams. Fugitive emissions from limestone stockout conveyor and existing transfer house. The stockout conveyor LSC1 is 250 ft in length. Belt width is 54 inches.





REQUESTED CAPACITY

Limestone 2800



REVISED 12/01/0 BEMISSION SOURCE ID NO: LS6, LS7CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): Fugitive


Coal,wood,oil, gas, other burner (Form B1 Woodworking (Form B4) Manufact. of chemicals/coatings/inks (Form B7)

Int.combustion engine/generator (Form B2 Coating/finishing/printing (Form Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) X Other (Form B9)

START CONSTRUCTION DATE:January 2007 OPERATION DATE: 2011 DATE MANUFACTURE 2007MANUFACTURER / MODEL NO. NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?):_OOO______ NESHAP (SUBPART?):________ MACT (SUBPART?):_______

EXPECTED ANNUAL HOURS OF OPERATI < 8760

SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION



PLETE THIS FORM AND COMPLETE AND ATTACH APPROPRIATE B1 THROUGH B9 FORM FOR EACH SO

LEAD

EXPECTED ACTUAL



lb/day









EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Stockout Conveyor and Radial Stacker Emissions

See Appendix G for process diagrams. Fugitive emissions from limestone stockout conveyor and radial stacker. The stockout conveyor LSC2 is 100 ft in length and 54 inches wide. The stacking tube ST5 is 80 ft high and has capacity of 60,000 tons at 65 PCF.








lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE ID NO: LS6, LS7




UNITS

tons

UNITS











REQUESTED CAPACITY

Fugitive

Limestone 2800



LIMITATION(UNIT/HR)

MAX. DESIGN


See Appendix G for process diagrams. Fugitive emissions from limestone stockout conveyor and radial stacker. The stockout conveyor LSC2 is 100 ft in length and 54 inches wide. The stacking tube ST5 is 80 ft high and has capacity of 60,000 tons at 65 PCF.

EMISSION SOURCE DESCRIPTION: Fugitive Limestone Handling - Stockout Conveyor Emissions

REVISED 12/01/01 BEMISSION SOURCE ID NO: FLandfillCONTROL DEVICE ID NO(S):

EMISSION POINT (STACK) ID NO(S):DESCRIBE IN DETAILTHE EMISSION SOURCE PROCESS (ATTACH FLOW DIAGRAM):



START CONSTRUCTION DATE NA OPERATION DATE: NA DATE MANUFACTURED: NAMANUFACTURER / MODEL NO.: NAIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): NESHAP (SUBPART?):________ MACT (SUBPART?):


SOURCE OFEMISSION



OTHER

SOURCE OFEMISSION



LEAD

EXPECTED ACTUAL



lb/day




EMISSION SOURCE DESCRIPTION: Landfill Emissions

Increased fugitive emissions are expected from the addition of Units 6 & 7. Landfill emissions include dumping of material from delivery vehicle to active landfill cell and active cell storage.

OPERATING SCENARIO ______1___________OF ________1__________Fugitive










lb/hr

REVISED: 12/01/01 B9EMISSION SOURCE DESCRIPTION: EMISSION SOURCE ID NO: FLandfill

Landfill Emissions CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S):


UNITS

Coal Combustion Products acres 12

UNITS











REQUESTED CAPACITY



LIMITATION(UNIT/HR)

MAX. DESIGN


Increased fugitive emissions are expected from the addition of Units 6 & 7. Landfill emissions include dumping of material from delivery vehicle to active landfill cell and active cell storage.

Fugitive

REVISED 12/01/01 BEMISSION SOURCE ID NO: QP6CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): EP-QP6



X Int.combustion engine/generator (Form B2) Coating/finishing/printing (Form B5) Incineration (Form B8) Liquid storage tanks (Form B3) Storage silos/bins (Form B6) Other (Form B9)

START CONSTRUCTION DATE January 2007 OPERATION DATE: 2011 DATE MANUFACTURED: 2007MANUFACTURER / MODEL NO.: TBDIS THIS SOURCE SUBJECT TO? NSPS (SUBPART?): IIII NESHAP (SUBPART?):________ MACT (SUBPART?):__________


SOURCE OFEMISSION

AIR POLLUTANT EMITTED FACTOR lb/hr tons/yr lb/hr tons/yr lb/hr tons/yrPARTICULATE MATTER (PM) NSPS 0.23 0.01 - - 0.23 0.01PARTICULATE MATTER<10 MICRONS (PM10) 2 1.16 0.06 - - 1.16 0.06PARTICULATE MATTER<2.5 MICRONS (PM2.5) NA NA NA NA NA NASULFUR DIOXIDE (SO2) 8 0.01 4.00E-04 - - 0.01 4.00E-04NITROGEN OXIDES (NOx) NSPS 4.63 0.23 - - 4.63 0.23CARBON MONOXIDE (CO) NSPS 4.01 0.20 - - 4.01 0.20VOLATILE ORGANIC COMPOUNDS (VOC) NSPS 4.63 0.23 - - 4.63 0.23

OTHER

SOURCE OFEMISSION


TOXIC AIR POLLUTANT AND CAS NO. EF SOURCEDuke Power is not proposing changes to previously permitted TAP emission due to this modification.

EXPECTED OP. SCHEDULE: ___ HR/DAY ___ DAY/WK ___ WK/YR



lb/day



POTENTIAL EMSSIONSEXPECTED ACTUAL




EMISSION SOURCE DESCRIPTION: Unit 6 Emergency Quench Water Pump

A new 700 hp diesel engine driven emergency quench water pump for Unit 6 will be installed. Duke requests an annual operation limit of 100 hours (including testing)


(AFTER CONTROLS / LIMITS) (AFTER CONTROLS / LIMITS)



LEAD

EXPECTED ACTUAL




lb/hr

REVISED 12/01/01 B2EMISSION SOURCE DESCRIPTIONUnit 6 Emergency Quench Water Pump EMISSION SOURCE ID NO: QP6


OPERATING SCENARIO: ______1________ OF _____1_________ EMISSION POINT (STACK) ID NO(S): EP-QP6

CHECK ALL THAT APPLY X EMERGENCY SPACE HEAT ELECTRICAL GENERATION

PEAK SHAVER OTHER (DESCRIBE): ___________________

GENERATOR OUTPUT (KW): ANTICIPATED ACTUAL HOURS OF OPERATION AS PEAK SHAVER (HRS/YR):

ENGINE OUTPUT (HP): 700

TYPE ICE: GASOLINE ENGINE DIESEL ENGINE UP TO 600 H X DIESEL ENGINE GREATER THAN 600 HP DUAL FUEL ENGINE

OTHER (DESCRIBE): _________________________________________ (complete below)

ENGINE TYPE RICH BURN LEAN BURN

EMISSION REDUCTION MODIFICATIONS INJECTION TIMING RETAR PREIGNITION CHAMBER COMBUSTION OTHER _________

OR STATIONARY GAS TURBINE (complete below NATURAL GAS PIPELINE COMPRESSOR OR TURBINE (complete below)

FUEL NATURAL GAS OIL ENGINE TYPE: 2-CYCLE LEAN BURN 4-CYCLE LEAN TURBINE

OTHER (DESCRIBE):____________ 4-CYCLE RICH BURN OTHER (DESCRIBE): _______________

CYCLE: COGENERATION SIMPLE CONTROLS: COMBUSTION MODIFICATIONS (DESCRIBE): __________________

REGENERATIVE COMBINED NONSELECTIVE CATALYTIC REDUCTION SELECTIVE CATALYTIC REDUCTION

CONTROLS: WATER-STEAM INJECTION CLEAN BURN AND PRECOMBUSTION CHAMBER UNCONTROLLED

UNCONTROLLED LEAN-PREMIX

No 2 Fuel Oil Gallons 35.8 NA

No. 2 Fuel Oil 137,000 Gallon 0.0015

- - - - -

DESCRIBE METHODS TO MINIMIZE VISIBLE EMISSIONS DURING IDLING, OR LOW LOAD OPERATIONS:

COMMENTS:


FORM B2EMISSION SOURCE (INTERNAL COMBUSTION ENGINES/GENERATORS)

FUEL TYPE UNITSBTU/UNIT

FUEL USAGE (INCLUDE STARTUP/BACKUP FUEL)REQUESTED CAPACITY

FUEL TYPE UNITSMAXIMUM DESIGN

CAPACITY (UNIT/HR) LIMITATION (UNIT/HR)


CO PM PM10 VOCPOLLUTANT

EMISSION FACTOR LB/UNIT

FUEL CHARACTERISTICS (COMPLETE ALL THAT ARE APPLICABLE) SULFUR CONTENT

(% BY WEIGHT)

UNIT

NOX OTHER

MANUFACTURER'S SPECIFIC EMISSION FACTORS (IF AVAILABLE)

REVISED 12/01/01 BEMISSION SOURCE ID NO: QP7CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): EP-QP7






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/hr




LEAD

EXPECTED ACTUAL




EMISSION SOURCE DESCRIPTION: Unit 7 Emergency Quench Water Pump

A new 700 hp diesel engine driven emergency quench water pump for Unit 7 will be installed. Duke requests an annual operation limit of 100 hours (including testing)





lb/day




REVISED 12/01/01 B2EMISSION SOURCE DESCRIPTIONUnit 7 Emergency Quench Water Pump EMISSION SOURCE ID NO: QP7


OPERATING SCENARIO: ______1________ OF _____1_________ EMISSION POINT (STACK) ID NO(S): EP-QP7


















- - - - -


COMMENTS:


(% BY WEIGHT)

UNIT

NOX OTHER


MAXIMUM DESIGNCAPACITY (UNIT/HR) LIMITATION (UNIT/HR)








FUEL TYPE UNITS

REVISED 12/01/01 BEMISSION SOURCE ID NO: EG1CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): EP-EG1






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/day







EMISSION SOURCE DESCRIPTION: Emergency Diesel Fired Generator No. 1

A new 750 kw (1000 hp) emergency diesel fired generator will be used for emergency power at the facility.





LEAD

EXPECTED ACTUAL




lb/hr

REVISED 12/01/01 B2EMISSION SOURCE DESCRIPTIONEmergency Diesel Fired Generator No. 1 EMISSION SOURCE ID NO: EG1


OPERATING SCENARIO: ______1________ OF _____1_________ EMISSION POINT (STACK) ID NO(S): EP-EG1

CHECK ALL THAT APPLY X EMERGENCY SPACE HEAT X ELECTRICAL GENERATION















No 2 Fuel Oil Gallons 51 NA


- - - - -


COMMENTS:











(% BY WEIGHT)

UNIT

NOX OTHER


REVISED 12/01/01 BEMISSION SOURCE ID NO: EG2CONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): EP-EG2






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/hr




LEAD

EXPECTED ACTUAL




EMISSION SOURCE DESCRIPTION: Emergency Diesel Fired Generator No. 2

A new 750 kw (1000 hp) emergency diesel fired generator for emergency power at the facility.





lb/day




REVISED 12/01/01 B2EMISSION SOURCE DESCRIPTIONEmergency Diesel Fired Generator No. 2 EMISSION SOURCE ID NO: EG2


OPERATING SCENARIO: ______1________ OF _____1_________ EMISSION POINT (STACK) ID NO(S): EP-EG2

CHECK ALL THAT APPLY X EMERGENCY SPACE HEAT X ELECTRICAL GENERATION















No 2 Fuel Oil Gallons 51 NA


- - - - -


COMMENTS:


(% BY WEIGHT)

UNIT

NOX OTHER


MAXIMUM DESIGNCAPACITY (UNIT/HR) LIMITATION (UNIT/HR)








FUEL TYPE UNITS

REVISED 12/01/01 BEMISSION SOURCE ID NO: FWPCONTROL DEVICE ID NO(S):EMISSION POINT (STACK) ID NO(S): EP-FWP






SOURCE OFEMISSION


OTHER

SOURCE OFEMISSION






lb/day







EMISSION SOURCE DESCRIPTION: Emergency Diesel Fired Fire Water Pump

A new 1200 hp emergency diesel fired fire water pump. Duke requests an annual operation limit of 100 hours.





LEAD

EXPECTED ACTUAL




lb/hr

REVISED 12/01/01 B2EMISSION SOURCE DESCRIPTIONEmergency Diesel Fired Fire Water Pump EMISSION SOURCE ID NO: FWP


OPERATING SCENARIO: ______1________ OF _____1_________ EMISSION POINT (STACK) ID NO(S): EP-FWP


















- - - - -


COMMENTS:











(% BY WEIGHT)

UNIT

NOX OTHER


REVISED 12/01/01 D1

AIR POLLUTANT EMITTED

HAZARDOUS AIR POLLUTANT EMITTED CAS NO.

Hydrogen Chloride 3.44E+02 - 3.44E+02

Hydrogen Fluoride 4.48E+01 - 4.48E+01

Antimony 6.60E-02 - 6.60E-02

Arsenic 1.50E+00 - 1.50E+00

Beryllium 7.80E-02 - 7.80E-02

Cadmium 1.88E-01 - 1.88E-01

Chromium 9.54E-01 - 9.54E-01

Cobalt 3.67E-01 - 3.67E-01

Lead 1.54E+00 - 1.54E+00

Manganese 1.80E+00 - 1.80E+00Mercury 2.95E-01 - 2.95E-01

Nickel 1.03E+00 - 1.03E+00

Selenium 4.77E+00 - 4.77E+00

Acenapthene 5.43E-05 - 5.43E-05

Acenapththylene 1.44E-05 - 1.44E-05

Acetaldehyde 2.09E+00 - 2.09E+00

Acetophenone 5.50E-02 - 5.50E-02

Acrolein 1.06E+00 - 1.06E+00

Aldehydes 2.10E-01 - 2.10E-01

Ammonia 2.24E+02 - 2.24E+02

Anthracene 7.78E-04 - 7.78E-04

Benzene 4.77E+00 - 4.77E+00

Benz(a)Anthracene 1.42E-05 - 1.42E-05

Benz(A)Pyrene 5.20E-07 - 5.20E-07

Benzo(b)Fluoranthene 3.80E-06 - 3.80E-06

Benzo(g,h,i)perylene 1.06E-04 - 1.06E-04

Benzo(k)Fluoranthene 4.25E-07 - 4.25E-07

Benzyl Chloride 2.57E+00 - 2.57E+00

Biphenyl 6.23E-03 - 6.23E-03

Bis(2-ethylhexyl)phthalate 2.68E-01 - 2.68E-01

Bromoform 1.43E-01 - 1.43E-01

Carbon Disulfide 4.77E-01 - 4.77E-01

2-Chloroacetophenone 2.57E-02 - 2.57E-02

Chlorobenzene 8.07E-02 - 8.07E-02

Chloroform 2.16E-01 - 2.16E-01

(AFTER CONTROLS / LIMITATIONS)

HAZARDOUS AIR POLLUTANT EMISSIONS INFORMATION - FACILITY-WIDE

CRITERIA AIR POLLUTANT EMISSIONS INFORMATION - FACILITY-WIDE

FORM D1

tons/yr

3,069.44

tons/yr tons/yr

- 3,069.44PARTICULATE MATTER (PM)

FACILITY-WIDE EMISSIONS SUMMARY

45,284.30

13419.67 to 13977.67

45,284.30 -

-

-

SULFUR DIOXIDE (SO2)

NITROGEN OXIDES (NOx)1

CARBON MONOXIDE (CO) 11,275.64

VOLATILE ORGANIC COMPOUNDS (VOC)

1.69LEAD

2,562.87

NA

PARTICULATE MATTER < 10 MICRONS (PM10)

PARTICULATE MATTER < 2.5 MICRONS (PM2.5)

2,562.87

NA -

(BEFORE CONTROLS / LIMITATIONS)

(AFTER CONTROLS /LIMITATIONS)

tons/yrtons/yrtons/yr


EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS

EXPECTED ACTUAL EMISSIONS POTENTIAL EMISSIONS POTENTIAL EMISSIONS(AFTER CONTROLS /

LIMITATIONS)

13419.67 to 13977.67

345.08-

1.69-

345.08

11,275.64

-

(BEFORE CONTROLS / LIMITATIONS)

(AFTER CONTROLS /LIMITATIONS)

Cumene 1.94E-02 - 1.94E-02

Cyanide 9.17E+00 - 9.17E+00

2,4-Dinitrotoluene 1.03E-03 - 1.03E-03

Dimethyl Sulfate 1.76E-01 - 1.76E-01

Ethyl benzene 3.45E-01 - 3.45E-01

Ethyl Chloride (Chloroethane) 1.54E-01 - 1.54E-01

Ethylene Dichloride 1.47E-01 - 1.47E-01

Ethylene Dibromide 4.40E-03 - 4.40E-03

Formaldehyde 1.03E+00 - 1.03E+00

Hexane 2.46E-01 - 2.46E-01

Isophorone 2.13E+00 - 2.13E+00

Methyl Bromide (Bromomethane) 5.87E-01 - 5.87E-01

Methyl Chloride (Chloromethane) 1.94E+00 - 1.94E+00

Methyl Ethyl Ketone 1.43E+00 - 1.43E+00

Methyl Hydrazine 6.23E-01 - 6.23E-01

Methyl Methacrylate 7.33E-02 - 7.33E-02

Methyl tert-butyl ether 1.28E-01 - 1.28E-01

Methylene Chloride 1.06E+00 - 1.06E+00

Naphthalene 5.04E-02 - 5.04E-02

Phenanthrene 9.93E-03 - 9.93E-03

Phenol 5.87E-02 - 5.87E-02

Propionaldehyde 1.39E+00 - 1.39E+00

Styrene 9.17E-02 - 9.17E-02

Tetrachloroethylene 1.58E-01 - 1.58E-01

Toluene 8.95E-01 - 8.95E-01

1,1,1-Trichloroethane 7.39E-02 - 7.39E-02

Vinyl Acetate 2.79E-02 - 2.79E-02

Xylene 1.36E-01 - 1.36E-01

Total PCDD/PCDF 6.46E-06 - 6.46E-06

TOXIC AIR POLLUTANT EMITTED CAS NO. lb/hr lb/day lb/year Yes No

Hydrogen Chloride 78.51 1884.18 687726.11 No

Hydrogen Fluoride 10.22 245.36 89555.15 No

Arsenic 0.34 8.25 3009.85 No

Beryllium 0.02 0.43 156.07 No

Cadmium 0.04 1.03 376.01 No

Chromium 0.22 5.23 1908.87 No

Manganese 0.41 9.86 3597.71 No

Mercury 0.07 1.62 590.63 No

Nickel 0.23 5.63 2055.55 No

Acetaldehyde 0.48 11.47 4184.75 No

Acrolein 0.24 5.83 2127.44 No

Benzene 1.09 26.14 9540.86 No

Benzyl Chloride 0.59 14.07 5133.98 No

Carbon Disulfide 0.11 2.61 953.45 No

Chlorobenzene 0.02 0.44 161.35 No

Chloroform 0.05 1.19 432.72 No

Ethylene Dichloride 0.03 0.80 293.37 No

Ethylene Dibromide 0.00 0.02 8.80 No

Formaldehyde 0.23 5.62 2051.31 No

Hexane 0.06 1.35 491.40 No

Methyl Ethyl Ketone 0.33 7.84 2860.36 No

Methylene Chloride 0.44 10.65 3887.16 No

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 ?

TOXIC AIR POLLUTANT EMISSIONS INFORMATION - FACILITY-WIDE

Phenol 0.01 0.32 117.35 No

Styrene 0.02 0.50 183.36 No

Toluene 0.20 4.90 1789.81 No

Xylene 0.03 0.74 271.37 No

Sulfuric Acid 94.27 2262.48 825806.54 Yes

Ammonia 62.80 1507.20 550128.00 Yes


1 Nox emissions are provided as a range reflecting operation of Unit 5 during the 5 month ozone season.

COMMENTS:

Revised:12/01/01 NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate D2

AIR POLLUTANT: Sulfuric Acid

EMISSION SOURCE ID NOS.: U6 & U7

LB/YEAR LB/DAY

MODIFICATION 2262 94.2

INCREASE

- MINUS - - MINUS - - MINUS - - MINUS -

MODIFICATION

DECREASE

= EQUALS = = EQUALS = = EQUALS = = EQUALS =

NET CHANGE

FROM MODIFICATION

CREDITABLE

INCREASE



NET CREDITABLE

CHANGE

TOTAL FACILITY

2262 94.2

TPER LEVELS (2Q .0711) 0.25 0.025

CHECK HERE IF AN AIR DISPERSION MODELING ANALYSIS IS REQUIRED

CAS NO.:

PURPOSE OF NETTING: AIR TOXICS PSD (100/250 tons per year) PSD SIGNIFICANT LEVELS

EMISSIONS


LB/HR

COMMENTS:

FORM D2AIR POLLUTANT NETTING WORKSHEET

SECTION C - FACILITY-WIDE EMISSIONS

Summarize in this sectionusing the B forms

CREDITABLE

DECREASE

EMISSIONS - USE APPROPRIATE COLUMNS ONLY

SECTION A - EMISSION OFFSETTING ANALYSIS FOR MODIFIED/NEW SOURCES

SECTION B - FACILITY-WIDE EMISSION NETTING ANALYSIS

Revised:12/01/01 NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate D2

AIR POLLUTANT: ammonia

EMISSION SOURCE ID NOS.: U6 & U7

LB/YEAR LB/DAY

MODIFICATION

INCREASE 62.8


MODIFICATION

DECREASE


NET CHANGE

FROM MODIFICATION

CREDITABLE

INCREASE



NET CREDITABLE

CHANGE

TOTAL FACILITY

62.8

TPER LEVELS (2Q .0711) 0.68

CHECK HERE IF AN AIR DISPERSION MODELING ANALYSIS IS REQUIRED

FORM D2AIR POLLUTANT NETTING WORKSHEET

SECTION C - FACILITY-WIDE EMISSIONS

Summarize in this sectionusing the B forms

CREDITABLE

DECREASE

EMISSIONS - USE APPROPRIATE COLUMNS ONLY

SECTION A - EMISSION OFFSETTING ANALYSIS FOR MODIFIED/NEW SOURCES

SECTION B - FACILITY-WIDE EMISSION NETTING ANALYSIS

CAS NO.:

PURPOSE OF NETTING: AIR TOXICS PSD (100/250 tons per year) PSD SIGNIFICANT LEVELS

EMISSIONS


LB/HR

COMMENTS:

REVISED: 12/01/01

1. Two Emergency Generators 1000 hp each 2Q.0503(8)(Limited to 500 operating hours each)

2. One Emergency Firewater Pump Engine 1200 hp 2Q.0503(8)

3. Two WFGD Emergency Quench Water Pumps 700 hp each 2Q.0503(8)

4. Unit 6 & 7 Start-Up/Aux. Boiler Fuel Oil Tank 168,000 gallons 2Q.0503(8)

5. Two Emergency Diesel Generator Fuel Oil Tanks 1,640 gallons each 2Q.0503(8)

6. Emergency Fire Water Pump Fuel Oil Tank 350 gallons 2Q.0503(8)

7.

8.

9.

10.


DESCRIPTION OF EMISSION SOURCEBASIS FOR EXEMPTION OR

INSIGNIFICANT ACTIVITY

SIZE OR PRODUCTION

RATE

FORM D4

INSIGNIFICANT ACTIVITIES PER 2Q .0503 FOR TITLE V SOURCESACTIVITIES EXEMPTED PER 2Q .0102 OR

EXEMPT AND INSIGNIFICANT ACTIVITIES SUMMARY NCDENR/Division of Air Quality - Application for Air Permit to Construct/Operate D4

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