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HomeMy WebLinkAboutNC0001422_Modification Request 2008_20110131Progress Energy File No.: SUT 12520 -B -01 January 25, 2011 NCDENR -DWQ, Surface Water Protection Section 1617 Mail Service Center Raleigh, NC 27699 -1617 Subject: Carolina Power & Light Company d/b /a Progress Energy Carolinas, Inc. (Progress Energy) L. V. Sutton Electric Plant NPDES Permit NC0001422 Permit Modification Request Dear Mr. Jeffrey O. Poupart: Progress Energy requests modification of the subject permit to include planned changes at the L. V. Sutton Electric Plant, New Hanover County. Progress Energy has committed to retire the existing coal -fired generation units upon completion of a natural gas -fired 2x 1 combined cycle facility at this site. The purpose of this modification request is to add the wastewaters expected from the proposed combined cycle block to the existing permit so that planning and construction may begin. The new generation is expected to begin commercial operation in early 2014. Enclosed are three copies of the completed EPA Forms 1 and 2C, with attachments, for the proposed modified flows and a check for the required review fee of $1,030. Effluent pollutant characteristics provided on Form 2C for the future Outfall 001 discharge were developed using available data from the existing Outfall 001 discharge, the Cape Fear River, water supply wells, and by applying projected cycles of concentration typical of combined cycle operations. All low volume wastewaters from the new power block will be directed to the cooling pond via two new internal outfalls. The cooling pond will continue to serve as water supply and discharge point for the recirculated condenser cooling water. The existing Outfall 001, from the cooling pond to the Cape Fear River, will continue to be the only discharge to surface water. To accommodate the construction of the new power block, the wastewater currently flowing to the south retention basin will be redirected to the west retention basin. As required in NPDES Permit Requirements Part III Section E, Progress Energy is notifying DWQ by this letter that the south retention basin wastewater treatment system will be closed upon the relocation of the wastewater piping. Please contact Ms. Robin Bryson, Environmental Specialist in our corporate office, at (919) 546 -3962, if there are any questions with this submittal. I certify, under penalty of law, that this document and all attachments were prepared under my direction or supervision in accordance with a system designed to assure that qualified personnel properly gather and evaluate the information submitted. Based on my inquiry of the person or persons who manage the system, or those persons directly responsible for gathering the information, the information submitted is, to the best of my knowledge and belief, true, accurate, and complete. I am aware that there are significant penalties for submitting false information, including the possibility of fines and imprisonment for knowing violations. Sincerely, J. Mark Frederick, Plant Manager L. V. Sutton Electric Plant Progress Energy Carolinas, Inc. Sutton Steam Plact 801 Sutton Steam Plant Road Wilmington, NC 28401 JAN 3 1 2011 G>= NR- V1IF.i i=R QUALITY POINT SOURCE BRANCH Progress Energy Carolinas, Inc. NPDES Permit NC0001422 L. V. Sutton Electric Plant Permit Modification Application January 2011 Al -2 Progress Energy Carolinas, Inc. NPDES Permit NC0001422 L. V. Sutton Electric Plant Permit Modification Application January 2011 Attachment 2 Form 2C - Item II -A Flow, Sources of Pollution, and Treatment Technologies Water Average FlowZ Path' (MGD) Flow Comments A 49 Maximum river water makeup to cooling pond (intermittent) B 589 Water intake for the coal -fired units C 6 Ash sluice water routed to new ash pond — variable 0 -7 MGD D 6 Internal Outfall 004 —Ash sluice water from new ash pond — variable 2- 7 MGD (optionally routed to Outfall 001, cooling pond, or old ash pond) E 5 Discharge from new ash pond to cooling pond— variable 0 -6.5 MGD F 3 Ash sluice water routed to old ash pond — variable 0 -7 MGD G 0 Internal Outfall 002 — Discharge from old ash pond to cooling pond — variable 0 -7 MGD H 2 Alternate discharge to Outfall 001 — variable 0 -3 MGD 7 Non - contact cooling water (service water) for coal -fired units J 583 Heated water discharge from coal units condensers to cooling pond K 0.05 Supply well water withdrawal for coal -fired units L 0.17 Low volume waste waters from coal -fired units M 0.18 Maximum flow from the retention basin to the old ash pond N 0 Internal Outfall 003 — Chemical metal cleaning wastes are normally disposed of by evaporation in the boilers; Outfall 003 is an alternate for discharging into an ash pond (approximate 0.145 MGD per event) O 0.11 Coal pile and tank farm area runoff — estimated 80 dpy P 20.4 Rainfall on the cooling pond— estimated 80 dpy Q 10 Seepage from the cooling pond— estimated R 1.5 Evaporation from the cooling pond— estimated S 25 (Coal units); Outfall 001 — Discharge from cooling pond to the Cape Fear River - 12 (CC block) variable 0 -380 MGD T 0.003 (Coal units); County water for potable water and sanitary systems 0.002 (CC block) AA 0.67 Supply well water withdrawal for the combined cycle power block HH 0.07 Water treatment filter backwash to Internal Outfall 005 via low volume waste collection sump CC 0.29 Service water to the Closed Cooling Water Cooler (CCWC) A2 -1 Progress Energy Carolinas, Inc. L. V. Sutton Electric Plant NPDES Permit NC0001422 Permit Modification Application January 2011 Water Average Flow2 Path' (MGD) Flow Comments I f , 0.14 Closed cooling water cooler blowdown discharge to Interna Outfall 00 via low volume waste collection sump EE 0.14 Closed cooling water cooler evaporation and drift losses FF 0.28 Service water for combined cycle power block plant systems GG 0.11 Service water to blowdown tanks HH 0.198 Internal .Autfall 006 --Heat recovery steam generators blowdown tank discharger-- - - 11 0.033 Blowdown tank flash evaporation JJ 0.12 Demineralized water to Heat Recovery Steam Generators (HRSGs) KK 0.088 Heat recovery steam generators blowdown LL variable Heat recovery steam generators cleaning wastes MM 0.023 Heat recovery steam generators vent losses NN 0 -0.02 Auxiliary boiler blowdown 00 0.3 Oil /water separator discharge to Interna( Outfall 005 Via low volume waste collection sump PP 0.25 Demineralized water to Combined Turbine Generator (CTG) NOx injection system QQ 0.003 Combustion turbine generator wash water and false start losses RR 0.25 Combustion turbine generator NOx injection system water losses SS 0.09 Reverse Osmosis (RO) and ElectrQdeionization (EDI) water treatment system reject water to Internal Outfall 00 via low volume waste ' collection sump TT 288 Combined cycle power block recirculated condenser cooling water withdrawal from the cooling pond UU 288 Combined cycle power block recirculated condenser heated water discharge to the cooling pond VV 0.65 Internal Outfall 005 — Combined cycle power block wastewater discharge to the cooling pond WW 0.29 Low volume wastes from coal -fired units 'Water path color indication: Blue = Coal -fired units water paths Red = Combined cycle power block water paths Green = Conjoined systems water paths 2Average flow values for the combined cycle power block are estimated based on proposed plant design. A2 -2 Progress Energy Carolinas, Inc. L. V. Sutton Electric Plant Coal -fired units water paths Combined cycle block water paths Conjoined systems water paths NPDES Permit NC0001422 Permit Modification Application January 2011 Supply wells Non - contact cooling � 10 Bearing Watertreatment I `I Plant systems I water (service water) �` cooling system 111' Condensers lE - Fire system Retention basin Low volume (III 1 wastes Eva T Evaporation Chemical metal Circu ating Yard drains rnemical metal cleanin� waste water pumps I I cleaninI waste I %1 Internal Internal W Outfa11003 Outfall003 � � I New Ash Pond k--(Ash sluice system Intake structure Ash sluice system I Old Ash Pond [Q - - I I 1 "' I 11�� fff���lll I�F '� 1 Internal Screen wash 4-1 g O D Outfa11004 Makeup water I Coal pile & tank intake structure farm runoff Ta Seepage Cape Fear River A [&-".Evaporation Rainfall —a-* � Internal Outfall 002 Cooling Pond �J Screen wash Intake structure H S I Supply wells Condensers I Cape Fear River 1 Clutfall001 vv Internal `•i' Clutfall 005 filter water Filter backwash BOB 4ow volume waste treatmreatment system collection sump A F-(9)-* Evaporation CC Closed cooling DD water cooler Storm water 00 r IService water FF ;� Plant systems CC block low Oil /water storage tank u volume wastes separator Coal units sow II Evaporation volume wastes GG 1 -1 Blowdown tanks NF' KK Vent losses Auxiliary boiler I HRSGs LL IL RR Water loss- off -site disposal RO /EDI water Demin water pp CTG NOx injection treatment system storage tanks CTG wash &false start 545 losses- off -site disposal A2 -3 County water IPotable water I 1 1 Sanitary systems I Septic tanks 1 I Leach fields 1 I Infiltration Storm water Yard drains I 1 111 Internal HH Outfall 006 - Progress Energy Carolinas, Inc. NPDES Permit NC0001422 L. V. Sutton Electric Plant Permit Modification Application January 2011 Attachment 3 Form 2C - Item II -B Flow, Sources of Pollution,, and Treatment Technologies The L V Sutton Electric Plant has three coal -fired electric generating units and three Internal Combustion (IC) turbine units The plant has a 1,110 -acre (6,900 acre -ft) off - stream cooling pond on the east side of the Cape Fear'River approximately ten river miles upstream of Wilmington, North Carolina Water is withdrawn from the Cape Fear River, as required, to makeup evaporative, seepage, and blowdown losses from the cooling pond A natural gas -fired 2x1 Combined Cycle (CC) combustion turbine power block is scheduled to be built adjacent to the,existing coal -fired units and begin operation in 2014. Upon commercial operation of this new power block, the three coal- fired'units will be retired. Chemical constituents contained in the discharge from the permitted outfall will, in part, be representative of the naturally - occurring chemical quality and quantity of the intake water and will also have chemical constituents of such quality associated with, similar discharges forfossil generating facilities,of this size, type, and in this geographical location Either all or part of the elements in the Periodic Table, either singularly or in any combination, may from time to time be contained in the discharge The Sutton Plant currently has one permitted outfall to the Cape Fear River,, discharges from the cooling pond ( Outfall 001) which, receives all combined wastewaters. This outfall will remain the only permitted outfall with completion of the combined cycle block and the retirement of the three coal - fired units. Recirculated Condenser_Coolinq Water Condenser cooling water for the coal -fired units is withdrawn and discharged to the cooling pond The condenser cooling water for the new CC block will also be withdrawn and discharged to the cooling pond. The heated discharge is routed around baffle dikes within the cooling pond to achieve maximum surface cooling efficiency and before reaching the condenser cooling water intake structure to be recirculated Evaporation, which is estimated to consume approximately 5 5 MGD above natural evaporation rates during'times of full operation, effectively cools the heated water discharge Bioloqical oulmq control agents are used on heate_ xchanger surfaces Non - contact Cooling Water Non - contact cooling water is also withdrawn from and returned to the cooling pond This water provides indirect cooling for various coal -fired unit equipment.by absorbing heat as it passes through a heat exchanger No direct contact is made with any other'equipment or process Coal Pile Runoff Storm water runoff from the coal pile is routed to the old ash pond (1971 pond), which provides neutralization and sedimentation treatment During maintenance activities, sludge removed from catch basins, sumps, etc may be transported to }the old and /or- new ash pond (1984 pond) for disposal Storm Water Runoff Exempt storm water runoff from the plant'area including parking lots, ,switchyard, and the IC Turbine area is collected in yard drains which flow to the cooling pond All other °yard drains and plant drains from the coal -fired units, which may contain pollutants from spills or leakage from plant processes,are routed to the retention basin, and pumped from there to the ash ponds,for treatment Drains from the new CC block which may contain oil and grease are routed to an oil /water separator before discharging into the cooling pond via Internal Outfall 005. During maintenance activities, sludge removed from catch A3'A Progress Energy Carolinas, Inc. 'NPDES Permit NC0001422 L.M. Sutton Electric Plant Permit Modification Application January"2011 .L + basins, sumps, etc may be transported to the old and /or new ash pond for disposal from the existing plant or transported off -site from the CC block. Ash Sluice Water Fly ash and bottom ash from all three coal -fired units is hydraulically conveyed by,an ash sluice pipeline,to the new ash pond, which provides sedimentation and oxidation treatment Alternatively, fly and bottom ash may be conveyed to the old ash pond for treatment white maintenance activities are performed on the new ash pond A Rotamix urea infection system and a Rotating Over Fire Air (ROFA) System are installed on the Unit 3 boiler These systems are used jointly to employ high velocity air infection and urea to reduce Nitrogen Oxides (NOx-) emissions Any un- reacted ammonia will be absorbed into the fly ash and will be carried to the ash pond via ash sluice water -Currently, as part�of our'ash treatment systernme have a drip that feeds either acid or caustic (depending on season and type of coal burned) into the ash sluice line to help with the pH adjustment of the ash sluice water before it is discharged to the ash pond Alum may be added to the ash pond, or to the retention basin that flows to the ash pond, as required, to control total suspended solids concentrations Additional process water Will be sent through the ,fly ash sluice lines to boost the system Jet propulsion nozzles are used to overcome the new head pressure associated with the additional height of an ash restacking project as -well as to send the ash sluice water further away from the ash sluice pumps Ash Pond Discharge Effluent from the new ash pond ,can be discharged to either'the cooling pond or to the Cape Fear River When the effluent from the new ash pond is routed to the Cape Fear River, up to approximatelyA 0 MGD will still be discharged to the cooling pond Effluent from the old ash pond discharges to the cooling pond Coolma Pond Discharge Discharges via, Outfall 001 from the cooling pond'to the Cape Fear River occur on an ,intermittent basis This outfall will continue to be the sole discharge of wastewater to the Cape Fear River with the operation of the new combined cycle power block: Domestic Wastes Sanita y wastes are treated by an onsite septic tank and drainage field that is permitted by the New Hanover County Health Department The septage is exempt from the 40 CFR 503 standards Progress Energy Carolinas, Inc will submit appropriate information to,the EPA if required Low-Volume Wastes All waste streams not identified above are categorized as low- volume wastes These wastes include plant drains, which convey miscellaneous equipment leakage, equipment drainage for maintenance, equipment washdown water, sampling streams, service water'system blowdown, °and water °treatment wastes Coal -fired Units Process water used in the coal -fired units is treated prior to use by an ion- exchange demmeralizer which must be periodically regenerated with solutions of sodium chloride, sodium hydroxide, and sulfuric acid Alternatively a vendor may be used'to provide treatment of plant process water Blowdown of boiler water to control boiler chemistry is routed through low- volume prior to discharge in the ash pond Boiler vacuuming sediment is routed through low- volume prior to discharge to the ash ponds The precipitators, are water washed approximately every 1 to 3 years with the wastewater discharging to the ash pond Drains from areas likely to contain oil - filled equipment or storage are routed through an oil -water separator with the effluent routed through low volume prior to discharge to the ash pond Waste oil is A3 -2 Progress Energy Carolinas, Inc. NPDES Permit NC0001422 L. V. Sutton Electric Plant Permit Modification Application January 2011 disposed of according to the appropriate regulations During maintenance activities, sludges removed from catch basins, sumps, etc may be transported to the old and /or new-ash pond for disposal All low volume wastes described above are routed by gravity flows to the retention basin at the plant and then to,the ash ponds for treatment by neutralization, sedimentation, oxidation, and absorption The air pre- heaters and electrostatic precipitators ate water washed approximately every one to three years with the wastewater discharging to the ash pond via,the ash sluice lines In many cases added chemicals are consumed or chemically altered during the plant processes Only trace amounts might be recoverable in water entering the ash ponds Since the ash ponds serve ,as a final treatment basin and receives, significantly greater volumes of,water from other inflows, detectable levels of these chemicals would not occur in ash pond discharges Combined Cycle Power Block Process wastewaters generated in the natural gas combined cycle block will be discharged to the cooling pond Via two new internal outfalls. Low volume wastewaters including the ultrafilter water'treatment system filter backwash, Closed Cooling Water Cooler (CCWC) bl'owdown,, Reverse Osmosis /Electrodeionizatiom(RO /EDQ) system reject wastewater, and other wastewaters entering the oil /water °separator are directed to the low volume waste ection sump for discharge to the cooling' pond via Internal Outfall 005. l Low volume wastewaters including the Heat Recovery Steam Generator (HRSG) blowdown and auxiliary boiler blowdown will be discharged to the cooling pond via Internal Outfall 006. LIncidentalleaks associated with the•operation of the,HRSG, Combustion Turbine Generators RO /EDI system, and infrequent draining and cleaning of'various rocesses may wastewate al Outfall 005 uring the initial startup phase, HRSG blowdown of up to 1.5 MGD may be released to OUtfaill 006 for several days. Wastewater from routine HRSG cleaning,, fuel oil /water condensate, and equipment drains potentially containing oil is directed to plant drains which are treated by the oil %water separator. The combustion turbinefa Ise, start drains, NOx injection, and compressor waste water is directed to a holding tank�and transported off -site. For a more extensive cleaning, the HRSGs may require flushing with a large volume of water. The wastewater from this flushing would be discharged via Internal Outfall 005 to the cooling pond or taken off -site. Various equipment, including fuel oil storage tanks; transformers, lube oil filters, etc. have containment areas,for,spills. Storm water collected in these areas is visually inspected for the presence of oil prior,to release to the,ground or released to plant.drains which flow to the oil /water °separator. Laboratory processes produce small amounts of,wastewater which are routed to plant drains. Wash /rinse water from an on -site washing machine is also routed to plant drains. Chemical Metal Cleaninq Wastes The boilers. ar& chemically cleaned approximately every,5 to 10 years The cleaning solution and rinses, are stored ion site for disposal by evaporation in the boilers Should chemical metal cleaning wastes not be evaporated, they will be treated by neutralization and precipitation in retention basin prior to discharge to the ash ponds Fire Water Svstem Several plant `heat exchangers are cooled by the fire water system A3 -3 • Progress Energy Carolinas,'Inc. L. V. Sutton Electric Plant NPDES Permit NC0001422 Permit Modification Application January 2011 • Ash Reclamation In the event,a practicable market becomes available, Progress Energy Carolinas, Inc may exercise the option of "reclaiming ash from the ash ponds However,, due to the limited scope of such an operation no additional discharges would be expected Inactive Hazardous Waste Sites List Areas A former ash disposal area and the old ash pond were listed on the State's Inactive Hazardous Waste Sites List Pesticide Usaae in Sutton Coolina Pond Herbicides a "re used when needed to control nuisance aquatic vegetation These her',bicides are applied by licensed applicators, or persons under the immediate supervision of a licensed applicator, in accordance with the manufacturer's instructions Pesticides are used when needed to perform biological assessments of fish populations These pesticides are applied by licensed applicators, or persons under the immediate supervision of a licensed applicator, in accordance with the manufacturer's instructions A3-4 Progress Energy Carolinas, Inc. L. V. Sutton Electric Plant Chemical NPDES Permit NC0001422 Permit Modification Application•January 2011 Attachment 4 Form 2C - Item VI Potential Discharges 'Not Covered by Analysis Hydrazine Ammonia Phosphate Sodium hydroxide (50 %) Sodium hydroxide (50 %) Sulfuric acid (93 %) Alum Sulfuric acid (93 %) Sodium chloride Bromine /Chlorine [Biotrol 88P (1- bromo- 3-chloro-5,5-dimethylhydantoin)] Sodium hypochlonte Sodium molybdate and sodium nitrate Cleaner,(sodi(im hydroxide, metasilicate_, and ethlenediaminetetraacetic acid) Ethylene glycol Urea Citric Acid (50 %) Ammonium hydroxide Cronex Inhibitor Sodium nitrite Ammonium bicarbonate Citric Acid — dry Estimated Quantity (per year) Frequency Coal-fired Units 500 gals Continuous 220 gals Continuous 500 gals Continuous 6000 gals Weekly 2000 gals As needed 2000 gals As needed 1800 gals As needed 1700 gals Weekly 500 Ibs As needed 45001bs Weekly 3432 gals As needed 110 gals As needed 1000 gals As needed 165 gals 2300 ammonia equiv_ tons Unit 11600 Ibs Unit 2 2000,Ibs Unit 3,6000 Ibs Unit 1 1800`Ibs Unit 2 2200 Ibs Unit 3 7000 Ibs Unit 125, Ibs Unit 2 35 Ibs Unit 3 70 Ibs Unit 12000 Ibs Unit 2 2900 Ibs Unit 3 5600,lbs Unit 1500 Ibs Unit 2 750 Ibs Unit 3 1400,Ibs 3500 Ibs Tetraammonium 10,000 gals ethylenediaminetetraacetic (EDTA), and ammonium hydroxide AP 1000 A4 -1 Purpose Oxygen scavenger in boiler pH control in,boiler pH control in boiler Demineralizer regeneration Ash pond pH control Ash pond pH control Ash pond total suspended solids control Demineralizer regeneration Water softener regeneration Control of biofouling on heat exchangers Control of biofouling on heat exchangers Corrosion control in cooling water system Cleaner As needed Equipment freeze protection Continuous NO„ Control Normally every Boiler cleaning 5 to 10 yrs Normally�every Boiler cleaning 5 to 10 yrs Normally every Boilerdeaning 5 to 10 yrs Normally�every Boiler cleaning 5 to 10 yrs Normally every Boiler cleaning 5 to 10 yrs Every 5 to 10 Boiler cleaning years — if needed Normally every Boiler cleaning 5 to 10 yrs Nofmally,every Boiler clean`mg 5 to 10 yrs w Progress Energy Carolinas, Inc. L. V. Sutton Electric Plant Estimated Quantity WDE3 Permit NC0001422 Permit Modification Application January 2011 Chemical (per year) Frequency Purpose Low hazard corrosion inhibitor 110 gal's Normally every Boiler cleaning 5 to 10 yrs ,Silicone antifoam agent 20 gals Normally every Boiler cleaning 5 to 10 yrs Antifoam agent 10 gals, Normally every Boiler cleaning 5 to 10 yrs Liquid oxygen 2500 gals Normally every Boiler cleaning 5 to 10 yrs Powerback Premix with anti -foam agent 110gals As needed IC unit cleaning Freeze control products (i a -, varying As needed As needed Coal freeze conditioning agent solutions of,glycol, calcium chloride, glycerin, diethylene, etc ) Combined Cycle Power Block Hydrazine TBD_ Continuous Steam cycle oxygen scavenger Amine /ammonia TBD Continuous Steam cycle pH control 'Phosphate TBD Continuous Steam cycle scale and pH control Corrosion inhibitor TBD Continuous Cooling +water system corrosion inhibitor Sodium hypochlorite or sodium bromide TBD Continuous Cooling water system biofouling control Mineral dispersant TBD Continuous Cooling water system scale inhibitor Sulfuric acid TBD Continuous Cooling water system pH control Citric acid TBD Continuous Water treatment system low pH reagent Sodium hydroxide, (50 %) TBD Continuous Water treatment system high pH reagent Sodium hypochlonte TBD Continuous Inlet water oxidation and filter backwash reagent Potassium permanganate TBD Continuous Filter inlet water chemical Sodium bisulfate, TBD TBD Plant systems process water dechlormation Sodium bisulfate TBD TBD Reverse,osmosis water system inlet water dechlorination Sodium hydroxide (50 %) TBD Continuous Reverse osmosis water system chemical Anti- scalant TO Continuous Reverse osmosis water system scale greyention A4 -2 Progress Energy Carolinas, Inc. 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Sutton Electric Plant NPDES Permit,NC0001422 Permit, Modification Application January 2.0.11 Attachment 5 Form 2C - Item V, Intake and Effluent Characterization Internal Outfal 1 0065 12 12 1.2 3 35 46 152 'All parameters are expressed in mg /,L except for color (CU) Available data, is presented A54 Supply Cooling Cape Fear Internal Parameter' WeiIS2 Pond River4 Outfall0055 Aluminum - -- 00455 062 - -- Ammonia - -- < 0 1 007 - -- Antimony < 0 006 0 003 - -- 0 037 Arsenic < 0 05 00385 0 031 Barium < 2 0 063 - -- 124 Beryllium < 0 004 < 0 001 - -- 0025 Boron 0 915 0 274 - -- 567 Bromide - -- 018 - -- - -- Cadmium < 0 00175 < 0 001 0 0 012 Calcium - -- - -- - -- 682 Chloride < 250 - -- - -- 529 Chromium < 0 05 < 0 005 0 0 310 Chlorine, TR - -- < 12 - -- < 1 2 Cobalt - -- 0 005 - -- - -- Copper < 1 0 024 - -- 62 Fluoride < 2 025 - -- 124 Iron 04 00805 1 25 85 Lead < 0 015 00125 0 0 093 Magnesium - -- 431 - -- 23 Manganese 086 < 0 005 - -- 53 Mercury < 0 00105 < 0 0002 0 0 006 Nickel < 0 1 0 005 0 062 Nitrate <10 - -- - -- 62 Nitrite <1 - -- - -- - -- Nitrate- Nitrite - -- < 0 25 005 - -- Nitrogen, T - -- 06 1 4 - -_ Phosphorus, T - -- 0 055 016 - -- ,Selenium < 0 05 0 017 - -- 0 310 Silver <0 01.75 < 0 005 - -- 0 109 Sodium - -- - -- - -- 62 Sulfate < 250 46 5' - -- 1153 Sulfide - -- 0015 - -- - -- 'Sulfite - -- < 1 0 - -- - -- Thallium < 0 002 < 0 001 - -- 0 012 Tin - -- < 0 05 - -- - -- Titanium - - -< <001 - -- - -- Zinc < 1 05 0 004 0600 62 Conductivity 527 - -- - -- 520, O &G - -- < 1 0 4:5 BOD 2 <_2 _ - -- 124 COD 88 1 5, - -- - -- TOC 1 8 77 - -- 7 4 TDS < 500 - -- - -- - -- TSS - -- _ 15 14 '17 Color - -- 22 - -- - -- Internal Outfal 1 0065 12 12 1.2 3 35 46 152 'All parameters are expressed in mg /,L except for color (CU) Available data, is presented A54 4 Progress Energy Carolinas, Inc. L. V. Sutton Electric Plant. NPDES Permit NC0001422 Permit Modification Application January 2011 2Averaged groundwater monitoring data for background well 2C and supply well 6C from 2006 to 2009 3Concentrations are the maximum.30 -day average values reported in the NPDES Permit Application 'm,2006 for Outfall 001, the discharge from the cooling pond to'the Cape Fear River The cooling pond will continue to be the water supply for the combined cycle power block recirculated condenser cooling water 4Data reported in the Environmental Assessment of the Lower Cape Fear River System, 2009, by Mallin et ,al , September 2010, for the station in the Cape Fear River- upstream and closest to the intake for the Sutton Plant cooling pond, Station IC (above Indian Creek) 5Values listed for the iproposed internal outfalls are estimated based on water source characteristics and normal design operations A5 -2 t.�t"Gi y -� � �I •r.' y, �•,�' `_'i ,.�V �,!n _ _ _ it ,f, m >`t_ � _ sJ f '''' _ _ _ ' ' -,- �, 'ti',_ �' + r , , .}r')in :/ 9nI p1 1 -P ,�` .sI 1p/4�L'�.11r_ ��_/ /j'•/�_�,�'.¢�'�� \���' `a" _ :�'t_ ,� -_ -, �� "i'? t`'` {i �t &�=._ `ti 't. - }p - .'` _ __ } "p �1 � -' l r /'i.V �F� �` t' fY /I1�� _ - _•_�t:,l. 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',,�' " °"}_'x"�;.` -�'+, "- r _ _ _ - 7,r �, 41r. _ •'r 'C-t' '�y`,� _ _ 4} __ 'i� ''ur.i, 'C.'t 3ati3?- RtlVMcGrory�_' ,� -v . _ ,•�.,' Cfiarles�111Vakild;-P_.AE=M - aria= =III'' f - _ 1 idohn�E Skv �a::•`�'r''.; a'�`~Prr � I' i'r;'' __ (.I 2hs�r A: it lr., 4. ,� 4���, -:_ ��;G__o�_e_rnor, , -� _- "1r - _ _ ,•' m,' 1 _ ;�Dlrectar °` - _ =- - _ ���� "' }��;,�i , ,^' , t F...` _ i, r i" '_ _ _ - _ ) y ` - _ _ `_ ?- -r' iW` L•.'` _ .C.¢ i`•' __,"�,. `7`` _ - _ J ,�I . _'� , Y"r ' a,K- - -' - °;�'- T= -_ „ ;: - - -- -- -AMa :3;2013 "4 -- _Y��;;''r,.:; °�, _ _. ,_ ,au;�,_�-- -.• ✓', -_s -a •rn P7 '31 +.:� ,s =L_�; i' 'I -I, Jrt'� °5 -Allen A Clare P.,Iamt�Mananne� 1'A �'I , _ - ,U_3i. ,, is w. y` v�pr. -�I±i, : _ _ ,`Y'.il';, .rah : %'- _ V -� _ , ''y'f'�;.'.;t �; , _ _ _ .�' '''�'> /�i- s'�`y_.dF•,'s �; �/ SuttOnyElectnc,Plant �,, Duke'Ener' ViPro r" r.,. .egy,_ • = .�:, �- ;80,1xStitton;Stdai tTlant'R6ad Wilmington; NC >28.401 } Ai,i)S.'- - 'r Y- '� ._ ` }'41I,: .I�,t' - -h -LEI Jt 'I,y i_� Sii 4Jfr' _ _ .cl+f'•,. _ _ - FrGii- �h -�t�'_ __ v `fir ' n� +;��a,, ;r,._ iii � - } _ - V}�* v v • _ � '^ - ' 9 � -�� -'e$'' �, � ` _ _ ;Ir=� _'<u�' 00 J9' _,Subject- oProgress,Energy'sI V., -Suton Steam' Plant;(NPDESIPemit NC0t .4;I22 ): r ? '� F.s41 y_Monrtonng,to Evaluafe_'the'Re`rciutrng of Ash.P,ondr'Effluent;20J2f i'ry�' N „ *;� ;' 'f” 'F '_`,' al, ,ait:,. _ -= _ t ` '� (' t � _r,t `^ _ _3Jr'•15 J' _ _ ___ _i�,r _ _ �1 r'' 4 _ _ <<_ hY" _ .[?,5, .�,,�I, ____ _ _ _ _ `DearFMr: Clare.- `,,�,,; -- _ ^J- }, 'ss t''- xT •`-•- ' µ n _'• Thank you =for your,contlriued efforts to proinde the North GaroliAabWlsiori ;of- WaterFQuality wtth annual fish: ' seleniummonitoring,tdata;from the lower Ga a Fear'River ^We;appre iate y (� ?' P . T c �our_voluntary sutimittahof' - "' IweIhV1le receivedtthis:re `vla;em ll �''" port, a' on "Apnl:29 -', 2013. _ N, : r .,1 O.date }aS- I. ��1 - - _ , t {' -✓ : ter' i-,� }" a bnium concentrations in-all,taMi§ted fi`sh�speaes "have' remained ;sirnila�;to- theptia "settne;`' ,� COnCerlii tlOns'r� f y_ _ " _ eported'in_1999 Pr' ogress Ener data.frorii;2012 cont�nuesao stiow'ttiat torero_ utmg of -ttie 2= �, fir, 9Y „� _ asFi�pond= ouffalllri.the Cape�Fear RiYer-hashad`iittleFeffect on= f "shSelernurn.le'vels,ln thetviclriity ofirthe'' power'plant' and' that° all_ Selenium- levels;in fish''a "rewuell 'below =the- Nortti`Carolina�De "artm'en " _ - trof HealtFi =and' t`���' 7 - ' °9 - _ • ; -. s^""�"a -T " = -- 1 ,, p r(a_`'''i'' ^, �k-L - _ Human Seniice'' s;{ NGDHHS }_fish�con'_sumptibn,action�level of 10ppr» In addltton, the +voluAiiryihe_rcurydata" J t ti i- t Lr,,, continue }to;demonsfrate,that levels are below the °NCDHHSlevel ofi0 ' }F',�” .f - -_ ,,,_ r� c - �'r: _ - =- `_ • _ rP�b'� "� `- - a� F-`� _ " "i Ir� y`- _ — T; -_ _ __ _ _ ` >�,p9 +t ,� „� 'Ifyou�have;an` uestions; >`lea'se do�nottiesitate'to contacfirti�;" " r Y 4 , P _ = - - e,or my staff:= _ rc�{kt``, r .I ^4 rr' 4,Ii -�. oh' °Sincerely, " }'' �''t ;nr,C '+ .I. p�Jr' y ;'A' '.I lll�u -�- _ `,Ja'• fir`„ - _ -+ s I , '1 = .._ S-y'ei u ,,�`✓ .r }�,i9- '_r _S`_'' -I '♦' � .Y'ziY, I Jl,an' ,b` 'ia - =r Jay,,H, Sauber - ., ;:a<i• _ _ ' `,_ `s" }n <- _ - -;,; r ,'. Chief; En' vlronfllental'Sclef3ces°Section " - - ,_� ° ✓, :_rte -= _ ', pry _ r. - -_.___ _ _ r t '6 ''4, %� __ -YT:`� -� _ _ -_ -__ r_ _ r�+cr ,ti ,, `�lua'. ' -:< -r_ ;. r, IM1 _, n n.♦;� -r = ,'� "�� _ ' fir, I£` _ _ �'j _ rIt'' -`I• `L'` _ ,1r � _ �t - .a`Jk .�a Tom Belnlck; NPOES 'Complex Rerrruttin Unit = 1e e 9 =Jim re so ,:- -_v_z - - • ' - - _ _ 9 �_ n=- V-- , __ �, - _KenR ud oNCDH HS < ' _ , ` �' {Y 4 \') ll� � - - - _.— _- „? i %� Z "Is• _ 't' ;' I.'i Ily iy� A„ � - __ - � __ v .. __ „,na r - ��`, •�1 '� +' J b} - ?,4 `f '.',`'_ - _ `„�`•' rn, "' -= - ' r: ` t - `& J ` =x�eY _ rl r` _ _' .E vlrOftrpt 9181 ±Scidnces•Secttppn . - P 1621 Mail,Sernce,6enter Raleigti;INo ttti Camllna 27699 ;1621 - .4 5 t ,� *'� § t, ' I3; .fob. ;- Location 4401Reed Creek Road „Ralei h� NoKh Car rn ' YI, F 9,M4_ _ of Aa'27607 Phorie '919 743 -' '8400 "1' FAX 919 =74 ale', 7 _ - `v?- _° - K a iS -'£� -n n.ir _`< _ -,ht.,+F' t a. ;tn #efnet_4h #tp /Jgartal nC nr rgJwet) /WC�IeSS /home, 7' ^�yTol tl�'4'ci% t1Il ] ' ,;s.� `_ t KLi , F - An Equal'Opportundy 1wArmatrve Actton,Employer' µ� " - - - altl_lr� �: Chernikov, Sergei " From•-;° =? Holt, Fred <Fred Holt @pgnmail com> Sent:{ ^" Monday, November 07, 201110 52 AM' 1, 47 `rte, To: Chernikov, Serge,, Stowe, Allen Subject: RE request A few comments — Slide 4— Current plann'ing statement: Sutton; to be converted by Dec. 311 2013; Cape Fear retired by June 2013, Slide 6 — first bulleted item, recommend adding the word "ponded ".before "ash" Slide 7-. lists a landfill and FGD /scrubbers as "typical plant components." Of our seven .plants We only have one landfill and three FGD /Scrubbers. May could change title to read just "plant components" or "certain plant components''. Slide 15 — Sutton does not have FGD; Cape Fear has what could be considered as three retired ,ash ponds; 9" NOK Environmental Servicestand Strategy ^.-,Progress Energy Carolinas, Inc. ,'Mail Code PEB 4 -V -Net 770 - 5286 External 919 546 - 5286 Mobile 919 632 - 8165 fred.holt@a oRnmail corn From: Chernikov, Serge, rmai Ito: seraei.chernikov @ ncdenr.aovl Sent: Wednesday, November 02, 2011 12:40 PM To: Stowe, Allen; Holt, Fred Subject: request Allen and Fred, X . I am making presentation,about NPDES permitting of the power plants to the EMC on November 17, please see attached. It'is very similar to the presentation that I did 2 years ago. Please review',t and' let me know if there are factual errors. Thank you! J Sergei - Sergei Chernikov, Ph.D. Environmental Engineer II Com -plex Pe- rmitting Unit Phone: 919- 807 -6393, fax 919 - 807 -6495 1617 Mail Service Center Raleigh, NC 27699 -1617 Express mail: 512 North Salisbury St. Raleigh, NC 27606 E -mail correspondence to and from this address may be subject to the North Carolina Public Records Law and may be disclosed to third parties. 'Please print or type in the unshaded areas only ' Form Approved OMB No 2040 -0086 FORM 'US ENVIRONMENTAL PROTECTIOWAGENCY I EPA I D NUMBER 1 0A�E�� GENERAL INFORMATION Consolidated Permits Program' 6 TIA c NCD 0'0 0'8 3 0 6 4'6 D GENERAL (Read the "General /nviructiorn',beforevarting) 1 12 13 14, 1 1s 'I 1 1 1 1 1 'Rol 1 1 1 1 1 1 1 1 1 1 `_ ,, GENERAL INSTRUCTIONS LABEL ITEMS _t If a preprinted label has been provided affix it in the �� y designated space Review the rrdortnation carefully,'if any of it 1 '1 EPA I MBE D NU E R I �, through and enter - is incorrect, cross throw h the correct data in the appropnate filNn area below Also if any of the preprinted data s -• - ' 7 is absent (the area to the left of fhe label space lists the III .. FAC_ILITY ^N_ AME P „LEASE'P,LACE ,LABEL' IN THIS'SPACE information that should appear), please provide it in the proper ” , ° '_ fill-in area(s) below If the,label,is complete and correct, you " - c, T'''r V' FACILITY'MQILING "'° 4 need not complete, Items I, III, V, and VI (except VI -B which I must be completed regardless) Complete all items if no,label F ,ADDRESSr has`been provided Refer to the.mstructions for detailed item u y ',FACIL'ITY?LOCATION' descriptions and for the legal authorizations under which this - i i I'ti, data is collected II POLLUTANT`CHARACTERISTICS X INSTRUCTIONS Complete A through J to determine, whether you need to submit any permit application'forms to'the EPA If you answer "yes" to any questions, you must submit this form and the supplemental form listed in the parenthesis' following the question Mark- "X " "imthe'box,in the third column if,the, supplemental form is attached If you,answer "no" to each question, you need not submit any of�these'forms You may answer "no" if your activity Is excluded from permit requirements,isee Section'C of the instructions See also, Section D of the instructions for definitions of bold -faced terms Mark 'x' Mar' 'x" I SPECIFIC'QUESTIONS ves NO ATTAC ED SPECIFIC QUESTIONS ves Ho ATTACHED A Is this facility a publicly owned treatment works which B Does or will, this facility (either exishng or proposed) results in a discharge to waters of the U S ? (FORM 2A) X include a concentrated animal feeding operation or •�- s� aquatic animal production facility which results in a 'I 1 1 1 1 1 'Rol 1 1 1 1 1 1 1 1 1 1 -6 17 16 discharge to waters of the U.S ? (FORM 2B) 19 m 21 C Is this a facility, which currently results in discharges to �/ -S, thanJhose A /� �/ D Is,this a� proposed facility (other than those described in A X B discharge to X waters of the U other �descnbed in or ,B or above) which will result in a waters of �'N,�3,,1� ''�' �1i1' .1 above ?, (FORM 2C) 115 the U'S 9 (FORM'2D) 22 23 24 25 N 27 E Does or will this facility treat, store, or dispose of F Do you or will you inject at this facility industrial or hazardous wastes? (FORM 3) X municipal effluent below the lowermost stratum X I I I I I I I I I I I I I I I I I I containing, within one quarter mile of the well bore, 26 29 30 underground sources of drinking water? (FORM 4) 31 32 33 1 G Do you or will,you inject at this facility any produced water H Do you or,will you inject at this facility fluids for,special 1 48 or other fluids which are brought to the surface in processes such as mining of sulfur by the Frasch process, connection with conventional oil or natural gas production, X, solution mining of minerals, in situ combustion of'fossil X inject fluids used for enhanced recovery of oil or natural E ZIP CODE fuel, or recovery of geothermal energy ?,(FORM 4) gas, or inject fluids for storage of liquid hydrocarbons? I I I I I I I I I I I I I I I I I I I Z C I (FORM 4) _ -31 35 38 37 38 39 1 1 Is this facility a, proposed stationary source which is one J Is this facility a proposed stationary source which is 41- 42 of the28 industrial categoneshsted in the instructions and X X NOT one of the 28 industrial categories listed in the X which will potentially emit 100 tons per year,of any air CONTINUE ON REVERSE instructions and which will potentially emit 250 tons per pollutant regulated'under the Clean Air,Act and'may affect year of, any, air, poll utant�regulated under the Clean AmAct or be located ^m an attainment area? (FORM 5) 4o d1 42 and may affect or be located in an attainment area? 43 44 as (FORM'S) III NAME OF FACILITY 1 SKIP LI V I Sutton E ectric P ant A 115 16 - z9 30 69 1 IV FACILITY CONTACT A NAME & TITLE (last, first, R title) B PHONE (area elodel& no), 2, J1. Mark Flreld''eril I IPla I IManag1 1 1 1 1 1 1 1 1 1 1 1 1 1 (bib) 1 3431 3201 I I 1' 15 16 451 46, b 149 51 152 V FACILTY MAILING ADDRESS A - STREET OR P O BOX 0 0 1_ I I I I I 3 Plant Road 801 Sutton St'ea'm 1 15 16 45 1 B CITY OR TOWN C STATE D ZIP CODE , HI I ,- I I " I I I I I I I I I I I I Wilmington I I I I I I I I I 1 I I I I NC 28401 I 15 16 40 41 42 47 1 4✓`I'��� �� _ _ — 1 VI FACILITY'LOCATION A STREET, ROUTE NO OR OTHER,SPECIFIC IDENTIFIER •�- s� b I I I 'I 'I 1 1 1 1 1 'Rol 1 1 1 1 1 1 1 1 1 1 1 1 1 ,1 I•_ 8 1 Sutton Steam Plant Roa �'N,�3,,1� ''�' �1i1' .1 115 .16 451' B ,COUNTY NAME' I IN I I I I I I I I I I I I I I I I I I I I I I DE','R -WATER QUALITY" New anover - P0INT`80UKCE,BRANCH, 1 48 70 C CITY OR TOWN D STATE E ZIP CODE F COUNTY CODE (fkno.'r) s WilniiAg�'oti I I I I I I I I I I I I I I I I I I I Z C I 294dl 11s 16 60 41- 42 47 - -- - - - 61 - 52 54 _ EPA Form 3510 -1 (8 -90) CONTINUE ON REVERSE i CONTINUED FROM THE FRONT ;7. VII SIC CODES'(4- digtt, to orderofpnonty) A FIRST B SECOND H741 I I (specify) c I I I I keC�) 4911 ' I Electric Power Services I15 16 19 15 16 191 1 C THIRD D FOURTH I c I (speL�) 7 I 1 I (speC�) 16 19J 15 16 191 VIII OPERATOR INFORMATION A NAME 1B is the,namelisted In Item I I I I I I I d I I 1 I I I I I I I I I h I I I I I I I IVIII-A Owner? 121 YES, ❑ °NO c Carolina Powe Light Co. I d /b /a I Progress' Energy I, CaroinI as,, I Lic 1 15'1 18 - 55166 C STATUS'OF OPERATOR (Finer the appropriate letter into the answer hox if "Other, -" sped) D PHONE (area code & no) F= FEDERAL (specify) 1 1 1 1 1 1 1 1 1 S = STATE M = PUBLIC (other than federal or stale) A ( 910) 343-3201 P = PRIVATE O =OTHER (sped) Public ur313ty 56 I15 8 18 119 21 122 ffi I OR,P O BOX 8 1 S1 I I I I I I I I I I utton Steam P ant Road 12 W1� F CITY OR TOWN G STATEI H ZIP CODE IX INDIAN LAND JI I I I IS the facility located on Indian lands? �wilmington NC 2,8401 ❑ YES ❑ NO 16 - b a1 42 In - 51 X EXISTING ENVIRONMENTAL PERMITS A NPDES(Dicchargesto Surface Water) D PSD (Air l ;missionsjrom Proposed Sources) xx Y_ _� •6' ` +��h" C T I I I I I I I I I I I I -c I T I I I I I I r I I I I I I I 9 N NC0001422 M.' I, T 15 16 1r 1s 30 118 b B UIC (UnderToundlnjection o(Flin&JI _ E OTHER (specify) c T I I f I I I I I I I) I I °`' w600001020 I I I I I I I I (specify) 9 U - - I NC Ash Ut>_ll.zat- 115 18 1] 16 30 15 16 1] 16 30 C RCRA (Hazardous Waster) E OTHER (specify) C T 1 I I 1 1 1 1 1 1 1 I 1 1 c I T 1 I (specify) g ft NCD000830646 - g 165-'88 LAMA Permit for intake structure 1 15 16: 171 16 30 t15 18 1]t 18 - - 30 XI MAP Attach to,thls application a topographic map of the area extending to at least one mile beyond property boundaries The map must show the \outline of the facility, the location of each of Its exlsling and proposed intake and discharge structures, each of 1tslha2ardous,waste treatment, storage „6r disposal facilities. and,e ch well wher it Injects fluids underground Include all springs, rivers, and other surface water bodles,In the map area See instructions for precise requirements (AttacGent 1� XII _NATURE OF BUSINESS (provide a bnef descnphon) The L V Sutton Plant is an electric generating facility currently consisting of three coal -fired units and three internal combustion turbines units This plant is being repowered Upon commercial operation of a new combined cycle power block, the coal -fired units will be retired XIII CERTIFICATION (see instructions) I certify under penalty of law,that 1 have personally,examined and am familiar with the information submitted in this application,and all attachments and that „based,on my inquiry`of those persons immediately responsible for obtaining the information contained, in the application, 1 believe,that'the information is true, accurate, and complete 1 am aware that there are significant penalties for submitting false'information„ including the possibility of fine and imprisonment A NAME,,& OFFICIAL TITLE (type or prun) B SIGNATURE C DATE`SIGNED J'. Mark`Frederick, Plant Manager W. COMMENTS FOR OFFICIAL USE ONLY I'Cc, 16 EPA Form 3510 -1 (8 -90) EPA I.D. NUMBER (copyfmm Item I oJForm l) Form Approved. OMB No. 2040 -0086. Please print or type in the unshaded areas only NCD000830646 Approval expires 3- 31 -98. FORM U.S. ENVIRONMENTAL PROTECTION AGENCY 2C � EPA EXISTING MANUFACTURING, FOR PERMIT TO DISCHARGE WASTEWATER ACTURING, COMMERCIAL, MINING AND SILVICULTURE OPERATIONS NPDES Consolidated Permits Program I. OUTFALL LOCATION For each outfall, list the latitude and longitude of its location to the nearest 15 seconds and the name of the receiving water. A. OUTFALL NUMBER B. LATITUDE C. LONGITUDE (list) 1. DEG 2. MIN. 3. SEC. 1. DEG, 2. MIN. 3. SEC. D. RECEIVING WATER (mmnc) 001 34 16 57 77 59 20 Cape Fear River II. FLOWS, SOURCES OF POLLUTION, AND TREATMENT TECHNOLOGIES A. Attach a line drawing showing the water Flow through the facility. Indicate sources of intake water, operations contributing wastewater to the effluent, and treatment units labeled to correspond to the more detailed descriptions in Item B. Construct a water balance on the line drawing by showing average flows between intakes, operations, treatment units, and outfalls. If a water balance cannot be determined (e.g.. for certain mining activities), provide a pictorial description of the nature and amount of any sources of water and any collection or treatment measures. B. For each outfall, provide a description of: (1) All operations contributing wastewater to the effluent, including process wastewater, sanitary wastewater, cooling water, and storm water runoff, (2) The average flow contributed by each operation, and (3) The treatment received by the wastewater Continue on additional sheets if necessary. 1. OUT - I 2. OPERATION(S) CONTRIBUTING FLOW 3. TREATMENT FALL b. AVERAGE FLOW b. LIST CODES FROM NO. (Gsl) a OPERATION (LsQ (include units) a DESCRIPTION TABLE 2C -1 EPA Form 3510 -2C (8 -90) PAGE 1 of 4 CONTINUE ON REVERSE Cooling Pond discharge Discharge to surface waters 001 0 -380 MGD 9 -A (Coal Recirculated cooling water Evaporation, recycle (4 -C) Units) I 583 MGD 1 -F Non- contact cooling service water Evaporation, recycle (4 -C) 7 MGD 1 -F Ash pond discharges Sedimentation, neutralization, recycle (4 -C) 7 MGD 1 -U 2 -K Intake screen wash Sedimentation, neutralization, recycle (4 -C) 0.84 MGD 1 -U 2 -K Low volume wastes (e.g., plan[ Sedimentation, neutralization, recycle (4 -C), 0.35 MGD 1 -U 2 -K drains, boiler blowdown, water oxidation, precipitation, and 2 -B 2 -C treatment wastes) sorption, reduction 1 -X 2 -L Storm water (exempt) Sedimentation, sorption, recycle (4 -C) 0.08 MGD 1 -U 1 -X Coal pile runoff Sedimentation, neutralization, recycle (4 -C) 0.2 MGD 1 -U 2-K Cooling Pond discharge Discharge to surface waters 001 0-380 MGD 4A (CC I Recirculated cooling water 288 MGD (estimated) Evaporation, recycle (4 -C) 1 -F BlOCiC) Storm water (exempt) Sedimentation, sorption, recycle (4 -C) 0.09 MGD (estimated) 1 -U 1 -% Low volume wastes (e.g., filter Sedimentation, neutralization, recycle (4 -C), 0.85 MGD (estimated) 1 -U 2 -K backwash, CCWC blowdown, HRSG oxidation, precipitation, and 2 -B 2 -C blowdown, aux. boiler blowdown, sorption, reduction 1 -X 2 -L HRSG cleaning wastewater,RO /EDI system wastewater,plant drains, equipment drains, portion of coal units low volume wastes) See Attachment 2 for aline drawina of the water flow throuc,Ih the existina units and the nroaosed combined cycle lock, See Attachment 3 for additional i lescri0ions of contributing flows. OFFICIAL USE ONLY (ef/luentguidelines.suh- categories) EPA Form 3510 -2C (8 -90) PAGE 1 of 4 CONTINUE ON REVERSE 001 (Coal 'Cooling Pond discharge 0 5 4 ,12 84 380 12 84,MG `380 MG 1 Units) OOP (CC Cooling Pond discharge (estimated) 0 5 4 12 380 12 MG t380 MG 1 Block) III PRODUCTION A Does an,eftluent guideline limitation'promulgated by EPA under Section 304 of the Clean Water Act apply to your facility? ® YES (complete Item II /`B) ❑ NO (go to'Section jV-) B Are the limitations m the applicable effluent guideline expressed in terms of production (or other measure of operation)? ❑ YES (complete Item III -C) 91 NO (go to Section IV) C If you answered-yes" to Item III -B, list,the quantity,which represents an, actual measurement of your level of production, expressed in the terms and units used in the applicable effluent guideline, and indicate the affected outfalls I %AVERAGE;DAILY'PRODUCTION 2 AFFECTED,OUTFALLS a QUANTITY PER,DAY b UNITS`OF,MEASURE c OPERATION, PRODUCT; MATERIAL,,ETC (/iuoutfol111umb'ers) (specify) NA IV IMPROVEMENTS A Are you now required by any Federal, State or local authority to meet any implementation schedule for the construction, upgrading or operations of wastewater treatment,equipment or practices or any other environmental programs which may affect the discharges,descnbed in this application? This includes, but is not limited to, permit conditions, administrative or enforcement orders, enforcement compliance schedule letters, stipulations, court orders, and grant or loan conditions ❑ YES (complete,rhe follom ink table) © NO (go to Item IV -B) 1 IDENTIFICATION OF CONDITION, 2 AFFECTED OUTFALLS 3 BRIEF DESCRIPTION OF PROJECT 4 FINAL COMPLIANCE DATE AGREEMENT, ETC a NO b,SOURCE OF DISCHARGE a REQUIRED b PROJECTED NA B OPTIONAL You may attach additional sheets describing any additional water pollution control programs (or other environmental projects which may affect your discharges) you now have underway or which you plan Indicate whether each program is now underway or planned, and indicate your actual or planned schedules for construction ❑ MARK "X" IF DESCRIPTION OF ADDITIONAL CONTROL PROGRAMS IS ATTACHED EPA Form 3510 -2C (8 -90) PAGE 2'of 4 CONTINUE`ON,PAGE'3 CONTINUED FROM THE FRONT C Except forstomi runoff, leaks, or spills; are any'of the discharges described in ItemsJI -A or B Intermittent or,seasonal? © YES (complete the following ing table) ❑ NO (go to Section 111) 3 FREQUENCY 4 FLOW a DAYS PER B TOTAL VOLUME 2 OPERATION(s) WEEK b MONTHS a FLOW RATE (m .g4 (specifyivith units) _ 1 OUTFALL CONTRIBUTING FLOW (st —Ify PER YEAR 1 LONGTERM 2 MAXIMUM 1' LONGTERM 2 MAXIMUM C DURATION NUMBER (het) (list) h—ge) (specifyawra'ge) AVERAGE DAILY AVERAGE DAILY (in days) 001 (Coal 'Cooling Pond discharge 0 5 4 ,12 84 380 12 84,MG `380 MG 1 Units) OOP (CC Cooling Pond discharge (estimated) 0 5 4 12 380 12 MG t380 MG 1 Block) III PRODUCTION A Does an,eftluent guideline limitation'promulgated by EPA under Section 304 of the Clean Water Act apply to your facility? ® YES (complete Item II /`B) ❑ NO (go to'Section jV-) B Are the limitations m the applicable effluent guideline expressed in terms of production (or other measure of operation)? ❑ YES (complete Item III -C) 91 NO (go to Section IV) C If you answered-yes" to Item III -B, list,the quantity,which represents an, actual measurement of your level of production, expressed in the terms and units used in the applicable effluent guideline, and indicate the affected outfalls I %AVERAGE;DAILY'PRODUCTION 2 AFFECTED,OUTFALLS a QUANTITY PER,DAY b UNITS`OF,MEASURE c OPERATION, PRODUCT; MATERIAL,,ETC (/iuoutfol111umb'ers) (specify) NA IV IMPROVEMENTS A Are you now required by any Federal, State or local authority to meet any implementation schedule for the construction, upgrading or operations of wastewater treatment,equipment or practices or any other environmental programs which may affect the discharges,descnbed in this application? This includes, but is not limited to, permit conditions, administrative or enforcement orders, enforcement compliance schedule letters, stipulations, court orders, and grant or loan conditions ❑ YES (complete,rhe follom ink table) © NO (go to Item IV -B) 1 IDENTIFICATION OF CONDITION, 2 AFFECTED OUTFALLS 3 BRIEF DESCRIPTION OF PROJECT 4 FINAL COMPLIANCE DATE AGREEMENT, ETC a NO b,SOURCE OF DISCHARGE a REQUIRED b PROJECTED NA B OPTIONAL You may attach additional sheets describing any additional water pollution control programs (or other environmental projects which may affect your discharges) you now have underway or which you plan Indicate whether each program is now underway or planned, and indicate your actual or planned schedules for construction ❑ MARK "X" IF DESCRIPTION OF ADDITIONAL CONTROL PROGRAMS IS ATTACHED EPA Form 3510 -2C (8 -90) PAGE 2'of 4 CONTINUE`ON,PAGE'3 EPA I.D. NUMBER (ca1!t fron+ Item l nff,win 1) CONTINUED FROM PAGE 2 1 NCD000830646 V. INTAKE AND EFFLUENT CHARACTERISTICS A. B. 8 C: See instructions before proceeding — Complete one set of tables for each outfall — Annotate the outfall number in the space provided. NOTE: Tables V -A, V -B, and V -C are included on separate sheets numbered V -1 through V -9. D. Use the space below to list any of the pollutants listed in Table 2c -3 of the instructions, which you know or have reason to believe is discharged or may be discharged from any outfall. For every pollutant yo t list, briefly describe the reasons you believe it to be present and report any analytical data in your possession. 1. POLLUTANT 2. SOURCE 1. POLLUTANT 2. SOURCE Coal Unite Strontium Occasionally found in coal Uranium occasionally found in coal Vanadium Occasionally found in coal Zirconium occasionally found in coal Asbestos May be component in insulation CC Block None VI. POTENTIAL DISCHARGES NOT COVERED BY ANALYSIS Is any pollutant listed in Item V -C a substance or a component of a substance which you currently use or manufacture as an intermediate or final product or byproduct? ® YES (list all such pallumna below ) ❑ NO (iv, n> hem 17 -h) Coal Units Antimony Arsenic Beryllium Cadmium Copper Lead Mercury Nickel Selenium Silver Thallium Zinc CC Block None See Attachment 4 for other substances used during operational processes or at the plant that potentially may be discharged. EPA Form 3510 -2C (8 -90) PAGE 3 of 4 CONTINUE ON REVERSE CONTINUED;FROM THE FRONT VII BIOLOGICAL TOXICITY TESTING DATA Do you have any knowledge or reason to believe that any biological test for acute or chronic toxicity has been made on any of your discharges or on a receiving water in relation to your discharge within the last'3 years? © YES (,dent fy the test(,) and describe their purposes below) ❑ NO (go to Section VIII) 24 -hour static acute toxicity tests using fathead minnows are conducted quarterly (February, May„ August, and November) on the wastewater discharge from Outfall 001 VIII CONTRACT ANALYSIS INFORMATION Were any of the analyses reported in Item V performed by a contract laboratory or consulting firm? ❑ YES (h st the name, address, and telephone number of and pollutants analyzed by, each such,laboratory orfrm helow) A NAME NA B ADDRESS h ® NO (go to Section A) C TELEPHONE D POLLUTANTS ANALYZED (area code d no) (list) IX CERTIFICATION I certify under penalty of law that this document and all attachments were prepared under my direction or supervision to accordance with a,system designed to assure that qualified personnel properly gather °and evaluate the information submitted Based on my inquiry of the person or persons who manage the system or those persons directly responsible forgathering the information, the information submitted ts; to the,best of my knowledge and belief, true, accurate, and complete I am aware that there are significant penalties for submitting false information, including, thepossibdityof fine and imprisonment for'knowmg violations ,A NAME B OFFICIAL TITLE, (type or print) B PHONENO (area -code 8 no ) J Mark Frederick, Plant Manager 'C SIGNATURE E A Form 3510 -2C (8 -90) PAGE 4of4 (919,) 343 -32,01 D DATE,SIGNED I /-Z,/, f// PLEASE PRINT OR TYPE IN THE UNSHADED AREAS ONLY. You may report some or all of this information EPA I.D. NUMBER (copvfrom Item / of Form 1) on separate sheets (use the same format) instead of completing these pages. NCD000 83 0 646 SEE INSTRUCTIONS. OUTFALL NO. V. INTAKE AND EFFLUENT CHARACTERISTICS (continued from page 3 of Form 2 -C) 00= (CC Block) PART A —You must provide the results of at least one analysis for every pollutant in this table. Complete one table for each outfall. See instructions for additional details. 3. UNITS 4. INTAKE 2. EFFLUENT (speciffyifblank) (npnnnaQ b. MAXIMUM 30 DAY VALUE c. LONG TERM AVRG. VALUE (r f available) (if available) CONCENTRATION (2) MASS (1) CONCENTRATION (2) MASS e. Ammonia (ua 4) < 0.1 est - -- VALUE VALUE f. Flow 12 .8 est . VALUE a. MAXIMUM DAILY VALUE 1. POLLUTANT (1) CONCENTRATION (2) MASS a. Biochemical Oxygen < 2 est - -- Demand (/101)) . 31 b. Chemical Oxygen 16 est. 777 Demand (t'01)) CONCENTRATION (2) MASS ANALYSES 0 c. Total Organic Carbon 7.9 est. 384 (70C) mg /L kg /day d. Total Suspended 0 mg /L Solids (TS.x) 2 . 0 est. 99.8 b. MAXIMUM 30 DAY VALUE c. LONG TERM AVRG. VALUE (r f available) (if available) CONCENTRATION (2) MASS (1) CONCENTRATION (2) MASS e. Ammonia (ua 4) < 0.1 est - -- VALUE VALUE f. Flow 12 .8 est . VALUE 0 mg /L kg /day 0 mg /L - -- VALUE 0 MGD - -- - g. Temperature VALUE VALUE VALUE VALUE °C a. LONG TERM 19 est. 0 h. Temperature AVERAGE VALUE d. NO. OF a. CONCEN- 31 (1) b. NO. OF ANALYSES TRATION b. MASS CONCENTRATION (2) MASS ANALYSES 0 mg /L - -- . 0 mg /L kg /day directly, or indirectly but expressly, 0 mg /L kg /day 0 mg /L kg /day 0 mg /L - -- VALUE 0 MGD - -- - g. Temperature VALUE VALUE VALUE VALUE °C (winter) 19 est. 0 h. Temperature VALUE VALUE VALUE VALUE °C (summer) 31 est. 0 MINIMUM MAXIMUM MINIMUM MAXIMUM i. pH 7.3 est . 9.0 est O STANDARD UNITS PART B — Mark "X" in column 2 -a for each pollutant you know or have reason to believe is present. Mark "X" in column 2 -b for each pollutant you believe to be absent. If you mark column 2a for any pollutant which is limited either directly, or indirectly but expressly, in an effluent limitations guideline. you must provide the results of at least one analysis for that pollutant. For other pollutants for which you mark column 2a, you must provide qua ititative data or an exp anation of their presence in your discharge. Complete one table for each outfall. See the instructions for additional details and requirements. 2. MARK "X" 3. EFFLUENT 4. UNITS 5. INTAKE (apnvnon 1. POLLUTANT b. MAXIMUM 30 DAY VALUE c. LONG TERM AVRG. VALUE a. LONGTERM AVERAGE AND a b, a. MAXIMUM DAILY VALUE (rfavadable) I ({l available) VALUE CAS NO. BELIEVED BELIEVED (1) (1) (1) d. NO. OF a. CONCEN- (1) b. NO. OF (rfavarlahle) PRESENT ABSENT CONCENTRATION (2) MASS CONCENTRATION (2) MASS CONCENTRATION (2) MASS ANALYSES TRATION b. MASS CONCENTRATION (2) MASS ANALYSES a. Bromide (24959 -67 -9) b. Chlorine. Total Residual Pollutant may be resent in source wate - - -su I w Y P PP Y Its and /or Ca P Fear Rivel. c. Color X Pollutant may be present in source watee -- supply w lls and /or Cape Fear Rivel. d. Fecal Coliform X Pollutant may be present in source water -- supply w As and /or Cape Fear River. e. Fluoride Pollutant may be resent in source wate - - -su I w Y P PP Y Its and /or Ca P Fear Rivel. (16984 -48-8) f. Nitrate - Nitrite �/ X Pollutant may be present in source watt -- supply w Its and /or Cap Fear River. (as M EPA Form 3510 -2C (8 -90) PAGE V -1 CONTINUE ON REVERSE ITEM V -B CONTINUED FROM FRONT 2. MARK "X" 1. POLLUTANT AND CAS NO. (rf available) g. Nitrogen, Total Organic (a.. ,V) h. Oil and Grease i. Phosphorus (as P), Total (7723 -14-0) j. Radioactivity (1) Alpha. Total (2) Beta. Total 3. EFFLUENT b. MAXIMUM 30 DAY VALUE c. LONGTERM AVRG. VALUE a, b. a. MAXIMUM DAILY VALUE (rjavadable) (ifaadable) BELIEVED BELIEVED (1) (1) (1) PRESENT ABSENT CONCENTRATION (2) MASS CONCENTRATION (2) MASS CONCENTRATION (2) MASS XPollutant may be present in source water -- supply wells and /or Cape Fear River. xPollutant may be present in source wate - -- supply wells and /or Capp! Fear Rivet. XPollutant may be presentin source water -- supply wells and /or Cap} Fear River. (3) Radium, Total (4) Radium 226, Total \ k. Sulfate (as SO.) y x (14808 -79-8) I. Sulfide \/ (as S) x m. Sulfite (aS SO Z) x (14265 -45-3) n. Surfactants o. Aluminum, Total (7429 -90-5) p. Barium, Total \ (7440 -39-3) n q. Boron. Total (7440 -42 -8) r. Cobalt. Total (7440 -48-4) s. Iron. Total (7439 - 89-6) x t. Magnesium, Total (7439 -95-4) u. Molybdenum, Total (7439 -98-7) v. Manganese, Total (7439 -96-5) w, Tin, Total (7440 -31 -5) x. Titanium, Total (7440 -32 -6) X X X X X X IA1 a X X Pollutant may be present in source wate - -- supply w Als and /or Cape Fear Rivet. Pollutant may be present in source wate • -- supply w-,lls and /or Cap- Fear Rivet. Pollutant may be present 'n source water -- supply w -11s and /or Cap± Fear River. Pollutant may be present n source water -- supply wells and /or Cap! Fear River. Pollutant may be present n source water -- supply wells and /or Cap+ Fear River. Pollutant may be present in source wateo - supply w Its and /or Cape Fear River. Pollutant may be present in source wate - -- supply w Its and /or Cape Fear Rivet. Pollutant may be present in source wate - -- supply wills and /or Capee Fear River. 4. UNI'-S 5. INTAKE (nptronan a. LONG TERM AVERAGE VALUE d. NO. OF a. CONCEN- (1) b. NO. OF ANALYSES TRATION b. MASS CONCENTRATION (2) MASS ANALYSES EPA Form 3510 -2C (8 -90) PAGE V -2 CONTINUE ON PAGE V -3 EPA[ D NUMBER (cope from lrem l of erm 7) I OUTFALL NUMBER I CONTINUED FROM PAGE 3 OF FORM 2 -C NCD00083'0646 001 (CC Block) PART C = If you are a primary industry andkthis outfall contains process wastewater, refer to Table 2c-2 m'the'mstnictions to determine which of the GC /MS fractions you must test for Mark "X" in column 2 -a for alli such GC /MS fractions that apply to your industry and for ALL toxic metals, cyanides, and total phenols If you are not required to mark ,column 2a (secondary'industnes, nonprocess wastewater outfalls; and nonregwred GC/MS fractions), mark "X" in column 2 -b for each pollutant you know or have reason to believe is present Mark "X" in column 2 -c for each pollutant you believe is absent If you mark column 2a for any, pollutant, you must provide the results of at least one analysis for that pollutant If you mark column 2b for any pollutant, you must provide the results of at least one analysis for that pollutant`rf you know or have reason to believe it will be discharged in concentrations of 10 ppb or greater If you mark column 2b for'acrolein, acrylonitrile, 2,4 dmitrophenol, or 2- methyl -4, 6 dmitrophenol, you must provide the results,of at least one analysis,for each of these pollutants which you know or have reason to believe that you discharge in,concentrrations of 100 ppb or greater Otherwise, for pollutants for which you mark column 2b, you must either submit atileast one analysis or briefly describe the reasons the pollutant,is expected to be discharged Note that there are 7 pages to this part, please review each carefully Complete one table (all 7 pages) for each outfall See instructions for additional details and requirements 2 MARK "X" 3 EFFLUENT 4 UNITS 5 INTAKE (optional) 1 POLLUTANT b MAXIMUM 30 DAY VALUE c LONG TERM AVRG I a LONGTERM AND a b c a MAXIMUM DAILY VALUE (rfavwla&o VALUE (�favailable) AVERAGE VALUE CAS NUMBER TESTING BELIEVED 'BELIEVED () () () d NO OF a CONCEN- () b NO OF (ifavaJable) REQUIRED PRESENT ABSENT CONCENTRATION I (2) MASS CONCENTRATION I (2) MASS CONCENTRATION I (2) MASS (ANALYSES TRATION b MASS CONCENTRATION I (2) MASS ANALYSES METALS, CYANIDE, AND TOTAL PHENOLS 1M Antimony, Total (7440 -36.0) 2M Arsenic, Total (7440 -38-2) 3M Beryllium, Total (7440-41 -7) 4M Cadmium, Total (7440 -434) 5M Chromium, Total (7440 -47 -3) 6M Copper, Total (7440 -50 -8) 7M Lead, Total (7439 -92 -1) 8M Mercury, Total (7439 -97 -6) 9M Nickel, Total (7440 -02 -0) 10M Selenium, Total (7782 -49 -2) 11 M Silver, Total (7440 -22-4) 12M Thallium, Total (7440 -28 -0) 13M Zinc, Total (7440 -66-6) ,14M Cyanide, Total (57-12-5) 15M Phenols, Total DIOXIN 2,3,7;8- Tetra- chlorodibenzo-P- Dioxin (176401 -6) a X X X X X X X X X X X X Pollutant maw be present in source wwter - -supp y wells and /oi Cape Fe+ir'River. X X XDESCRIBE RESULTS N/A EPA Form 3510 -2C (8 -90) PAGE V -3 CONTINUE ON REVERSE r CONTINUED FROM'THE,FRONT 2 MARK "X" 3 EFFLUENT 4 UNITS _ - -_ _ 5 ,I_NTAKE (opaonan_ 1 POLLUTANT b mAxiMUM301)AYVALUE(j c' LONG TERM AV,RG a LONGTERM ,AND a b c a MAXIMUMDAILY'VALUE' (ifm +affable) VALUE(rfavarlable) AVMR GEVALUE CAS NUMBER TESTING BELIEVED (1) (1) d NO OFD a CONCEN- b NO OF (1) r available REQUIRED if ) PRESENT ABSENT CONCENTRATION (2) MASS CONCENTRATION `(2) MASS' (2) MASS ANALYSES TRATION b MASS CONCENTRATION (2)IMASS ANALYSES GC /MS,,FRACTION - VOLATILE COMPOUNDS 1 V ,Accrolem \/ x (107 -02 -8) 2V Acrylonitnle x (1o7A3 -1) 3V ,Benzene (71 432) mrne Bos hlr ` rlrvl) Ether (542 -88=1) /X\ _ 5V Bromoform (75 -25=2) 6V-Carbon ' Tetrachloride X (5b:235) 7V Chlorobenzene 8V Chl \ / bromometha ne, th /X\ 9V Chlofoethane (7x00 -3), - ,10V 2;Chloro- ethylvinyl4Ether (110 -758) -- - - - - - - - 11V Chloroform (67 -66?3) - — - '12V `Dichloro- bromomethane, X (75-274) 13V Dichloro- ddluoromethane X (7571;8) �1ik 1,1- Dichloro- ethane (75-343) �15V- 1,,2- Dichloro -, ethane,(107- 06=2)' 16V 11,1- Di6hlCro- ethylenea(75 -354) - 117V 1;2- Dichlor"o- propanel(78 -87 -5) 18V 1,3- Dichi6io- \ / i Propylene X (542 -75-6) 19V' Ethylbeniene ,(10041 -4)� — - - - - 20V Methyl ,13romide(74 -83 -9) 21Y Methyl - Chioride (74 -87 -3) / EPA]Form,3510- 2&(8 -90) PAGE V=4 CONTINUE ON PAGE V -5 CONTINUED FROM PAGE V-4 2 MARK "X" 3 EFFLUENT 4 UNITS 5' INTAKE (opttonao 1 POLLUTANT b MAXIM_ UM 30 DAY VALUE c_ LONG TERM AVRG a LONGTERM AND a b c a MAXIMUM DAILY VALUE (rfavadable) VALUE (rfavadable) AVERAGE VALUE CAS NUMBER TESTING BELIEVED BELIEVED (1) (1) d NO OF a CONCEN- (1) b NO OF (ifavarlable) REQUIRED PRESENT ABSENT CONCENTRATION I (2) MASS C (2) MASS CONCENTRATION I (2) MASS ANALYSES TRATION b MASS CONCENTRATION I (2) MASS ANALYSES GC /MS FRACTION — VOLATILE COMPOUNDS (continued) 22V Methylene v Chloride (75 -09 -2) 23V rhio 2- ` , Tetrachloroethane X (79 -345) 24V Tetrtrachloro- ethylene (127 -181) 25V Toluene (108 -88-3) 26V 1,2- Trans- ` , Dichloroethylene X i1 ss- so='s) 27V 1;1,1 - Tnchloro- ethane (71 -55-6) 28V 1,1;2 - Tnchloro-\X, ethane (79 -00-5) 29V-Tnchloro- ethylene (79 =01_6) 30V Tnchloro-` fluoromethane /�[\ r (75 -69-4) _ 31V Vinyl Chlorde (7501 -4) GC /MS FRACTION —ACID COMPOUNDS 1A 2- Chlorophenol x (95 -57 -8) 2A 2,4Dichloro- phenol(120 -83-2) 3A - 2,4- Dimethyl- phenol (10567 -9) 4A 4,6- Dindro-0- Cres6l(534 -52 -1) SA ,2,4- Dimtro- x phenol(51- 28-5) 6A ,2- Ndrophenol (88 -755) 7A 4Ndrophenol (100- 02_7)_ 8A P- Chlwo-M- Cresol(59 -50-7) 9A Pentachloro- phenol (87 -86.5) 10A Phenol �' (10 &95-2) 11A 2,46- Tri6hloro- phenol (88 -052) EPA Form 3510 -2C (8 -90) PAGE V -5 CONTINUE ON, REVERSE CONTINUED FROM THE FRONT 2 MARK "X" 3 EFFLUENT 4 UNITS 5 INTAKE (oprronao 1 POLLUTANT b MAXIMUM 30 DAY VALUE c LONG TERM AVRG a LONGTERM AND a b c a MAXIMUM DAILY VALUE (rfaealab/e) VALUE (javarlable) AVERAGE VALUE CAS NUMBER TESTING BELIEVED BELIEVED 1 () (t) (1) d NO OF a_ CONCEN- (1) b NO OF (if mailable) REQUIRED PRESENT ABSENT CONCENTRATION I (2) MASS CONCENTRATION I (2) MASS CONCENTRATION I (2) MASS ANALYSES TRATION b- MASS CONCENTRATION (2) MASS ANALYSES GC /MS IFRACTION — BASE/NEUTRAL COMPOUNDS 1B Acenaphthene (8332 -9) _ 2B AcenapFrtylene (208 -96-8) 3B Anthracene (120 -12 -7) 48 Benzidine �/ (92- 87 -5)' x 5B Benzo (a) Anthracene (56 -55-3j 6B Benzo (a) x Pyrene (50 -32 -8) 7B 3,4 -Benzo- fluoranthene X (205 -99-2) 8B Benzo (Rhr) x Perylene (191 - 24-2) 9B Benzo,(k) Fluoranthene (207 -08-9) 10B Bis (LChloro- erhoxy) Methane (111 -91 -1) 11B Bis (2 -( hloro- erhyn Ether �/ x (111 -44-4) 12B Bis�(2- ChlororaopropvQ Ether (102 -80-1) 13B, Brs (2- Crhil- - hexy!) Phthalate (117 -81 -7) 14B 4- Bromophenyl Phenyl Ether �/ x (101 -55-3) 15B Butyl Benzyl �/ x Phthalate (85 -68-7) 16B 2- Chloro- naphthalene (91 -58-7) 17B 4- Chloro- phenyl Phenyl Ether �/ x (7005 -72 -3) 18B Chrysene �/ x (218 -01 -9) 19B Dibenzo (a h) Anthracene (53 -7a3) 20B 1.2- Dichloro- benzene(95 -50 -1) X 21B 1,3Di- chloro- x benzene (5417731) EPA Form 3510 -2C (8 -90) PAGE V -6 CONTINUE'ON PAGE,V -7 0 _CONTINUED�FROM PAGE V-6 2 MA_ RK "X" 3 EFFLUENT 4 UNITS 5 INTAKE (optrona! 1 POLLUTANT b ,MAXIMUM 30 DAY VALUE c LONG'TERM AVRG aL`ONG TERM AND a CAS NUMBER b c a MAXIMUM,DAIL - -Y VALUE _ _ (ifavadable) VALUE (rfavadab[e) d NO OF �a CONCEN= AVERAGE'VALUE b NO OF TESTING (ifavarlable) REQUIRED, BELIEVED PRESENT BELIEVED 1 O ABSENT_ CONCENTRATION ( (2) MASS (1)_ CONCENTRATION I (2) MASS (1) CONCENTRATION I (2MASS ANALYSES TRATION b MASS (1) CONCENTRATION I (2)WASS ANALYSES GO /MS FRACTION - BA_SE%NEUTRA_L COM_ POUNDS (cofiumn ed) 226 1,4 Dichloro- - benzene(106-46 =7) 236 3,3- Dichloro- benzidine (91 -94-1) x '246 ,Diethyl Phthalate,(8466 -2) 258 Dimethyl Phthalate (4 31 ,1 �1 -3)' _ 268sDi-N -Butyl iPhthalate,(8474 -2) _ 2713 ,2,44Dindro- toluene (12144 -2) X-- 286' 2,6 -Dmtro= - - toluenea(606 - 296- DiaN -Octyl - 1, � - - F5h-tthalatei(11,7 -84-0) x 306 -1,2- Diphenyl- hydrazine (as A`zo- benzene)(122 -6rr7) 3113 Fluoranthene 328 ,Fluorene (86- '73-7) X 3313 Hexachloro - be6iene;(118 -74-1) 348''Hexachloro- v butadienej87 -6 &3) 3513 Hexachloro I cyclopentadiehe X , (77 -47 -4) 3613 Hexachloro-v ethane (67 -72 -1) 3713 Indeno x(1,2,3 - -cd) Pyrene (193-39'5) 389 Isophorone X 39B Naphthalene �/ (91 -20.3) ^ - 140B Nitrobenzene - 41B N -Ndro- sodimethylamme y 75-9 (62- )' - 426 N- Ntrosodi= N- Propylamme (621 -647) �EPA,Form;3510 -2C (8 -90) PAGE V -7 CONTINUE ON REVERSE, CONTINUED FROM THE FRONT 2' MARK "X" 1 POLLUTANT AND a b c a MAXIMUM'DAILY VALUE CAS NUMBER TESTING BELIEVED BELIEVED (1) ffavudable) REQUIRED PRESENT ABSENT CONCENTRATION I (2),MASS GC /MS FRACTION — BASE/NEUTRAL`COMPOUNDS (conamtea) 43B N -Nitro- sodiphenylamme (86-30 -6) 446 Phenanthrene v (85 -01 -8) 45B Pyrene (129 -00-0) 46B 1,2,4 -Tri- chlorobenzene (120 -K -1) GC /MS FRACTION — PESTICIDES 1P Aldnn (309 -00-2) 2P a -BHC (319 -846) 3P ,(3 -BHC (319 -85-7) 4P y -BHC x (58 -89 -9) 5P b -BHC x (319- 86-8) 6P Chlordane x (57 -749) 7P 4,4' -DDT x (50 -29 -3) 8P,4,4'-DOE (72- 55-9) x 9P 4,4' -DDD (72 -548) 10P ,Dieldnn v (60 -57 -1) 11P a- Enosulfan (115 - 29-7) x 12P p- Endosulfan (115 -29 -7) _ 13P Endosulfan Sulfate (1031 -07 -8) 14P Endnn (72 -20-8) 15P Endnn Aldehyde (7421 -93-4) 16P Heptachlor (76 -448) 3 EFFLUENT b MAXIMUM 30 DAY VALUE (J available) (1) CONCENTRATION 1 (2) MASS 4 UNITS 5 INTAKE (optionan c LONG TERMAVRG a LONGTERM VALUE (�favatlable) AVERAGE VALUE d NO_OF a_ CONCEN- b NO OF CONCENTRATION I (2) MASS ANALYSES TRATION b MASS CONCENTRATION I (2) MASS ANALYSES EPA Form 3510 -2C (8 -90) PAGE V -8 CONTINUE ON PAGE V -9 See Attachment 5 for estimated average concentrations for selected parameters for the two new proposed internal outfalls. EPA 1. D. NUMBER (cant from Item ! ofI thin 1) NUMBER NCD000830646 IOUTFALL 001 (CC Block) CONTINUED FROM PAGE V -8 2. MARK "X" 3. EFFLUENT 4. UNITS 5. INTAKE (optionao 1. POLLUTANT b. MAXIMUM 30 DAY VALUE c. LONG TERM AVRG. a. LONG TERM AND a b e_ a. MAXIMUM DAILY VALUE ( {favatlahle) VALUE (tfuvuilahle) AVERAGE VALUE CAS NUMBER TESTING BELIEVED BELIEVED (1) (1) d. NO. OF a. CONCEN- (1) b. NO. OF (ifuvmluhle) REQUIRED PRESENT ABSENT CONCENTRATION I (2) MASS C (2) MASS CONCENTRATION I (2) MASS ANALYSES TRATION b. MASS CONCENTRATION I (2) MASS (ANALYSES GC /MS FRACTION — PESTICIDES (conrutued) 17P. Heptachlor ` , Epoxide X (1024 -57 -3) 18P. PCB - 1242 \/ x (53469 -21 -9) 19P. PCB - 1254 \/ x (11097 -69 -1) 20P. PCB -1221 (11104 -28-2) 21 P. PCB -1232 (11141 -16-5) 22P. PCB -1248 (12672 -29 -6) 23P. PCB -1260 (11096-82 -5) 24P. PCB -1016 (12674 -11 -2) 25P.Toxaphene (8001 -35-2) f � EPA Form 3510 -2C (8 -90) PAGE V -9 See Attachment 5 for estimated average concentrations for selected parameters for the two new proposed internal outfalls. Progress Energy Carolinas, Inc. NPDES Permit NC0001422 L. V. Sutton Electric Plant Permit Modification Application January 2011 Attachment 1 Form 1 - Item XI Maps N'. A16W Facility Property Boundary Intake : �• i' -I. ` ~r � r -. . y1•• � � '•'s'. r,r' , ,f'�� -''"' { ~y' V e C L T AN Sutton Plant Tank n Discharge j Outfall 001 Lk + Ale j "k 'PLY es t prox 119� A11-1