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HomeMy WebLinkAboutNC0000396_Permit Modification 2004_20040510 1• Progress Energy 9 CERTIFIED MAIL 7003 1680 0002 1069 8380 File No.: 12520A Date: May 10, 2004 Ms. Susan Wilson O V North Carolina Department of Environment and Natural Resources Division of Water Quality 1617 Mail Service Center 3 Raleigh, NC 27699-1617 �`( , vN`-`c� Subject: Progress Energy Carolinas, Inc. (PEC) var" Asheville Steam Electric Plant ,0041: 00' NPDES Permit No. NC0000396 NPDES Permit Modification - Flue Gas Desulfurization A : ewater Dear Ms. Wilson: As was discussed and emailed to you on March 17, 2004, by Louise England of Progress Energy Carolinas, Inc., enclosed is an amendment to the NPDES permit application for Asheville Steam Electric Plant. Previously water from the ash pond was to be used as chloride dilution water. Because the additional metals loading from the ash pond water would have required a much larger constructed wetland, the decision has been made to use water from Lake Julian as chloride dilution water. Water from Lake Julian will be combined with the clarified FGD water prior to entering an equalization basin. The discharge of the equalization basin is routed through the wetland and is then combined with ash pond effluent and discharged to the French Broad River via Outfall 001. Enclosed is a table with expected concentrations of parameters in the scrubber wastewater and revised Attachments 2 and 3 of the NPDES permit application. If you have any questions regarding any information in this submittal please call Louise England at (919) 362-3522. 1 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. l am aware that there are significant penalties for submitting false information, including the possibility of fines and imprisonment for knowing violations. Sincerely, William A. Phipps Plant Manager—Asheville Plant Progress Energy Carolinas,Inc. Asheville Steam Plant 200 CP&L Drive Arden,NC 28704 • • / Progress Energy Carolinas, Inc Asheville Steam Electric Plant FGD Blowdown Estimated Concentrations The flowrate of the FGD blowdown will be approximately 0.108 MGD. The flowrate of the dilution water will be approximately 0.432 MGD Parameter Estimated FGD Blowdown Concentration (ppm) Antimony 0.080 Arsenic 0.058 Barium 2.185 Beryllium 0.002 Boron 0.283 Cadmium 0.007 Chloride 20,000 Chromium 0.073 Cobalt 0.075 Copper 0.059 Fluoride 12.0 Lead __ 0.092 Manganese 11.654 Mercury 0.027 Molybdenum 0.015 Nickel 0.433 Selenium 3.654 Silver 0.007 Sulfate 7,098 Thallium 0.055 Vanadium 0.052 Zinc 3.149 French Broad > Make-Up River Water Intake Stormwater Old Ash Pond VFlue D Settling X ) Desulfurization V > Clarifier . > n Eq ualiaA Zone B Y — IUnits 1 &2 S Lake Julian Condensers A Outfall 002 Lake NIntake Julian Structure _� Circulating Water F—)11' Ash Sump _ to Heat Exchanger A I Y l___U Diesel T Fire > Fire Preheater Ash Evaporation Pump Protection Cleaning Sluice in Boilers System Water Water TL Chemical Metal Service Water Vendor supplied Q R Cleaning Waste V A — water treatment G Constructed Wetland I r y Combustion M > E I Z Turbine Site New > Low Volume E > Ash Pond Secondary French Broad Waste Sources > Settling River A A Basin A Outfall 001 Storm Water J H K 1 Dam Seepage Coal Pile Public Potable and C Public Runoff Attachment 2-form 2C-Item IIA Flows,Sources of Water ) Sanitary > Sewage Pollution.and Treatment Technolooies Supply System System Progress Energy Carolinas,Inc. Asheville Steam Electric Plant Buncombe County Page 1 of 2 • Progress Energy Carolinas, Inc. Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NCOO00396 Attachment 2 Form 2C - Item Il-A Flow, Sources of Pollution, and Treatment Technologies Stream Name Average Flow Comments A Ash Pond Discharge 3.10 MGD Outfall 001 B Intake to Once-through Cooling&Circulating 250.1 MGD Water to Heat Exchangers C Plant Potable and Sanitary Uses 0.002 MGD To POTW D Makeup to Lake from River 7500 gpm Maximum Flow E Low Volume Wastes • Ash Hopper Seals 0.05 MGD • Sandbed Filter Backwash 2600 Gal/event Rare Usage • Water Softener Regeneration and Washing 3100 Gal/event Rare Usage • Boiler Blowdown 0.006 MGD Startup-Estimated F Circulating Water from Heat Exchangers 19.3 MGD Estimated G Ash Sluice Water 2.0 MGD Estimated H Dam Seepage 0.09 MGD Calculated I City Water Supply to Boiler Makeup 0 MGD Rare Usage J Coal Pile Runoff 0.01 MGD Based on Average Annual Rainfall of 47"and 50%Runoff K Storm Water 0.052 MGD Estimated L Chemical Metal Cleaning Wastes 0-90,000 Gallons Normal Practice is Evaporation (0 gallons anticipated) M Water From Combustion Turbine Facility 0-0.02 MGD Intermittent Operation N From Lake to Intake 250.15 MGD Estimated O Intake to Service Water 0.05 MGD Estimated Q Fire Protection Water 0.010 MGD Estimated R Air Preheater Cleaning 10,000 gallons/event Estimated S Discharge to Lake Julian 248.4 MGD Outfall 002-Estimated T Emergency Fire Protection Water 0 Used for fire fighting U Diesel Fire Pump to Lake Julian 0.128 MG/week Estimate-pump testing ✓ Flue Gas Desulfurization Blowdown 0.108 MGD Estimated X Intake to FGD system 0.864 MGD Estimated Y Chloride Dilution Water 0.432 MGD Estimated Z Constructed Wetland Discharge 0.54 MGD Estimated 2 Carolina Power & Light Company Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NC0000396 Attachment 3 Form 2C - Item Il-B Flow, Sources of Pollution, and Treatment Technologies The Asheville Steam Electric Plant is located in Arden, North Carolina south of Asheville, North Carolina. The Asheville Steam Electric Plant is a coal-fired, steam cycle electric generating plant with two generating units. Two Internal Combustion (IC) Turbines are also located on the plant site. The plant has a 320-acre cooling lake (Lake Julian) on the east side of the French Broad River in Buncombe County, North Carolina. Chemical constituents contained in the discharges from this plant will, in part be representative of the naturally occurring chemical quality of the intake water and will also have chemical constituents of such quality and quantity associated with similar discharges for fossil generating facilities of this size, type and in this geographical location. Either all or part of the elements listed on the Periodic Table, either singularly or in any combination, may from time to time be contained in the discharge. Outfall 001 - Discharge from Ash Pond to French Broad River The Plant's ash pond, which is located east of the French Broad River and south of the plant, discharges into the French Broad River. The ash pond receives ash sluice water, low volume wastes, coal pile runoff, air preheater cleaning water, fire protection system drainage, chemical metal cleaning wastes (potentially), storm water and other waters from the Combustion Turbine Facility constructed on the Plant's site. The proposed wheel wash and weigh stations will also discharge to the Ash Pond. The Pond provides treatment by sedimentation and neutralization to the above-referenced individual waste streams. Water leaves the ash pond via a standpipe with skimmer and flows by pipe and lined ditch to a secondary basin, where it is discharged by overflow to a ditch that coveys it to the French Broad River. Detailed descriptions of the individual waste streams are below. Ash Sluice Water Fly ash and bottom ash from both units are hydraulically conveyed by an ash sluice pipeline to the ash pond. An Amine Enhanced Fuel Lean Gas Reburn (AEFLGR) process will be installed on Unit 1 in the spring of 2000. This process utilizes urea to reduce NOx emissions and will be 1 Carolina Power& Light Company Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NC0000396 used in high ozone months (approximately May through September). A byproduct of this process is ammonia which will be carried to the ash pond via ash sluice water. Coal Pile Runoff Storm water runoff from the coal pile is collected in drainage ditches that surround the coal pile. The drainage ditches are routed to the ash pond for treatment. During maintenance activities, sludges removed from catch basins, sumps, etc. may be transported to the old and/or the new ash pond for disposal. Storm Water Storm water runoff from the plant area, parking lots, combustion turbine area, oil storage and handling facility and the plant's 115 KV substation is routed to the ash pond for treatment. During maintenance activities, sludges removed from catch basins, sumps, etc. may be transported to the old and/or the new ash pond for disposal. Low Volume Wastes Boiler water make up is withdrawn from Lake Julian and purified utilizing vendor supplied equipment. A second option is to perform these activities using plant equipment to filter, soften, and evaporate make up water with the filter backwash, softener regeneration, and softener rinses discharged to the ash pond. The water softeners are regenerated using salt. Boiler water is treated with ammonia, hydrazine, and sodium hydroxide. Boiler and evaporator blowdown and drainage is sent to the ash pond and may contain small quantities of the chemicals. Some molybdate waste from the closed cooling water system is created through valve leakage and maintenance activities and is discharged to the ash pond. A furnace ash hopper seal is maintained by using plant service water. A standard operation water level is maintained in a seal trough for the ash hopper seal. Overflow from this trough is discharged to the ash pond. A sodium hydroxide solution is fed into this flow stream as necessary for ash pond pH adjustment. Coal dust suppression is achieved by spraying a proprietary chemical on coal at different stages of coal use. Small amounts of excess dust suppression chemical have the potential to be discharged to the ash pond via plant drains or coal pile runoff. Small amounts of urea waste from bulk urea unloading operations are discharged to the ash pond. All plant area floor drains are routed to the ash pond and include equipment drainage and wash down along with rainfall runoff. During maintenance activities, sludges removed from catch basins, sumps, etc. may be transported to the old and/or the new ash pond for disposal. 2 Carolina Power & Light Company Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NC0000396 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 pond. Detectable levels of these chemicals would not be expected to occur in ash pond discharges. Flue Gas Desulfurization Blowdown (Low Volume Waste) The Flue Gas Desulfurization (FGD) system directs flue gas into an absorber where a limestone (calcium carbonate) slurry is sprayed. Sulfur dioxide in the flue gas reacts with the limestone to produce calcium sulfate (gypsum). This system reclaims any unreacted limestone slurry to be reused in the absorber. A small blowdown stream is used to maintain the chloride concentration in the reaction tank. The blowdown stream is passed through a clarifier to remove solids and the chloride concentration in the waste stream is diluted using water from Lake Julian. A constructed wetland is used to remove metals, mercury and selenium specifically, and the treated wastewater is discharged into the secondary settling pond. Air Preheater Cleaning (Low Volume Waste) After the Amine Enhanced Fuel Lean Gas Reburn (AEFLGR) system is operational, the air preheater will be water washed on a more frequent basis. It is expected to require cleaning once per year or more frequently as needed. The wastewater from this activity will be discharged to the ash pond. Chemical Metal Cleaning Wastes The boilers are chemically cleaned every five-to-eight years using a weak citric acid solution. This cleaning solution and its rinses are stored on site for disposal by evaporation in an operating unit's furnace. Typical cleanings would result in a waste of approximately 80,000 gallons. Should evaporation not be used, the waste can be routed to a treatment basin for neutralization and precipitation prior to being conveyed to the old ash pond with permission of the DWQ, to the newer ash pond, or other means of disposal. Cleaning of other heat exchanger surfaces may produce 5,000-10,000 gallons every three-to-five years. Other Wastes Operation of the combustion turbine (CT) generation facility may produce turbine blade wash water, inlet filter cooling water, various condensate waters, and water from equipment and tank drains. These wastewaters will be collected in the storm water collection system of the CT site 3 Carolina Power& Light Company Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NC0000396 and routed to the ash pond. During maintenance activities, sludges removed from catch basins, sumps, etc. may be transported to the old and/or the new ash pond for disposal. - Plant Potable and Sanitary System - The supply of water for plant potable and sanitary use is obtained from the Asheville/Buncombe Water Authority system and waste from this system is discharged to the Metropolitan Sewage District System. - 230 KV Substation Storm Water- Storm water runoff from the substation located adjacent to the plant is conveyed to the old ash pond. Outfall 002 - Discharge to Lake Julian Once-Through Cooling Water This flow provides condenser cooling water for the generating units 1 and 2. Maximum condenser flows for units 1 and 2 are 124 MGD and 162 MGD, respectively. Once-through cooling water is used to supply non-contact cooling water for the component closed cooling water system. The component closed cooling water system flows combine with unit 1 and 2 condenser flows prior to discharge to Lake Julian. Maximum component closed cooling water system flows for unit 1 and 2 are 9.1 MGD and 10.2 MGD, respectively. Discharge flow to Lake Julian is calculated at the intake to units1 and 2 condensers and to the circulating water to the heat exchanger. The discharge of water from the heat exchangers is routed to an ash sump. The majority of this water is further routed to the discharge of units 1 and 2 condensers. Less than one per cent of the flow to the ash sump is used to supply ash sluice water, preheater cleaning water, and fire protection water. Control of biological fouling on heat-exchanger surfaces is accomplished by addition of sodium hypochlorite as required, which is usually less that 2 hours per day per unit, with a net total residual chlorine of less than 0.2 ppm discharged during that period. Cooling is accomplished by evaporation from the surface of Lake Julian and mixing and convection with lake waters. Make up for Lake Julian is from the French Broad River, natural runoff and creek flows. Water is pumped from the French Broad River during dry periods to supplement the flow. Although 4 Carolina Power& Light Company Asheville Steam Electric Plant National Pollutant Discharge Elimination System Permit Number NC0000396 discharge from Lake Julian to the river is extremely rare, any occurrence would be during periods of heavy rainfall. 5