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HomeMy WebLinkAboutNC0005088_Renewal Application_20030128Duke � Pow er- A Dukr Energy Company January 27, 2003 Mr. David Goodrich North Carolina Department of Environment and Natural Resources Division of Water Quality 1617 Mail Service Center Raleigh, North Carolina 27699 -1617 Subject: Cliffside Steam Station NPDES Permit Application for Renewal of NPDES Permit No. NC0005088 Dear Mr. Goodrich: Duke Power Company Fossil and Hydro Generation Department P.O. Box 1006 Charlotte, NC 28201 -1006 The subject NPDES permit is scheduled to expire on July 31, 2003. As required by the North Carolina Administrative Code (15A NCAC 211.0105(e)), this permit application for renewal is being submitted at least 180 days prior to the expiration date of the current permit. In accordance with this requirement, please find enclosed in triplicate, the application for renewal. The following items are attached: • EPA Form 1 — General Information • EPA Form 2C — Application for Permit to Discharge Wastewater Existing Manufacturing, Commercial, Mining and Silvicultural Operations • Site Map • Supplemental Information to the NPDES Application o Characterization of NPDES related process and wastewater streams. o Schematic water flow diagram. • The Balanced Indigenous Population (BIP) Report Duke Energy Corporation requests a continuation of the current thermal limits at outfall 001. The attached Balanced Indigenous Population (BIP) Report concludes that the current NPDES permit's thermal limits provide sufficient protection to the aquatic population in the Broad River. Additionally, it should be noted that annual monitoring has been performed to support the NPDES permit thermal limits since 1990. Duke Energy Corporation believes that data collected during the twelve years of annual monitoring provides a sufficient baseline to characterize thermal considerations for the receiving water body. Therefore, a reduction in the annual monitoring program is requested. Duke Energy Corporation proposes to meet with your staff to discuss at a later date. In review of monitoring data, oil & grease test results for outfall 002 are significantly below the NPDES permit limit. For example, during the 12 month period of August 2001 to July 2002, the oil & grease monthly test results were all below detection except for one month in which the results were 6.5 mg/1. Thus, it is requested that the monitoring requirements for oil & grease be reduced from monthly to quarterly. Units 1 — 4 retired ash basin currently has a discharge tower that allows rainfall runoff to discharge to the Broad River. In close proximity, the yard drainage basin collects wastewater and rainwater and pumps it LL JAN 28 20 i._ ` NMI fi The subject NPDES permit is scheduled to expire on July 31, 2003. As required by the North Carolina Administrative Code (15A NCAC 211.0105(e)), this permit application for renewal is being submitted at least 180 days prior to the expiration date of the current permit. In accordance with this requirement, please find enclosed in triplicate, the application for renewal. The following items are attached: • EPA Form 1 — General Information • EPA Form 2C — Application for Permit to Discharge Wastewater Existing Manufacturing, Commercial, Mining and Silvicultural Operations • Site Map • Supplemental Information to the NPDES Application o Characterization of NPDES related process and wastewater streams. o Schematic water flow diagram. • The Balanced Indigenous Population (BIP) Report Duke Energy Corporation requests a continuation of the current thermal limits at outfall 001. The attached Balanced Indigenous Population (BIP) Report concludes that the current NPDES permit's thermal limits provide sufficient protection to the aquatic population in the Broad River. Additionally, it should be noted that annual monitoring has been performed to support the NPDES permit thermal limits since 1990. Duke Energy Corporation believes that data collected during the twelve years of annual monitoring provides a sufficient baseline to characterize thermal considerations for the receiving water body. Therefore, a reduction in the annual monitoring program is requested. Duke Energy Corporation proposes to meet with your staff to discuss at a later date. In review of monitoring data, oil & grease test results for outfall 002 are significantly below the NPDES permit limit. For example, during the 12 month period of August 2001 to July 2002, the oil & grease monthly test results were all below detection except for one month in which the results were 6.5 mg/1. Thus, it is requested that the monitoring requirements for oil & grease be reduced from monthly to quarterly. Units 1 — 4 retired ash basin currently has a discharge tower that allows rainfall runoff to discharge to the Broad River. In close proximity, the yard drainage basin collects wastewater and rainwater and pumps it to the present ash basin (outfall 002) for,additional treatment. The yard drainage basin presently has a "blocked off' emergency overflow discharge line that connects to a ditch that directs waterflow to the Units 1-4 retired ash basin's discharge tower. The potential exists for the yard drainage basin's pumps to be•damaged if the pump motors were submerged in water due to a system malfunction. Therefore, permission is requested unblock the emergency overflow discharge line and permit the retired, ash basin discharge tower as outfall'002A. This outfall is sirmlar to emergency sump overflow outfalls that have been permitted at other Duke Energy Corporation locations. Outfall 003 no longer discharges process cooling water. Previously, once through non - contact cooling water, from Units 1-4 transformers, was discharged through this outfall. These transformers have been converted to an air cooling system and no longer use once through non-contact-cooling water as their cooling source. Therefore, it is requesfe`d that outfall 003 be elimmated from the NPDES permit. If additional'mformation is needed pleaseycontact Robert Wylie at (704) 382=4669. Sincerely, Michael A. Ruhe, Manager Environmental, Health and Safety Fossil/Hydro Operations Attachments cc: Ms. Tris,MacPherson — NCDENR (BIP Report only) Cliffside Steam Station, Rutherford County NPDES # NC0005088/ Page 2 of 17� General Information Cliffside Steam Station (CSS) is located at 573 Duke Power Road, off NC State Road 1002 just south of Cliffside, North Carolina beside-the Broad- River. The five unit coal fired steam electric generating station has a combined rated capacity of 760 MW =net. Units 1 - 4 have a combined capacity, of 1,98 MW -net and a once- through Condenser Cooling Water (CCW) maximum flow rate of 4.17 cfs. Unit 5 has a capacity oU562 MW- net and utilizes closed cycle, forced draft cooling towers for heat dissipation. Unit '5 cooling tower make -up water is withdrawn at a maximum rate of 14_cfs and the blowdown is discharged to the ash basin. .CSS utilizes waters from the Broad River for the CCW and other service water systems. The .service water required �by units 1 - 4 is initially pumped to a, settling basin for sedimentation of sand and silt before it is taken into the plant. 'Unit, 5 can acquire intake water from either; the unit 4 screen room (normal operation) or from the condenser cooling water discharge of unit's 3 and 4. The intake water for unit 5 flows to a storage tank before entering the unit. A schematic flow diagram of water use, treatment, and discharge is attached. A discussion, of the individual waste streams follows._ EOutfaIII-U01 -Condenser Cooling Water ( M,Units 1- 4 s Units 1 - 4 utilize raw river water for` once - through-- non- contact_conden`'ser - cooling =water requirements. This water system removes heat from the condensers and other selected heat exchangers. No biocides or other - additives are used in the condenser cooling water. There are two condenser circulating pumps per ,condense'r /unit for units 1 - 4. Rawiriver water is pumped through the condensers for cooling. Annually, the condensers may be opened and cleaned by forcing plugs through the tubes. The plugs are collected within the cooling water system prior to being discharged into the Broad River. Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 3 of 17 Approximately twice per year, the condenser tubes may need to be tested for leaks. This test is conducted using a tracer gas (i.e., sulfur hexafluoride, helium, etc.). The levels of discharge will be well below any levels of aquatic biological toxicity concern. If a leak was detected, any release to the environment will only occur during short intervals (approximately thirty seconds per injection, normally less than six injections per condenser) as the tests are being conducted. The entire test period per unit is normally conducted in two or three hours. Units 1 - 4 CCW Pump Maximum Capacity Unit # 1 -Pump Operation 2 -Pump Operation gpm gpm 1 19,800 39,600 2 19,800 39,600 3 28,125 56,250 4 28,125 56,250 Operational schedule for these pumps is dependent upon the intake water temperature and on the unit loads. Depending on the electrical demand, pumps are operated to maximize CSS efficiency and to assure compliance with its permitted NPDES thermal and flow limits. Flow recorded on the monthly Discharge Monitoring Reports (DMR) is based on CCW pump run times. Closed Cooling Systems Unit's 1-4 Recirculated Cooling Water (RCW) system is used for cooling various station components. The CCW system is used to cool the RCW system. The RCW system is a relatively small closed cooling system that uses maintenance chemicals (microbiocides and corrosion inhibitors) in order to prevent biofouling and system corrosion. The primary corrosion inhibitor used in these systems is sodium nitrite. The potential exists for minor plate leaks to occur. For units 1-4 if a plate leak occurs, the leak will discharge into the CCW system. Routine system monitoring for nitrite concentrations and make -up water, provides input that assists in determining a tube leak. Once a leak is identified corrective measures will be implemented to minimize and repair the leak. During a leak the concentration of the maintenance chemicals will not exceed the No Observed Effect Concentration (NOEC). The closed cooling water Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 4 of 17 systems for Unit 5 include the RCW and chiller systems. Both of these systems use microbiocides and corrosion inhibitors. The RCW and Chiller systems are required to be cleaned periodically. The cleanings normally use a dispersant, wetting agent and detergent. In addition leak detection is conducted using a fluorescing dye. While these are closed systems, they are drained on a non - routine basis,, as necessary for,maintenance, to the sump and pumped to the ash basin (outfall 002). Intake Screen Backwash The CSS intake screens are continuously backwashed during unit operation. The wash water is taken from the service water system (raw water). An average flow of 3000 gpm is utilized. The debris collected on the screens consists of twigs, leaves and other material indigenous to the, river, and is therefore flushed back to the river. Hydrogen and Oil Coolers Once through non- contact cooling water is supplied from the Low Pressure Service Water System that draws water from the CCW system to hydrogen and oil coolers. The system consists of four Low Pressure Generator Hydrogen Coolers and two Turbine Lube Oil Coolers for each unit=. ` Discharge from these coolers combines with the condenser cooling water flow and discharged at outfall 001 Station Equipment Cooling Water Once through non- contact cooling water is supplied from .the Low and High Pressure Service Water System to the bearings of the induced draft (ID) ; and forced draft (FD) fans to remove excess heat. No chemicals are added to the once through raw lake water discharged to the -Broad River. 10Utfa11=002 -Ash Basin The ash basin is the primary treatment system for waste water produced, at Cliffside Steam Station. The ash basin treatment consists of sedimentation,— _ion7exehange= andvpH =adjustments. The ash basin's pH is adjusted using sulfuric acid. The additions of carbon dioxide and also sodium hydroxide are under review for pH control. Additionally, aluminum Cliffside,Steam Station, Rutherford County MIMES # NC0005088 Page 5 of 17 sulfate is being reviewed for use as a coagulant in order to further settle out solids. Wastewater from Air Pollution Control Systems At Cliffside Steam Station waste water streams that are generated from the operation of air pollution control systems, are sent to the Lash --basin. The following, provides a� brief, description of these waste stream's in addition, to the .above mentioned fly ash sluicing system. Continuous Emissions Monitors Continuous Emissions Monitors, produce potassium permanganate during normal operation at a ,rate of approximately 2 pints /month. This waste stream is sluiced' to the ash basin. Flue Gas Conditioning For increased precipitator performance, anhydrous ammonia and sulfur trioxide ($03) gases are injected into the gas stream prior to Unit 5's precipitators- The injection of the gases increases the efficiency of the precipitators and the injection rate varies to prevent ammonia and SO3 slippage through the precipitator. The designed maximum injection rate for ammonia is, 15 ppm and 12 ppm for the sulfur trioxide. The ammonia and sulfur concentrations will not significantly increase in the ash basin from this flue gas conditioning system. Selective. Catalytic Reduction (SCR) 'Unit 5 has a Selective Catalytic Reduction unit installed in the gas Y path prior to the preheater. The SCR uses anhydrous ammonia and a catalyst to convert nitrous oxides to nitrogen and water vapor. The flow rate of anhydrous ammonia depends upon the level of reduction on nitrogen oxides, the flue gas emission rate, and the slip through the SCR. The slip rate for anhydrous ammonia through the SCR is projected to be less than 2 ppm. The design injection rate of ammonia is 400 Ibs /hour. During operation fly ash may absorb low concentrations of ammonia. Fly ash for Unit 5 is primarily collected and sent to a silo, for off -site use. iPeriodically the fly ash is sluiced to the site's ash basin. The ammonia concentrations are not Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 6 of 17 expected to significantly increase in the- ash basin from the SCR operation. Selective Non — Catalytic Reduction (SNCR) In the future, Units 1-4 may have SNCR systems installed to lower Nitrogen Oxide (NOX) emissions. SNCR systems operate by 'injecting urea into the upper section ,of the boiler, where a chemical reaction will occur, to reduce the NOX,to water and nitrogen. Some residual ammonia may be collected onto the fly ash and sent to the ash basin. However, the operation of the SNCR systems is not expected to require additional treatment capabilities to ensure compliance with NPDES permit limits. ,Flue Gas Desulphurization In the future, 'Unit 5 plans to install a Flue Gas Desulphurization (FGD) system to reduce the SO2 in the stack gas. The FGD system will discharge blowdown waste water to the ash basin. Operation of the FGD system will be evaluated to determine if additional, treatment capabilities will b& required to ensure compliance with NPDES permit limits. Notification of the proposed installation of a FG'D system will be communicated to address any permitting concerns. Cooling Towers Unit 5 utilizes two cooling towers for its cooling water requirements. Unit 5 has four circulating pumps. Each circulating condenser pump has a capacity of 62,500 gpm for a combined total of 250,000 gpm. The circulating pumps on unit 5 operate continuously. Each tower has a circulation rate of 125,000 gpm with a make -up rate of 2875 gpm per tower and a blowdown rate of approximately 2500 gpm. The cooling tower blowdown is pumped to the ash basin. Cooling tower water is chlorinated to approximately 0.5 ppm, for,one half hour, 3 times /wk during the winter and approximately 1.0 ppm, for one hour,, 5 times /week during the summer months. Fifty gallons, of the microbiocide iBu°lab 6002 are added approximately every 6 months, to each tower. The towers are sprayed with, the microbiocide Bulab 6009 once yearly. Mechanical means are employed for additional cleaning., Cliffside Steam Station, Rutherford County NPDES #'NCooO5088 Page 7 of'17 Sanitary Wastes The sanitary wastes from Units 1� 4 ,are treated Eby a,'2500 gpd -capacity, septic tank. The Unit 5 sanitary wastes are treated by an activated, sludge unit with a 3000 gpd capacity. An average of fifty people contribute for,the ,load oa the 2 systems. The effluent, from both systems, is ,pumped to ,the yard' drainage basin and then to -the ash basin,: The water "for the sanitary waste systems and the drin'ki'ng, water system ,is supplied by the Grassy Pond 'Municipal water°system. Storm Water The ash basin ,at CSS, collects %receives flows from the yard drainage basin, ,ash removal lines, and` rainfall run -off from the basin "watershed area: The average rainfall Arun-off flows are based on 49 inches of rain per year with 100% run -off, from thelpond, surfaces and 50% run -off from, other areas.. , The average rainfall run -off for the °ash basin watershed area ,is -0.640 MGD. The ,coal yard drainage at Cliffsi'de, Steam- Station drains to� the yard drainage basin :and is then pumped ,to the ash basin. The, coal yard `has. an averaged run -off'of 0:027 M'GD., Cliffside, Steam Station, has, several stor =m water outfalls, that ,discharge to the,15road River. These storm drains do notcontain any process wastewater discharges.. On the main entrance road to the site, �a,natural spritig/dreek flows continuously in the road ditch. The water enters the storm ,drainage system and flows directly to the Broad 'River. Cliffside Steam, Station was included in the group application submitted, to the,Envi'ronmental ,Protectio Agency in March 1991. CSS maintains a site St'orrii 'Water �Pollu�tion, Prevention Plan (SWPPP) to minimize the discharge of ,pollutants in the storm water discharges. Boiler- Chemical Cleaniog Boilers#1 and, #2 at ,CSS are not chemically cleaned. Boilers #3, #4; and #5 are chemically cleaned as needed. The wastes 'produced from a boiler dleaning are, pum,ped to the ash basin, The chemical's and approximate amounts for leach cleaning are Ii'sted below. Chffside Steam Station, Rutherford County NPDES # NC0005088 Page.8 of 17 Cherni'cals Unit 3 or4 Unit 5 Sodium bromate - -- 550 Ibs Ammonium carbonate - -- 100014S Ammonium hydroxide, 260 Be * - -- 1000 gal Hydrochloric acid, 200 Be * 3300 gal 9000 gal Thiourea * 1000 Ibs 2900 Ibs Ammonium biflouride 1000 Ibs 2700 Ibs Proprietary Inhibitor 24 gal 130 gal Citric acid 200 Ibs 600 Ibs Soda Ash 2000 Ibs 5600 Ibs Sodium sulfite - -- 100 Ibs Iodine 213 24 gal 130 gal Approximately 220,000 gals of wash water are required for cleaning boilers #3 or #4. Boiler #5 requires 950,000 gals of wash water per cleaning. Immediately, prior to the beginning of a boiler chemical cleaning procedure, additional ,stop logs are added to the ash basin discharge structure. This assures longer retention time of the chemical, wastes for proper treatment through dilution, neutralization, precipitation and ion - exchange. * During a chemical metals cleaning these chemicals are present in ` amounts greater than the reportable quantity as identified under the Comprehensive Environmental Response, Compensation, and Liability Act (CERCLA). If a spill of any these chemicals were to occur, in most cases, it would be routed to the ash basin for treatment. Per 40 CFR 117 the chemicals that are routed to the ash basin are exempt from reporting -• requirements. Floor Drains, CSS floor drains contain boiler blowdown, leakage from seals, equipment cooling water, condensates, regeneration wastes, miscellaneous plant wastes and area wash down water. Effluents from these drains are flushed to the, plant sumps and then to the yard drainage basin and are then pumped to the ash 'basin. The floor drains in the powerhouse connect to sumps where they are pumped to the ash basin. These drains can receive inputs from spillage or leakage, floor wash water, as well as flows from water treatment Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 9 of 17 processes. The following are examples of materials that are stored inside the powerhouse: sulfuric acid sodium hydroxide water treatment chemicals ammonium, hydroxide . industrial cleaning products used for general housekeeping hydrazine oil, lube oil (recycled) Ash Basin Toe Drains In order to assure the integrity of the ash basin's dike structure, the dikes are designed with, a system that, allows for the water to seep through the dike. This drainage system prevents the dikes from becoming overly saturated'with water. This water is discharged out of the dikes via toe drains. The volume of water is normally, at a nominal seeping rate. It discharges to the ground and is ,ultimately routed' to Suck Creek and Broad River. Water Treatment System The CSS make -up water treatment system (non- potable) is comprised of: (a) a clarifier, (b) three gravity filters, (c) two activated carbon filters, (d) chlorination, (e) two mixed bed demineralizers, (f) a polisher and (g) a reverse osmosis process. Make -up water is supplied to the boilers to generate steam to turn the turbines. On occasion a vendor may be used with a mobile water treatment unit to augment the facility•water treatment capacity. Any vendor will use traditional water-treatment methods, chemicals; and disposal methods, generally described. below. The water treatment wastes consist of (a) flocculants and' sedimentation, (b) filter backwash, (c) demineralizer regeneration wastes, and (d) reverse osmosis wastes. This waste is sent to the ash basin. Clarifier The clarifier currently utilizes a continuous feed of cationic water treatment polymer and clay (Nalco 8105 and Nalco Coagulant AID 25, respectively or, similar products) to remove suspended solids and Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 10 of 17 colloidal material. The flocculent and sedimentation collected by the clarifier consists of solids that were suspended in the service water. Approximately 1000 GPD of sedimentation wastes are pumped to the yard drainage basin and then to the ash basin. The station may alter this process to supply site clarified water by other traditional water treatment methods and using traditional chemicals other than those listed above. JUDv Gravity Filters There are three gravity filt`er's composed ofanthracite (coal) which follow the clarifier in the water treatment process. Each of these filters has a capacity of 360,000 GPD. One of these filters is backwashed once per day with the backwash_ water going to the ash basin. The gravity filters are changed out on an as- needed basis with, the spent filter medium going to the ash basin: Activated Carbon Filters Two activated carbon filters are backwashed and steam cleaned once per,month. The,wash water is pumped to the ash-basin. The activated carbon filters are changed out approximately twice per year with approximately 147 ft3 of activated carbon being pumped to the ash basin. Desrninerailiiers Demineralized water, is used to supply the plant with its make -up water requirements. Each demineralizer consists of two mixed bed cells,. Only one demineralizer is in operation; at a time. A demineralizer is regenerated once per week. A regeneration requires 39.5 gallons of 66013e sulfuric acid and 150 gallons of 50% sodium hydroxide. Approximately, 10,000 gal of rinse water is used .per regeneration. Double regenerations are required for each regeneration. The dilute acid and caustic are discharged to the floor drains simultaneously through the same header for neutralization purposes. The, demineralizer resin is changed out approximately every seven years with the waste resin being pumped to the ash basin. Approximately, two times- a year each d'emineralizer is brine treated to clean the resin. This process uses approximately 3000 Ibs of salt (sodium chloride) and filtered water for each demineralizer treatment. All regeneration wastes are pumped to the ash basin. Cliffside,Steam Station, Rutherford,County °NPIDES4 NC0006088 ` Page 11 of 17 Cooling water for the ,unit 5 stator ,cooler,goes through an additional �dernineralize_r- The ,demineralizer resin is changed out approximately every, 18 months with approximately 9 cubic feet being pumped to the ash basin. Polisher A fifty cubic foot polisher (20 cubic Reef cation, 30 cubic feet anion resin) ;is used to, popish d'ernineralizer effluents.- Th'i`s ;polisher will minimize silica leak8ge. The resin will be, replaced anmally with spent r-esi`n being pumped to the -ash basin. �- Reverse ,Osmosis A Reverse Osmosis (RO), unit is used at'`Clfffside Steam Station to decrease the conductivityAn the de *ineralizer snake -utp water., 'The, RO unit treats 400 ,gpm with 100 �gpm rinse water.. This rinse water drains to the yard settling,,basin and then is, pumped to the ash basin. The 'RO, unit increases the efficiency, of the demineralizers. Sulfuric acid (25 %)' is injected, at approximately,5, gal %day. 'This controls ,the unit's pH.' Sodiu.*hisulfite i5jhen injected downstream of the SRO unit to remove any residual chlori'ne.- The concentration of sodium bisulfite is maintained at 2 ppm. The RO unit is cleaned on a quarterly, basis with the, rNaste going to the yard drains aqd eventually the ash basin. During a cleaning, approximately,30 Ibs ,of the cleaner, OSMO AD -20 containing °sulfarhic acid, citric acid anti •sodium lauryl sulfate is, used_ Also, used is a generic cleaner consisting of tfi; sodium ;phosphate, sodium laurylsulfate and sulfuric acid with ,approxirnately'40G gallons of waste water going to the ash` basin. JDd f Boiler BloWdown Boilers 1' - 4 each blowd`own at a rate of approximately 500 Ibs,. of steam %hour. Most of the bl'owdoWh is vented to the atmosphere With a minimal amount going to, the, boiler, room fl'gor draih& The blowdown from unit 5, is vented to a bl`owdown tank, With 8 mini -mal flow of condensate being, pumped, to the ash basin. Hydrazine, is maintained at a concentration of <30, p0b, in the feed water train for deoxygenation., Ammonium,'hydroxJde ,i's used for .pH control in the units: A, minute arno`unt, of fh„ydra2ine ,( <10 ppb) may be Cliffside Steam, Station, Rutherford County NPDES # NC0005088 Page 12 of 17 present in the steam jet air ejector waste condensate flow to the floor drains which are pumped to the ash basin. Oil Storage Run -Off CSS currently has 8 above ground oil storage tanks and one �und'erground gas tank (1,000 gal). The total above ground storage capacity is 125,300 gal. All above ground tanks are surrounded by concrete dikes. Any spill not contained by the dikes would be drain to the yard drainage sump system. The spill will be cleaned up within the yard drainage sump system. The yardisump system pumps wastewater to the ash, basin. If for some reason a spill is not completely cleaned up within the yard sump system it will be cleaned up in the ash basin. The underground gas tank ,is of double- walled fiberglass construction. All oil storage facilities and oil- filled equipment are presently covered under the Spill Prevention Control and Countermeasure Plans (SPCC). ,Outfall 002A —Yard Drainage Basin Overflow An overflow pipe directs flow from the yard drainage basin in the event that the basin's pumps malfunction. _ This'is_a very rare- event. Routine inspections and system alarms alert Cliffside operators when a high level alarm is, reached. The operators' response will normally prevent an overflow from occurring. However, this design is needed in order to protect, the pump motors from being submerged and damaged. Miscellaneous Waste Streams Dredging The intake at CSS is dredged on an as needed basis. All Hof the dredge discharge, is pumped to the yard drainage basin.. The yard drainage basin is dredged as needed with the dredge spoil going to the ash basin. In addition to this process, sand mining is, also permitted. The sand mining operation is permitted under permit 23 -16. 'During this operation sand material is pumped from the ,bottom of the river,and settles out on land. The effluent from, this operation discharges back Cliffside Steam Station, Rutherford County NPDES #,NC0005088 Page 13 of 17 to the Broad River. This discharge is permitted under NPDES general permit MG520000 (Certificate Number NCG520067): 'Laboratory Wastes The chemistry lab on site performs a variety ,of water analyses and routine sample collections. Therefore, several chemicals/reagents are used in the lab in small quantities for sample preservation, equipment calibration, analytical analyses, etc. The wastes, are poured down the sink, flushed to the activated sludge unit and "then pumped to the ash basin. Boresonic Rotor Testing Approximately once per year, one turbine is tested for cracks in the generator shaft using an ultrasonic nondestructive test. During the process a maximum of 400 gal of demineralized water mixed with 4 gal of corrosion inhibitor is used and is, pumped to, the ash basin. Condenser Leakage, Testing Occasionally, the condensers are tested for in leakage. This involves filling the steam side of the condenser with demineralized water and using a disodium fluorescing dye. The maximum yearly usage of the dye would be 6 Ibs of dye in 90,000 gal of water. All wastes are pumped to the ash basin. Heat Exchanger Cleaning On average, one heat exchanger per month is cleaned of mud fouling with 40 gallons of tri- sodium phosphate (1 %) and sodium hydroxide (5 %). The mixture is then discharged to the sump and pumped to the ash basin. Vacuum Trucks Commercial vacuum trucks are used to remove sediment from various pits and trenches. The material will be deposited in the yard drainage basin or the ash basin. Vacuum trucks are also used to vacuum areas of the plant that can not be washed with water, to the plant sumps. This material is hauled to the ash basin for disposal. Cliffside Steam Station, Rutherford County NPDES # NC0005088 Page 14 of 17 Vehicle and Equipment Washing The site vehicles are planned to be hand washed with mild detergent once a month. The rinse water will be routed to the yard drainage basin and pumped to the ash basin. An employee vehicle rinse station is used by the site employees to rinse their- cars. The employee drives their vehicle through a curtain of water spraying through nozzles. No detergent is'used for the employee's vehicles. The rinse water is routed to the yard settling basin and pumped to the ash `basin. During maintenance activities some plant equipment is washed with a steam cleaner. If possible, this equipment is moved into the tractor shed. This allows the rinse water to drain into an oil separator prior to be discharged to the yard drainage basin. Photographic Waste Streams Periodically welding operations occur at Cliffside Steam Station. In some situations the wel'dsl are x -rayed -to verify completion. During this process, a low volume photographic waste stream is generated. The waste stream is primarily composed of rinse water. This waste stream is analytically characterized to ensure that it is not a hazardous waste prior to be discharged 'into the ash, basin. Hazardous ,and Toxic Substances Table 2c -3 At Cliffside, the potential for toxic and hazardous substances being discharged is very low. In reference to Item, V -D of Form 2 -C, the substances identified under Table 2c -3 that may be in the discharge are as follows: Acetaldehyde, Alkanolamine, Asbestos, Butyl Acetate, Cyclohexane, Cyclohexanone, Epichlorohydrin, Formaldehyde, Monoethylamine, Naphtentic Acid, Pyrethrins, Vanadium, Vinyl Acetate, Xylene and Zirconium. Cliffside Steam Station, Rutherford County NPDES,# NC000508& Page 15 of 17 40 CFR 117 and CERCLA.Hazard'ous Substances The following table identifies hazardous substances located on -site that may be released to the ash basin during a spill in quantities equal' to or greater than the Reportable Quantity (RQ) levels as referenced in 40 CFR 117, 302' and' 355. This list is being provided 'in order to qualify for the spill reporting exemption provided in 40 CFR 117 and the Comprehensive Environmental Response Compensation .and, Liability Act (CERCLA). 'These values below represent the maximum quantities on -site that could be released at one time, and sent to the ash basin. They do not necessarily reflect quantities that are discharged through typical use. List of Hazardous Substances SUBSTANCE APPROXIMATE SOURCE Reportable QUANTITY Quahtity (Lbs.) Two 45,000 gallon tanks of Anhydrous Ammonia are located, at Cliffside Steam Station., This product is used in the SCR system. If a leak did occur from these tanks an emergency fogging system would immediately initiate. This would result in an ammonia water mixture which would be captured into the containment system that surrounds the two tanks. The discharge from the secondary containment system is ,normally closed by ,a valve. When open the discharge drains into the yard drainage basin which pumps to the ash basin. The adjacent unloading areas for these tanks also drain to the yard drainage basin. Balanced and Indigenous Populations Attached is the report entitled "Assessment of Balanced and Indigenous Populations in the Broad River near Cliffside Steam Station ". This report concludes that the operation of Cliffside Steam Station did not have an adverse impact on the balance indigenous aquatic communities in the Cliffside Steam Station, Rutherford County v NPDES # NC0005088 ~ Page 16 of 17 e. Broad River. Duke Energy Corporation therefore requests a continuation of the current NPDES thermal limits for outfall 001. Ash Basin Capacity ,Part CII B (1) of the existing NPDES permit for Cliffside requires the permittee to provide and maintain at all times a minimum free water volume (between the top of the sediment level and the minimum, discharge elevation). The sum of the maximum 24 hour plant discharges plus all direct rainfall - and all runoff flows to the pond resulting from a 10 year, 24 hour rainfall event, when using a runoff coefficient of 1.0 equals 213.1 acre -feet. The ash basin was last surveyed for its level of sediment ;in December 19,92. The amount of sediment to accumulate in the ash basin since December 1992 is based on coal consumption and ash content of the coal., It is estimated that from 1992 through 12/31/2008 the volume of solids to the ash basin will be 1,069 acre -feet. The required storage volume equals the summation of 1,069 and 213 or 1,283 `acre -feet. The available storage capacity based on the 1992 basin survey is 1,458.0-acre-feet. Therefore, sufficient capacity 'is ,available through December `31, 2008.- o 0 IM — E J � o O N of 00 cd 00 �o cd o 03 O Z O �w oU Z -d ct b .0 U W CISA �:z l c L L « �m{o r L3 1 0 U �za— aleiul JoleM MAIN pea8 a m 0 L 0 Nc t7 Q c 0 a c m N+ N � 7 0 N mmE m v N m �anib pea8 t N 0 0A mrom 0 v E a a m E � � d me to _ U W L 41 � U; E c N c m m t N Q E a a m E � � d me to _ U W L 41 � U; E N 0 C NN a co `o Ow 0 7 L N� Q c� 4-r 0 mW 41 0 U; c 41 om R L a0 U_ N 0 c « 0 �o w L m v3 C LLm r, m a 0 N a co `o Ow 0 7 L N� Q c� 4-r 0 WASTE WATER FROM X -RAY OPERATION AT CLIFFSIDE STEAM STATION .s Subject: WASTE WATER FROM X -RAY OPERATION AT CLIFFSIDE STEAM STATION Date: Tue, 3 Dec 2002 13.37.26 -0500 From: "Robert.R Wylie" <rrwylle @duke- energy com> To::Natal'ie.Slerra @ncmall.net CC: "Randolph W Price" <rwpnce @duke- energy.com> Natalie„ At Belews Creek Steam Station the same process that was used a't Clif'fside Steam Station of x- raying welds for boiler tube work is scheduled to begin in January -2003. It will be conducted over approximately a 5 month period. The process will not occur each day On th_e days that welding occurs it is estimated that approximately 55 gallons of waste water may be generated The current plans are to send this wastewater to the ash basin. The ash basin has a long term average flowrate of 7.7 mgd with an estimated ash basin capacity of 1„26,0 million gallons (at pond elevation of 752 +0 feet msl). Thus based on the analysis below and the low volume of this waste stream there should not be any significant Changes to the ash basin's waste water Your approval of this'process is requested If you need additional information please feel free to contact Randy Price (336) 445 -:0324 or me ('704) 382 -4669 Thanks, Robert - - - -- Forwarded by Robert R Wylie /Gen /DukePower on 12/03,/2002 01:13 PM Robert R Wylie < Natalie Sierra @ncmail.net> 03/'27/2002 01:06 Hodges /Gen /DukePower @DukePower PM OPERATION AT CLIFFSIDE STEAM STATION Natalie, To: Natalie Sierra CC: Steve D Subject: WASTE WATER FROM X -RAY As we discussed yesterday, at Cli.ffsi.de Steam Station (NPDES permit 0005088) the process of k- raying welds for boiler tube work, has generated wastewater that needs to be disposed. During the process the wastewater was /is being collected in,drums An analysis has been performed on the waste already collected. The results of this analysis is below. Currently there is approximately 500 gallons of wastewater and used developer from this process that has been collected in drums It is estimated that up to 5,00 gallons more wastewater and used developer- will be generated from the process for a total of 1,000 gallons Based on the analytical results (below,) it is requested that this non - hazardous waste be disposed of in a controlled amount into the station power house sump which, discharges ultimately into the ash basin (permitted NPDES Outfall 002) available capacity estimated > 100 mgal. The long term average flowrate from the ash basin is 10 mgd,. I wi -11 be out of my office from 3/28/02 until 4/8/02 Please feel free to respond to Steve Hodges (,sdhodges @duke- energy,com or 828 - 657 - 233,9) once you 1219/02 4 05 PM WASTE'W°ATER FROM' XLRAY'OPERATION AT CLIFFSIDE STEAM STATION s - ,i have'had a chance to determine an acceptable disposal rate. Thanks, Robert -`------=---------+--------- =-------- +- -------- - - - --- _ --- '+-------- - - - - -- ----- Parameter (Waste Water (mg /l)jUsed Developer ITCLP Limit (mg /l) 1(mg /1) ------------------ +------------------ +--- - - - - -- +----- - - - - -- -- Silver 14 7 10.49 15 ------------------ +----- - - - - -_--------------------------------------------- Barium 10.05 10.1 1100 _ ------------------+------------------+-------------------+---_-------------- Cadmium 1 <0.3 1 <0.3 11 --- - - - - -- ----+------------------+------------------+------------------ Chromium 1<0 4 10.6 15 -----+------------ _=------------------- - -- --+------------ - - - - -- Lead <0 9 14.4 15 ---------- ------------------------ __-- +-------- - - -_ -- __- +----- - - - - -- ------- Arsenic 1' <0'.1 1<0 1 1'5, - - - - - -- ----------+---------_-__-----+-----_------- WASTE,*WATER FROM X -RAY OPERATION AT CLIFFSIDE STEAM STATION .s Subject: WASTE WATER FROM X -RAY OPERATION AT CLIFFSIDE STEAM STATION Date: Wed, 27 Mar 2002 13:06:53 -0500 From: "Robert R Wylie" <rrwylie @duke- energy.com> To: Natalie Sierra <Natalie.Sierra @ncmai1.net> CC: "Steve D Hodges" < sdhodges @duke- energy.com> Natalie, As we discussed yesterday, at Cliffside Steam Station ( NPDES permit 0005088) the process of x- raying welds for boiler tube work, has generated wastewater that needs to be disposed. During the process the wastewater was /is being collected in drums. An analysis has been performed on the waste already collected. The results of this analysis is below. Currently there is approximately 500 gallons of wastewater and used developer from this process that has been collected in drums. It is estimated that up to 500 gallons more wastewater and used developer will be generated from the process for a total of 1,000 gallons. Based on the analytical results (below) it is requested that this non - hazardous waste be disposed of in a controlled amount into the station power house sump which, discharges ultimately into the ash basin (permitted NPDES Outfall 002) available capacity estimated > 100 mgal. The long term average flowrate from the ash basin is 10 mgd. I will be out of my office from 3/28/02 until 4/8/02. Please feel free to respond to Steve Hodges (sdhodges @duke - energy.com or 828 - 657 -2339) once you have had a chance to determine an acceptable disposal rate. Thanks, Robert ---------------+---------------+---------------+--------------- Parameter lWaste Water JUsed Developer JTCLP Limit 1(mg /1) 1(mg /1) 1(mg /1) ---------------+---------------+---------------+--------------- Silver 14.7 10.49 15 ---------------+---------------+---------------+--------------- Barium 10.05 10.1 1100 ---------------+---------------+---------------+--------------- Cadmium 1<0.3 1<0.3 11 ---------------+---------------+---------------+--------------- Chromium 1<0.4 10.6 15 ---------------+---------------+---------------+--------------- Lead <0.9 14.4 15 ---------------+---------------+---------------+--------------- Arsenic <0.1 <0.1 15 ---------------+---------------+---------------+--------------- Selenium 10.1 10.1 I1 ---------------+---------------+---------------+--------------- Mercury <0.01ug /g 1<0.01 ug /g 10.2 ---------------+---------------+---------------+--------------- % ash 10.11 1 1 ---------------+---------------+---------------+--------------- BTU 10 1 1 --------------------------------------------------------------- Total Sulfur 1<0.01 ---------------+---------------+---------------+--------------- Ignitibility >94 1 1 ---------------+---------------+---------------+--------------- pH 19.1 1 1 ---------------+---------------+---------------+--------------- % Water 177 1 1 1 of 2 4/2/02 4:31 PM W,ASTE,WATER FROM X -RAY OPERATION AT CLIFFSIDE STEAM STATION ---------------i---------------i---------------i---------------- 1 Total Halides <500 ---=-----------+---------------+---------------- +---------- - - - - -� COD 1831.1 1---------------+---------------+----------- _--- +-----=---- - - - - -� 2 of 2 4/2/02'4 31 PM