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HomeMy WebLinkAboutNC0072575_Staff Comments_19900508DIVISION OF ENVIRONMENTAL MANAGEMENT May 8, 1990 Memorandum To: Rosanne Barons From: Carla Sanderson L_(T Through: Trevor Clements V_ Subject: Response to Golden Poultry NPDES Permit No. NC0072575 Request for Modification I am responding to the letter sent March 27, 1990 from Mr. John E. Starkey concerning a modification of the NPDES permit for Golden Poultry. Technical Support performed an analysis for the Golden Poultry discharge in February, 1988. Several scenarios of limitations were developed for the facility to choose from which would not further degrade the water quality in the Deep River. The facility cho(►se a set of limits necessary for their proposed plant perfor- mance (i.e. 53.5 #/d BOD5 and 1.27 #/d NH3N monthly averages). Since Golden Poultry has been in operation, they have discovered that another set of limita- tions may be more applicable for their facility's performance. Therefore, the previous analysis has been re-evaluated for the requested set of limitations to check for protection of the water quality in the Deep River. Below, I have listed the set of limitations for the requested modification of the Golden Poultry Permit: summer Winter Mon Ave Dal Max Mon Ave Dal Max BODS (#/d) 40 60 80 120 NH3N (#/d) 4.2 6.3 8.4 12.6 According to the permit sheets attached with the letter from Mr. Starkey, the limits were not listed as recommended from Technical Support in February, 1988. The Daily Maximum limitations were listed as 2 times the monthly average in the attached permit for both the summer and winter months. Technical Support's recommendation for daily maximum limits were 1.5 times the monthly average. All other limitations in the NPDES permit should remain the same. Additional limits may be adjusted when this permit is renewed in April, 1991. If you have any questions concerning this matter, please let me know. cc: Dale Overcash Tim Donnelly WLA File R ta, Ca 3030 2 etr�.E ors Ga 30_ March 27, 1990 �990 Mr. Donald Safrit Supervisor, Permits and Engineering ..i( NC Department of Environmental Management aFrl�E 3800 Barrett Drive Raleigh, North Carolina 27687 Re: Golden Poultry Company Sanford, NC NPDES #0072575 Per our recent conversation, attached you will find an NPDES permit application and a $25.00 minor modification processing fee for the referenced facility. Our purpose in filing for the modification is to allow adjustment of our BOD and NH3 limits. At the time of initial permit issuance, NCDEM developed various BOD limits and ammonia limits necessary to protect instream water quality. A table (attached) was prepared showing various BOD/NH3 limitation combinations. Golden was allowed to choose the specific combination and chose summer time limits of 53.5 lb/day BOD5 and 1.27 lb/day NH3-N. Winter limits were double those above. We selected these limits based on literature values for other overland flow treatment systems. To date, our BOD performance has been significantly better than anticipated, however, our ammonia performance has not been quite as good as anticipated. Consequently, we are requesting the permit be modified to list the following limits. Summer Levels D NH (Olb/day) (lb/day) 40 4.2 Winter Levels VN `.'i: �fL +;J�_ BO(lb/day) (N/day) J`��c`-�t1� ��-r•;�,., •. 80 8.4 Should you have any questions or comments concerning the above or attached, or wish to meet to discuss this matter, please call. Sincerely, John E. Starkey, Manager Environmental Engineering (404)393-5203 JES:er Attachment cc: Mr. Glenn Berry Mr. Matt Hopkins File 4001cWQ Mr. James Brown Mr. Bruce Morgan Telex: 6827213 Fax. 404-393-5421 Phone: (404) 393-5000 PRELIMINARY RESULTS WITH LIMITS TO PROTECT INSTREAM4 .•LATER QUALITY GOLDEN POULTRY WASTELOOD ALLOCATIONS WITH LOADS FOR NBOD AND CBOD NBOD CBOD (#/D) (#/D) 1.5 200 3.75 180 7.5 140 18.8 120 37.5 80 COMPLIANCE VALUES (SUMMER DISCHARGE) BOD5 BOD5 NH3-N NH3-N (#/D) (MG/L) (#/D) (MG/L) 67 40.2 0.33 0.2 60 36 0.83 0.5 47 28.2 1.7 1.0 40 24 4.2 2.5 27 16.2 8.3 5.0 TABLES SHOWING THE LEVEL B MODEL RESULTS 7Q10 = 17 CFS WASTEFLOW = 0.2 MGD (020% OF DESIGN) a� 70 �✓ -(I�7iw1i�t5 I.f.GviIC41114v10c� , ,-1q-73� } goo�tool� 9�r/afcr/ `L %rcy'1� �o yam. s,airy Z�6 4r-3;. SUPPLEMENTARY INFORMATION GOLDEN POULTRY COMPANY NPDES PERMIT APPLICATION 1. A description of the origin, type, and flow of waste which is proposed to be discharged. Flow shall be determined in accordance with Rule 2H. 0206(1) of this Chapter. Golden Poultry Company owns and operates a chicken processing plant in Lee County. The site for the new plant is located approximately 8 miles north of Sanford, North Carolina off N.C.S.R. 1400. Golden owns approximately 440 acres, two sides of the property are bounded by the Deep River. The plant is capable of processing 182 birds per minute, and employs approximately 400 people. Chicken processing is a water -intensive industry. Regula- tions issued by the United States Department of Agriculture specify minimal water uses in several areas of the processing operation. Even a well managed plant with a good water conservation program will use 11 to 12 pounds of water per pound of chicken produced. The water use schematic included in this permit package delineates where water is used. Wastewaters generated by the processing plant will contain the pollutants BOD5, TSS, oil and grease, organic nitrogen and ammonia nitrogen. The approximate strength of that wastewater following screening will be as follows: BOD 1500 - 2000 mg/1 TSS 700 - 900 mg/1 FOGS- 300 - 500 mg/l Organic Nitrogen 110 - 140 mg/l Ammonia Nitrogen 15 - 30 mg/l *Fats, Oils and Greases Average daily flow from the processing plant will be approximately 0.75 MGD. However, depending upon market demand, up to 1.0 MGD may be discharged by the facility. 2. A summary of waste treatment and disposal options that were considered and why the proposed system and point of discharge were selected; the summary should have sufficient detail to assure that the most environmentally sound alternative was selected from the reasonably cost effective options. A non -discharge system was investigated for this site. However, as is described in detail in the August 1987 engineering report, permeability of soils at the site are not adequate to handle a slow rate infiltration system for a discharge of this size. t -2- The Deep River at the discharge point has been modelled. Effluent limits are based on this previous modeling. 3. A narrative description of the proposed treatment works in- cluding type and arrangement of major components, in sufficient detail to assure that the proposed facility has the capability to comply with the permit limits; for commonly used treatment system or components with well established treatment capabilities, detailed plans and specifications need not be submitted until the application for the authori- zation to construct; however, detailed plans and specifica- tions shall be required with the permit application for any system or component without well established treatment capabilities for the nature of waste or degree of treatment needed to meet the permit limits. The treatment train consists of primary screening dissolved air flotation with chemical addition, overland flow, chlori- nation and discharge: The wastewater treatment schematic is included in this permit package. Storage is provided between dissolved air flotation and overland flow to be utilized as needed. Specifications for each treatment unit is as summarized below. Screening - Two 4' x1 O' shaker screens ( mesh 36x40) are utilized on the offal line; three 4'x10' shaker screens (mesh 20x2O) are utilized on the feather line. Dissolved Air Flotation with Chemical Addition - Screened wastewater flows to a wet well where a ferric salt is introduced for coagulation. Next, the wastewater is pumped into a pressurization tank. Air is injected at the pump. The wastewater is held in the pressurization tank for a period of 1-2 minutes at approximately 40 psig, causing injected air to go into solution. As the wastewater is released into the flotation cell, an anionic polymer is introduced. This causes flocculation of solids, blood and grease in the wastewater. As the air comes out of solution, these pollutants float to the surface. This float fat is skimmed off for recovery by an off -site renderer. Wastewater discharging from the DAF system has as minimum following quality. BOD 500 mg/l TSS 500 mg/l FOG 100 mg/l Organic Nitrogen 100 mg/l Ammonia Nitrogen 20 mg/l -3- Sizing of the dissolved air flotation unit is 30,000 gallons, with 700 ft2 of surface area. Overland Flow System (and storage) - Effluent from the DAF system flows to a wet well. Pumps controlled by level controllers, sprays the wastewater on the appropriate overland flow field. A basin of approximately 1 million gallons is connected to the wet well to handle any surge flows and to provide temporary storage in the event of any mechanical problems. This surge basin overflows to an approximately 4-million gallon off-line storae basin, in the event longer periods of storage are necessary. The overland flow system encompasses 130 acres, sufficient area to treat 1 MGD. An automatic control system will direct flow to the appropriate fields. A more in-depth discussion concerning overland flow is presented in the concept design report included in previous application packages. Chlorination and Monitoring - Effluent from the overland flow system is collected, disinfected, flows through a Parshall flume with a recording device, and then discharged to the Deep River. 4. A general location map, showing orientation of the facility with reference to at least two geographic references (numbered roads, named streams/rivers, etc.). Included elsewhere in this application package. 5. A scale location plan, of the site showing location of the proposed treatment works and the proposed point of discharge. Included elsewhere in this application package.