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NC0006548_Wasteload Allocation_19950316
NPDES DOCUMENT 5CANNIN`: COVER SHEET NPDES Permit: NC0006548 Wayne Farms / Dobson facility Document Type: Permit Issuance Wasteload Allocation Authorization to Construct (AtC) Permit Modification Complete File - Historical Engineering Alternatives (EAA) Plan of Action Instream Assessment (67b) Speculative Limits Environmental Assessment (EA) Permit History Document Date: March 16, 1995 Thin document is printed on reutae paper - ignore any content on the reYerae aide NPDES WASTE LOAD ALLOCATION PERMIT NO.: NC0006548 PERNIITTEE NAME: Continental Grain Company FACILITY NAME: Wayne Farms -Dobson Plant Facility Status: Existing Permit Status: Modification Major Minor Pipe No.: 00 I Design Capacity: 0.60 MGD Domestic (% of Flow): Industrial (% of Flow): 100 % Comments: Request to increase flow from 0.48 MGD to 0.60 MGD. RECEIVING STREAM: Fisher River Class: C Sub -Basin: 03-07-02 Reference USGS Quad: B 16NW (please attach) County: Surry Regional Office: Winston-Salem Regional Office Previous Exp. Date: 6/30/93 Treatment Plant Class: Classification changes within three miles: Requested by: Prepared by: Reviewed by: :tL C L��.(���L , Susan Robson Date: 11/21/94 Date:1 51, Date: 3I I SIC-0 Modeler Date Rec. # MAW I//zi/94- 8o6,/ Drainage Area (mi2 ) I OC1 Avg. Streamflow (cfs): 15 5 3 3 7Q10 (cfs %- Winter 7Q10 (cfs) Toxicity Limits: IWC .3,% Instream Monitoring: Parameters tx) , eV1�l.p) C he r U• c--e DI CO L -(- o i' ., Upstream ✓ Location AiC„.. ap g r;dee Downstream Location MUC5t?, IIOU (� c 30Q2 (cfs) Acute/ Effluent Characteristicsis� Oh 1 , , y . �� BOD5 ( ) -5 Ucl W Nx3-N (mg/1) 0 ( l0 /6) 30 65o /d) D.O. (mg/1) TSS () Log COO F. Col. (/100 ml) 0,0 v 4{ rD pl I (SU) - l Ou ('5t cl) ISO O (i.ki.J ag / g nte7 rilc4e -mow Cti-t3 Comments: 2c2 7 RECEIVE WASHINGTON Facility Name: NPDES No.: Type of Waste: Facility Status: Permit Status: Receiving Stream: Stream Classification: Subbasin: County: Regional Office: Requestor: Date of Request: Topo Quad: Wayne Poultry Farms -Dobson Plant NC0006548 100% Industrial Existing Increasing flow and production Fisher River C 030702 Surry WSRO Susan Robson = 11/21/94 ,.,, B16NW .:i.+�• FACT SHEET FOR WASTELOAD ALLOCATION FEB 21 1— D. E. M. Request # 8061- L. N.C. Dept. of EHNR FEB 2 7 1995 1Niidslon-S'a1nri Stream Characteti t c USGS # n n ` Date: Drainage Area (mi2): 109 Summer 7Q10 (cfs): Winter 7Q10 (cfs): Average Flow (cfs): 142 30Q2 (cfs): 48.7 IWC (%): 3.9 2/2/94 Wasteload Allocation Summary (approach taken, correspondence with region, EPA, etc.) Facility proposing to increase flow from 0.48 MGD to 0.60 MGD and to increase production from 600,000 #/day to 750,000 #/day. I updated flows (HA10 and MAR=1.3) due to facility expanding flow and ran a Level B model. The guideline limits will protect D.O. instream. The allowable NH3N = 20 mg/1 based on new flows. IWC changed to 3.9%. Faciliaty has failed WET test 3 times at P/F 2.5% since 8/93. There are excessive levels of NH3N ( month max = 73.7 mg/1) and Chlorine (month max =1.4 mg/1) in the effluent. I recommend adding a chlorine limit and giving facility a compliance schedule so they can install necessary facilities. Special Schedule Requirements and additional comments from Reviewers: / /7r3 /(-/;U)(//;� `r�6Gyc-ire tea pv,/(461/i/e4 7RC { 0,3 /'',' rY5 . Recommended by: 7/Z1 Y �, . Date: ZAA Reviewed by ?�Instream Assessment: regional Supervisor: Permits & Engineering: RETURN TO TECHNICAL SUPPORT BY: Date: a. l Date:.? Date:-3/O//15 MAR 1 1995 v 0 C-) 2 TOXICS/METALS/CONVENTIONAL PARAMETERS Recommended Limit: Existing Limit: Monitoring Schedule: Existing Limits Chronic P/F Ceriodaphnia Qrtly at 3.9% Chronic P/F Ceriodaphnia Qrtly at 2.5% JAN, APR, JUL, OCT Monthly Avg. Daily Max. Monthly Avg. Daily Max. Flow (MGD): 0.48 BOD5 (lbs/day): 276 552 TSS (lbs/day): 372 744 Fecal Coliform (/100m1): 200 400 pH (SU): 6-9 Oil and Grease (lbs/day): 120 240 Recommended Limits Monthly Avg. Daily Max. Monthly Avg. Daily Max. Flow (MGD): 0.60 BOD5 (lbs/day): 345 690 TSS (lbs/day): 465 930 NH3N (mg/1) 20 WQ 30 WQ 100#/day 150#/day T.R. Chlorine (ug/l) 28 Fecal Coliform (/100m1): 200 400 pH (SU): 6-9 Oil and Grease (lbs/day): 150 300 Limit Changes due to an increase in production, increase in wasteflow and a decrease in stream flow. --F cakcvvrl0 Ism. .wilt-t&. tw -Imi- loco -Pau) I.vac.ea) ►4,5) _X_ Parameter(s) are water quality limited. For some parameters, the available load capacity of the immediate receiving water will be consumed. This may affect future water quality based effluent limitations for additional dischargers within this portion of the watershed. OR No parameters are water quality limited, but this discharge may affect future allocations. 3 INSTREAM MONITORING REQUIREMENTS Upstream Location: NCSR 2258 at Bridge Downstream Location: NCSR 1100 at Bridge Parameters: , Temp, Conductivity)'d,`Fe C e ' Co akov iVt. Special instream monitoring locations or monitoring frequencies: Region please comment about instream monitoring recommendation MISCELLANEOUS INFORMATION & SPECIAL CONDITIONS Adequacy of Existing Treatment Has the facility demonstrated the ability to meet the proposed new limits with existing treatment facilities? Yes No _— If no, which parameters cannot be met? / l - A., ` % : Ic (4 la, - Would a "phasing in" of the new limits be appropriate? Yes V No If yes, please provide a schedule (and basis for that schedule) with the regional office recommendations: ictC'.'�' I�us Lree.1 et, / 2CGiil1Y1'EnSeer /U' p r'Jl /;:_n f •`✓)1r s <'n *(f pc's Ufi rmYa.(ts / /ny n # A `` l,O/1a Sin c' , r ' ,.� /1 3 lG /%, ('..CN r' r<nt f r� s If no, why not? Special Instructions or Conditions Wasteload sent to EPA? (Major) I\\ (Y or N) (If yes, then attach updated evaluation of facility, including toxics analysis, modeling analysis if modeled at renewal, and description of how it fits into basinwide plan) Additional Information attached? (Y or N) If yes, explain with attachments. Port) 11(1 Facility Name pant Permit # NC OOCth5 5 . Pipe # UU f d CIII<UfN11 1 UXIU.Ci a 4'A�5/rAlL ?ERMii' LIMIT (Q1CTRLY) The effluent discharge shall at no time exhibit chronic toxicity using test procedures outlined in: 1.) The North Carolina Ceriodaphnia chronic effluent bioassay procedure (North Carolina Chronic Bioassay Procedure - Revised *September 1989) or subsequent versions. The effluent concentration at which there may be no observable inhibition of reproduction or significant mortality is ;,` % (defined as treatment two in the North Carolina procedure document). The permit holder shall perform quarterly monitoring using this procedure to establish compliance with the permit condition. The first test will be performed after thirty days from the effective date of this permit during the months of 3 14-02 Tut- 1 ocr . Effluent sampling for this testing shall be performed at the NPDES permitted final effluent discharge below all treatment processes. All toxicity testing results required as part of this permit condition will be entered on the Effluent Discharge Monitoring Form (MR-1) for the month in which it was performed, using the parameter code TGP3B. Additionally, DEM Form AT-1 (original) is to be sent to the following address: Attention: Environmental Sciences Branch North Carolina Division of Environmental Management 4401 Reedy Creek Road Raleigh, N.C. 27607 Test data shall be complete and accurate and include all supporting chemical/physical measurements performed in association with the toxicity tests, as well as all dose/response data. Total residual chlorine of the effluent toxicity sample must be measured and reported if chlorine is employed for disinfection of the waste stream. Should any single quarterly monitoring indicate a failure to meet specified limits, then monthly monitoring will begin immediately until such time that a single test is passed. Upon passing, this monthly test requirement will revert to quarterly in the months specified above. Should any test data from this monitoring requirement or tests performed by the North Carolina Division of Environmental Management ipdicate potential impacts to the receiving stream, this permit may be re -opened and modified to include alternate monitoring requirements or limits. NOTE: Failure to achieve test conditions as specified in the cited document, such as minimum control organism survival and appropriate environmental controls, shall constitute an invalid test and will require immediate retesting(within 30 days of initial monitoring event). Failure to submit suitable test results will constitute noncompliance with monitoring requirements. .._..Mils 7Q10 2 3 cfs Permitted Flow _0, (o _ MGD IWC 3 , y % Basin & Sub -basin 03470 2 . yfa v Receiving Stream risky 41 vei- County cirri QCL PIF Version 9191 WAYNE POULTRY NC0006548 FOR APPROPRIATE DISCHARGERS, LISST COMPLETE GUIDELINE LIMITATIONS BELOW at, .;-1 nit th j '' Effluent Characteristics Monthly Average I Daily Maximum Comments BOD5 276.0/345.0 -7 60 ..� fiQ 552.0/690.0 original production limit/increased limit TSS 372.0/465.0 ' 744.0/930.0 original production limit/increased limit Oil & Grease 120.0/150.0 240.0/300.0 original production limit/increased limit Fecal Coliform 200 400 NH3 (f / ivogri., 30 .D IJ /iv tt/d . C Type of Product Produced Lbs/Day Produced Effluent Guideline Reference Processed chicken 600,000 Proposed 40 CFR Part 432 subpart 112 750,000 proposed increase Proposed 40 CFR Part 432 subpart 112 Pod I, .iwp( /14.44lL; L,#nfl . g4),. o q4, 3VS 0( Table 23. Recommended Effluent Limitations for July 1, 1977 Industry Subcategory Effluent Parameters BOD5, kg/kkg LWK* Chickens Turkeys Fowl Ducks Further Processing Only • SS, kg/kkg LWK Grease, kg/kkg LWK Fecal Coliform, Max. Count/100 ml 0.39 0.61 0.77 0.30 kg/kkg FP 0.57 0.72 0.90 0.35 kg/kkg FP 0.20) 0.14 0.15 0.26 0.10 kg/kkg FP 400 400 400 400 400 *kg/k'.g LWK is equivalent to lb/1000 lb LWK NC D ‘95 ¢i( W 63- 07- Cur/ /1/IiYl I (UJ70 lettaiel .04 Z1/4gib tea ( 1 nt6,14 sc ve v ifrn 41 ffD KL N s 1' W H-Y N E ► r l�i2r� BAN, 305h , 3o3d , ,.Sf : V „/ fp kicrEwe ilk di Iid ?T d vv CalICI,DG�J llg � i?J t), <` G t if°t_( r hi 0 Q Z (we = 2,5 `?a 1 1091.14,z 7`S/,7c r 23,05 A 34-c 48.74( it 3.37Z- ' 3,7)7. r//16t„G.LQ{k �xrsh►� NO3Nis) -- 3/,4 �jJ9 N 3hlrw� = !)1.S5 fjq -1); 1ur = 40: I1,.l,1a� n�o� II u v N443 N - /70'b/a/ rah,) D,3��sp = 73.'%i'� -� o 3' - `J �vs -600,5 = 345 °Af a.6.34 _ 0 • c, Pr( = /04. 7 4 /,0 - O' OD = C �,o.� hit - 26(� �� srh . j c BOO', � 3 s U ;n p �- N 2°,26 x 4,5 97, (e 2 (ct f �� , �- tea, e Rao e ilskit )) fr wayne poultry fisher river existing flows Residual Chlorine 7010 (CFS) DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (UG/L) UPS BACKGROUND LEVEL (UG/L) IWC (%) Allowable Concentration (ug/i) Fecal Limit Ratio of 39.0 :1 Ammonia as NH3 (summer) 29 7010 (CFS) 0.48 DESIGN FLOW (MGD) 0.744 DESIGN FLOW (CFS) 17.0 STREAM STD (MG/L) 0 UPS BACKGROUND LEVEL (MG/L) 2.50 IWC (%) 679.63 Allowable Concentration (mg/i) Ammonia as NH3 (winter) 7010 (CFS) 200/100m1 DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (MG/L) UPS BACKGROUND LEVEL (MG/L) IWC (%) Allowable Concentration (mg/i) 29 0.48 0.744 1.0 0.22 2.50 31.40 53 0.48 0.744 1.8 0.22 1.38 114.35 SYYI -gown + Ienvve.c-P ir) OW 4v 046 r17(,) wayne poultry fisher river Residual Chlorine 7010 (CFS) DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (UG/L) UPS BACKGROUND LEVEL (UG/L) IWC (%) Allowable Concentration (ug/I) Fecal Limit Ratio of 24.8 :1 Ammonia as NH3 (summer) 23.08 7010 (CFS) 0.6 DESIGN FLOW (MGD) 0.93 DESIGN FLOW (CFS) 17.0 STREAM STD (MG/L) 0 UPS BACKGROUND LEVEL (MG/L) 3.87 IWC (%) 438.89 Allowable Concentration (mg/i) Ammonia as NH3 (winter) 7010 (CFS) 200/100mI DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (MG/L) UPS BACKGROUND LEVEL (MG/L) iWC (%) Allowable Concentration (mg/I) 23.08 0.6 0.93 1.0 0.22 3.87 20.36 34 0.6 0.93 1.8 0.22 2.66 59.56 OLE EFFLUENT TOXICITY TESTING 0(SELF-MONITORING SUMMARY] Mon, Jan 16, 1995 II.ITY REQUIREMENT YFAR JAN LACE WWTP PERM CHR LIM:27% 91 PASS '0020702/001 Begin:5/1/93 Frequency: Q P/F A MAR JUN SEP DEC NonComp:SINGLE 92 PASS wily:DUP1.IN Region: WIRO Suhhasin: CPF22 93 FAIL 1.0 Special 94 --- 10:4.20 IWC(%):20.53 Order: 95 FEB MAR PASS APR MAY 111N JUL AUG SEP Of' LATE LATE PASS PASS — — FA! PASS — — PASS — — PA: FAIL PASS PASS — — PASS - -- •-- PASS --- --- PASS STONBURG WWI? PERM CHR LIM:90% 91 PASS — PASS — — FAIL PASS PASS — '0020362/001 Begin:5/1/94 Frequency: Q P/F A MAR JUN SEP DEC NonComp:SINGLE 92 PASS — PASS — PASS -- --- FAIL PA: :inty:GREENE Region: WARO Subbasin: NEU07 93 — — PASS — NRLFAIL FAIL PASS PASS -- 0.138 Special 94 — PASS — LATE PASS -- FAIL LA1 10: 0.01 IWC(%):95.5 Order 95 LD TRANSFORMER CO, INC. PERM CHR LIM:90% 91 N1 — — FAIL PASS — FAIL PASS — FAI '0045608/001 Begin:10/1/93 Frequency: Q P/F A JAN APR JUL OCT NonComp:SINGLE 92 FAIL FAIL FAIL FAIL bt FAIL.71.0 FAIL PASS PASS FAI only:WAKE Region: RRO Suhhasin: NE1102 03 FAIL PASS — FAIL PASS >100 PASS PASS -- PA! VAR Special 04 PASS ••• PASS --• -• PASS --- PA: In. OA00 IWC(%)'I 00.13) Order: 95 'KEN CO. WWTP PERM CIIR LIM:76% 01 -- --- -- --- -• -.. --- --- --' '0020834/001 Begin:12/1/91 Frequency: Q P/F A MAR JUN SEP DEC NonComp: 92 N1 Ng PA PASS PASS' — — FAIL PA: unty:WARREN Region:RRO Subbuln:TAR04 93 — — PASS — PASS — — PASS — '_2_0 Special 94 — — PASS -- LATE PASS LATE PA: •10:1.0 IWC(%):75.6 Order 95 :I IINGTON WWTP PERM CIIR LIM:90%;IF DISCH TO TAR R. do PF 2.12 OR 2 Y 91 NONE' 14.55' FAIL FAIL PASS LATE PASS FAIL FAIL FA: '0020648/001 Begin:12/1/93 Frequency: Q P/F A FEB MAY AUG NOV NonComp:SINGLE 92 FAIL PASS — FAIL PASS — PASS — nnty:BF.AUFORT Region: WARO Suhbasin: TAR07 93 — PASS — FAIL PASS — FAIL PASS. 2.12 Special 94 — FAIL PASS — FAIL LATE PASS PASS — •10:0.0 IWC(%):100.0 Order 95 NE POULTRY PERM CIIR LIM:2.5% 91 PASS — — PASS '00065481001 Begin:6/1/94 Frequency: Q P/F A JAN APR JUL OCT NonComp:SINGLE 92 PASS — — PASS only: SORRY Region: WSRO Subbasin: YAD02 93 PASS — — NH/PASS :0.48 Special 94 PASS — — PASS "10:29.00 IWC(%):2.50 Order. 95 LATE PASS PASS — Pts 5 — — PAS LATE.FAIL PASS✓; Faivpas., PASS --- PASS 'NFSVILLE WWTP PERM CIIR LIM:9% 91 -- 1)025321/001 Bcgin:5/1/94 Fnxiucncy: Q P/F A FEB MAY AUG NOV NonComp:SINGLE 92 -- onty:HAYWOGD Region: ARO Subbasin: FRB05 93 — 6.00 Special 94 — )10: 95.0 IWC(%):8.91 Order. 95 PASS — — LATE PASS — PASS — PASS PASS — FAIL PASS PASS — — PASS — — PASS PASS — — PASS — — PASS )GEPIELD ACRES MHP PERM CHR LIM:90% (GRAD) 91 — — — — — — — — — :A062634/001 Begin:l1/1/91 Frequency: Q P/F A JAN APR JUL OCT NonComp: 92 NI — — PASS — — FAIL PASS — PA: .unty:BUNCOMBE Region: ARO Subbasin:1Z2➢02 93 FAIL FAIL PASS FAIL FAIL PASS FAIL PASS — PA: ':0.025 Special 94 FAIL FAIL PASS FAIL FAIL fit PASS -- — FAt )10: 0.0 IWC(%): 100.0 Omer 05 DON WWTP PERM AC LIM:2411R PA, 90% (FTIID) IF EXI'AN TO 1.2 MC 91 — — --- H --- — — — — 00025721/00l Begin:l/1/93 Frequency: Q P/F G JAN APR JUL OCT NonComp:SINGLE 92 — — — --- — — — 'unty:HALIFAX Region: RRO Subbasin: ROAM 93 H — — H — — H — — H ':0.6 Special 94 H — — H — — H — — H ;10:1500 IWC(%):0.19 Order. 95 IT JEFFERSON WWTP PERM CHR LIM:45% 91 FAIL PASS '0020451/001 Dcgin:7/1/89 Frequency: Q P/F G JAN APR JUL OCT NonComp: 92 PASS — nity:ASIIG Region: WSRO Subbasin: NIIWO2 03 PASS ':0.369 Special 94 PASS )10:0.70 IWC(%):44.92 Orden 95 — PASS — — PASS — — PA — PASS — PASS — -- FA — PASS — PASS — PA — LATE,PASS — PASS — — PA consecutive failures = significant noncompliance Y Pre 1991 Data Available END: M = Permit Requirement LET = Administrative Letter • Target Frequency = Monitoring frequency: Q. Quarterly; M- Monthly; BM• Bimonthly; SA- Semiannually; A- Annually; OWD- Only when discharging; D- Discontinued monitoring require :n = First month required 7QI0 = Receiving stream low flow criterion (cis) A = quarterly monitoring increases to monthly upon single failure Months that testing must occur • ex. JAN.APR.JULOCT NonComp = Current Compliance Rcquin Permitted flow (MGD) IWC%= Instream waste concentration P/F = Pass/Fail chronic test AC = Acute CIIR = Chronic • Notation: f - Fathead Minnow: • - Ceriodanhnia so.; my - Mvsid shrimp: ChV - Chronic value: P - Mortality of stated percentage at highest concentration: at - Performed by DEM Tox Eval Group: bt - Bad test ming Notation: — = Data not required; NR - Not reported; ( ) - Beginning of Quarter Facility Activity Status: I - Inactive, N - Newly Issued(To construct); 11- Active but not discharging; f-More data available for month in question SIG = ORC si 52 USGS weighted low flow estimate procedure Facilitylti rune Poultry Region DA LFPR s7010_LFPR DA new MAR QA eq STEP 1 NPDES # NC0006548 J Stream '• Fisher River j _._ HA10_.._ sq mile cfs .__.109 ._IMMI_.._.._ 1.3 141.70 sq mile cfs/sq mile cfs calculate drainage area ratio NOTE: procedure applies for regions HA3, HA5, HA9, and HA10, else see flow SOP RATIO = new drainage area drainage area at gage IF 0.25 < RATIO < 4, CONTINUE to STEP 2, ELSE too far from gage #DIV/0! STEP 2 determine weight of gage (weight_LFPR) A. RATIO < 1 weat #DIV/O! #DIV/0! talk 1 1 0.25 weight = #DIV/0! B. RATIO > 1 weight ratio 0 1 #DIV/0! i #DIV/O! 1 4 STEP 3 calculate 7010 EQ using regional equation HA3 HA5 HA9 HA10 STEP 4 28.04 2.36 2.36 23.08 cfs cfs cfs cfs 7Q10 EQ= calculate 7010 yield using weighted equation 23.08 7Q10yield = [weight_LFPR * 71010 LFPR] + [weight EQ * 7010_EQJ cfs DA LFPR DA_new yield = #DIV/0! + #DIV/01 = #DIV/0! cfs/sq mile STEP 5 calculate s7010 7010 = 7Q10yield * DA new summer 7010 = #DIV/0! cfs USGS weighted low flow estimate procedure FacilityjWayne Poultry Region DA_LFPR w7Q10 LFPR DA new MAR QAeq STEP 1 NPDES # 1 _.,_ HA10_,._ 0 sq mile ._.._.._..___.._.._.. cfs 109 1.3 141.70 sq mile cfs/sq mile cfs calculate drainage area ratio NC0006548 Stream) Fisher River J NOTE: procedure applies for regions HA3, HA5, HA9, and HA10, else see flow SOP RATIO = new drainage area drainage area at gage IF 0.25 < RATIO < 4, CONTINUE to STEP 2, ELSE too far from gage #DIV/0! STEP 2 determine weight of gage (weight_LFPR) A. RATIO < 1 weight talk/ 0 1 #DIWOI #DIV/Ol 1 0.25 weight = #DIV/0! B. RATIO > 1 weight 0 1 #DIV/0! #DIV/01 1 4 STEP 3 calculate 7Q10 EQ using regional equation HA3 HA5 • HA9 HA10 STEP 4 STEP 5 53.80 10.99 10.99 33.98 cfs cfs cfs cfs 7Q10 EQ= calculate 7Q10 yield using weighted equation 33.98 cfs/sq mile 7Q10yield = [weight_LFPR * 7010 LFPR] + [weight_EQ * 7Q10 EQ] DA LFPR DA new yield = #DIV/01 + #DIV/0! calculate w7010 7010 = 7Q10yield * DA new winter 7010 = #DIV/01 cfs #DIV/0I #DIV/01._.J cfs/mile USGS weighted low flow estimate procedure Facilityl fa ne Poultry NPDES # Region DA LFPR 30Q2_LFPR DA new MAR QA eq STEP 1 s NCOO00548 .j Stream': Fisher River j _.» H_A1_0_.._ 00 NOTE: procedure applies for regions HA3, HA5, 0 sq mile HA9, and HA10, else see flow SOP ....._.._.._...... cfs ____ 1.3 141.70 sq mile cfs/sq mile cfs calculate drainage area ratio RATIO = new drainage area = ! #DIV/0! drainage area at gage _..�._.���.. IF 0.25 < RATIO < 4, CONTINUE to STEP 2, ELSE too far from gage #DIV/0! STEP 2 determine weight of gage (weight_LFPR) A. RATIO < 1 weight 0 #iwoi 1 ratio 1 0.25 weight = B. RATIO > 1 weight ratia _ 0 _ 1 #DIV/0! 1 4 #DIV/01 STEP 3 calculate 3002_EQ using regional equation HA3 HA5 HA9 HA10 60.74 15.51 15.51 48.74 cfs cfs cfs cfs 30Q2 EQ = STEP 4 calculate 3002 yield using weighted equation 48.74 cfs/sq mile 3002yield = [weight_LFPR * 3002_LFPR] + [weight_EQ * 3002_EQ] DA LFPR DA_new yield = #DIV/0! + #DIV/01 = #DIV/0! cfs/sq mile STEP 5 calculate 3002 3002 = 30Q2yield * DA new 3002 = #DIV/0! cfs NC00�28tc w 61vu"rivr Adlows lita) IV wayne poultry fisher river existing flows Residual Chlorine 7Q10 (CFS) DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (UG/L) UPS BACKGROUND LEVEL (UG/L) IWC (%) Allowable Concentration (ug/l) Fecal Umit Ratio of 31.2 :1 Ammonia as NH3 (summer) 29 7010 (CFS) 0.6 DESIGN FLOW (MGD) 0.93 DESIGN FLOW (CFS) 17.0 STREAM STD (MG/L) 0 UPS BACKGROUND LEVEL (MG/L) 3.11 IWC (%) 547.11 Allowable Concentration (mg/1) Ammonia as NH3 (winter) 7Q10 (CFS) 200/100m1 DESIGN FLOW (MGD) DESIGN FLOW (CFS) STREAM STD (MG/L) UPS BACKGROUND LEVEL (MG/L) IWC (%) Allowable Concentration (mg/I) 29 0.6 0.93 1.0 0.22 3.11 25.32 53 0.6 0.93 1.8 0.22 1.72 91.84 SUMMER UPDATED FLOWS ALLOWABLE NH3N PRODUCT & QW CBOD:BOD5=6 MODEL RESULTS Dri schar•ger• : WAYNE POULTRY Receiving Stream : FISHER RIVER The End 0.0. Is 6.83 mg/1. The End CBOD is 12.19 mg/1. The End NBOO 1s 2.77 mg/1. WLA WLA WLA 00 Min CBOD NBOO DO Waste Flow (mg/1) Milep©int Reach # (mg/1) (mg/1) (mg/1) (mgd) Segment 1 6.64 3.06 1 Reach 1 413.40 1 WI g/(oj-e N 91.62 0.00 0.60000 4 '6 *** MODEL SUMMARY DATA *** Discharger : WAYNE POULTRY Receiving Stream : FISHER RIVER Slimmer 7010 : 23.0 Design Temperature: 25.0 Subbasin : 030702 Stream Class: C Winter 7010 : 34.0 'LENGTH' SLOPE' VELOCITY 1 DEPTH I Kd 1 Kd 1 Ka 1 Ka 1 KN 1 KN 1 KNR 1 KNR 1 SOD 1 SOD 1 1 mile 1 ft/mil fps i ft 'design' 020° Idesignl @20° Idesignl @20° 'design' @20° 'design' @20° 1 I 1 1 1 1 1 1 1 1 1 1 1 1 1 1 Segment 1 1 6.801 8.601 0.453 1 1.93 10.31 1 0.25 1 3.83 1 3.431 0.44 1 0.30 1 0.44 1 0,00 1 0,00 1 0.00 I Reach 1 1 1 1 1 1 1 1 1 1 1 1 1 I I Flow 1 CBOD 1 NBOD 1 0.0. I I cfs 1 mg/1 1 mg/1 1 mg/l I Segment 1 Reach 1 Waste 1 0.930 1413.400 1 91.620 1 0.000 Headwaters) 23.000 1 2.000 1 1.000 1 7.440 Tributary 1 0.000 1 2.000 1 1.000 1 7.440 * Runoff 1 0.440 1 2.000 1 1.000 1 7.440 * Runoff flow is in cfs/mile I Seg 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 I Seg # I Reach # I Seg Mi 1 0.00 1 0.34 1 0.68 1 1.02 1 1.36 1 1.70 1 2.04 1 2.38 1 2.72 1 3.06 1 3.40 1 3.74 1 4.08 1 4.42 1 4.76 1 5.10 1 5.44 1 5.78 1 6.12 1 6.46 1 6.80 # I Reach # I Seg M7 I I D.O. 7.15 7.01 6.91 6.82 6.76 6.71 6.68 6.66 6.65 6.64 6.65 6.65 6.66 6.68 6.69 6.71 6.73 6.76 6.78 6.80 6.83 D.O. I I CBOD 17.99 17.63 17.29 16.95 16.62 16.29 15.98 15.67 15.36 15.06 14.77 14.49 14.21 13.94 13.67 13.41 13.16 12.91 12.66 12.42 12.19 CBOD I I SUMMER UPDATED FLOWS ALLOWABLE NH3N PRODUCT & QW CBOD:BOD5=6 NBOD I Flow I 4.52 23.93 4.41 24.08 4.30 24.23 4.20 24.38 4.09 24.53 3.99 24.68 3.89 24.83 3.80 24.98 3.71 25.13 3.62 25.28 3.53 25.43 3.45 25.58 3.36 25.73 3.28 25.87 3.20 26.02 3.13 26.17 3.05 26.32 2.98 26.47 2.91 26.62 2.84 26.77 2.77 26.92 NBOD I Flow I SUMMER UPDATED FLOWS ALLOWABLE NH3N PRODUCTION & QW INCREASE Drischarger MODEL RESULTS : WAYNE POULTRY Receiving Stream : FISHER RIVER The End D.O. is 7.28 mg/1. The End CBOD is 6.83 mg/1. The End NBOD is 2.77 mg/1. WLA WLA WLA D0 Min CBOD NBOD D0 Waste Flow (mg/1) Milepoint Reach # (mg/1) (mg/1) (mg/1) (mgd) Segment 1 7.07 1.70 1 Reach 1 206.80 91.62 0.00 0.60000 7 651AW4A x c�agot=3 .trr- *** MODEL SUMMARY DATA *** Discharger : •WAYNE POULTRY Subbasin 030702 Receiving Stream : FISHER RIVER Stream Class: C Summer 7010 : 23.0 Winter 7Q10 34.0 Design Temperature: 25.0 'LENGTH' SLOPEI VELOCITY I DEPTH' Kd 1 Kd I Ka I Ka 1 KN 1 KN 1 KNR 1 KNR 1 SOD 1 SOD I 1 mile 1 ft/mil fps 1 ft 'design) @20° Idesign) @20° 'design' @20° 'design) @20° 'design' @20° 1 11 1 1 1 1 1 1 1 1 1 1 Segment 1 1 6.801 8.601 0.453 1 1.93 1 0.31 1 0.25 13,83 1 3.431 0.44 1 0.30 1 0.44 1 0.00 10.00 1 0.00 1 Reach 1 1 1 I 1 1 1 1 1 1 1 1 1 I 1 Flow 1 CBOD 1 NBOD I D.Q. I cfs I mg/1 1 mg/1 1 mg/1 I Segment 1 Reach 1 Waste 1 0.930 1206.800 1 91.620 ( 0.000 Headwaters) 23.000 1 2.000 1 1.000 ) 7.440 Tributary 1 0.000 1 2.000 1 1.000 1 7.440 * Runoff 1 0.440 1 2.000 1 1.000 1 7.440 * Runoff flow is in cfs/mile SUMMER UPDATED FLOWS ALLOWABLE NH3N - PRODUCTION & QW INCREASE I Seg # I Reach # I Seg M7 I D.O. I CBOD I NBOD I Flow I 1 1 0.00 7.15 9.96 4.52 23.93 1 1 0.34 7.12 9.77 4.41 24.08 1 1 0.68 7.10 9.58 4.30 24.23 1 1 1.02 7.08 9.40 4.20 24.38 1 1 1.36 7.07 9.22 4.09 24.53 1 1 1.70 7.07 9.05 3.99 24.68 1 1 2.04 7.07 8.88 3.89 24.83 1 1 2.38 7.08 8.71 3.80 24.98 1 1 2.72 7.09 8.54 3.71 25.13 1 1 3.06 7.10 8.38 3.62 25.28 1 1 3.40 7.11 8.23 3.53 25.43 1 1 3.74 7.13 8.08 3.45 25.58 1 1 4.08 7.14 7.93 3.36 25.73 1 1 4.42 7.16 7.78 3.28 25.87 1 1 4.76 7.18 7.63 3.20 26.02 1 1 5.10 7.19 7.49 3.13 26.17 1 1 5.44 7.21 7.36 3.05 26.32 1 1 5.78 7.23 7.22 2.98 26.47 1 1 6.12 7.25 7.09 2.91 26.62 1 1 6.46 7.27 6.96 2.84 26.77 1 1 6.80 7.28 6.83 2.77 26.92 I Seg # I Reach # I Seg Mi I 0.0. I CBOD I NBOD I Flow I SUMMER UPDATED FLOWS PROPOSING PRODUCTION & QW INCREASE QI scharger MODEL RESULTS : WAYNE POULTRY Receiving Stream : FISHER RIVER The End D.O. is 6.60 mg/1. The End CBOD is 6.83 mg/1. The End NBOD is 8.31 mg/1. WLA WLA WLA D0 Min CBOD NBOD D0 Waste Flow (mg/1) Milepoint Reach # (mg/1) (mg/1) (mg/1) (mgd) Segment 1 6.38 3.40 1 Reach 1 206.80 331.65 0.00 0.60000 rif5 . 1 Seg # 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 Seg # Reach 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 Reach Seg M-i 0.00 0.34 0.68 1.02 1.36 1.70 2.04 2.38 2.72 3.06 3.40 3.74 4.08 4.42 4.76 5.10 5.44 5.78 6.12 6.46 6.80 # 1 Seg Mi #I D.O. 7.15 6.95 6.79 6.66 6.57 6.50 6.45 6.41 6.39 6.38 6.38 6.38 6.39 6.41 6.43 6.45 6.48 6.51 6.54 6.57 6.60 1 D.O. 1 CBOD 9.96 9.77 9.58 9.40 9.22 9.05 8.88 8.71 8.54 8.38 8.23 8.08 7.93 7.78 7.63 7.49 7.36 7.22 7.09 6.96 6.83 CBOD '6UMML F UPDATED FLOWS PROPOSING PRODUCTION & QW INCREASE NBOD 1 Flow I 13.85 13.50 13.15 12.81 12.49 12.17 11.86 11.56 11.27 10.98 10.70 10.43 10.17 9.92 9.67 9.43 9.19 8.96 8.74 8.52 8.31 NBOD 23.93 24.08 24.23 24.38 24.53 24.68 24.83 24.98 25.13 25.28 25.43 25.58 25.73 25.87 26.02 26.17 26.32 26.47 26.62 26.77 26.92 I Flow I *** MODEL SUMMARY DATA *** Discharger : WAYNE POULTRY Receiving Stream : FISHER RIVER Summer 7Q10 : 23.0 Design Temperature: 25.0 Subbasin : 030702 Stream Class: C Winter 7Q10 : 34.0 'LENGTH' SLOPE' VELOCITY 1 DEPTH' Kd I Kd I Ka I Ka I KN I KN I KNR I KNR 1 SOD I SO0 I 1 mile 1 ft/mil fps 1 ft 'design' @20° 'design' @20° 'design' @20° 'design' @20° 'design) @20° 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 Segment 1 I 6.801 8.601 0.453 1 1.93 10.31 10.25 13.83 I 3.431 0.44 10.30 10.44 10.00 10.00 10.00 I Reach 1 I I I 1 1 1 1 1 1 1 1 1 I Flow 1 CBOD 1 NBOD I D.O. I 1 cfs 1 mg/l 1 mg/l 1 mg/1 I Segment 1 Reach 1 Waste 1 0.930 1206.800 1331.650 1 0.000 Headwaters) 23.000 1 2.000 1 1.000 1 7.440 Tributary 1 0.000 1 2.000 1 1.000 i 7.440 * Runoff 1 0.440 1 2.000 1 1.000 1 7.440 * Runoff flow is in cfs/mile North Carolina Division of Environmental Management Water Quality Section / Intensive Survey Group March 22, 1994 MEMORANDUM To: Ruth Swanek Through: Jay Sauber From: Howard Bryant Subject: Long-term BOD Analysis forPerdue Inc. (ROA22) County: Halifax NPDES #NC0028835 Receiving Stream: Roanoke River Sub -basin: 030208 DAY TKN--N NOX-N MI 0 0.26 3.1 14.00 17.0 5 5.51 0.76 5.4 12.00 17.0 10 9.45 1.00 3.9 13.00 17.0 15 14.52 0.45 3.3 12.00 15.0 20 17.88 25 19.78 30 22.54 0.06 10.0 13.00 23.0 35 24.23 40 25.65 50 27.82 60 29.10 0.07 1.9 14.00 16.0 70 30.84 80 32.28 90 33.46 0.06 1.7 13.00 15.0 100 34.77 110 35.66 120 36.33 0.04 1.8 14.00 16.0 140 37.62 Date Collected: October 5, 1993 1440 NBOD: 5.94 Collected by: Low pH: 8.0 CBOD: 31.68 cc: Central Files 1-1 Regional Water Quality Supervisor __30-0 . = 3 ' =-sC' Test evaluation: excellent Seeded: seeded CBOD/BOD-5: 5.75 M0►D Oh Li SLIMMER UPDATED FLOWS ACTUAL NH3N PRODUCT & QW CB,OD : BOD5=5 MODEL RESULTS c1 scharger : WAYNE POULTRY Receiving Stream : FISHER RIVER The End D.O. is 6.14 mg/1. The End CBOD is 12.19 mg/1. The End NBOD is 8.31 mg/1. WLA WLA WLA DO Min CBOD NBOD D0 Waste Flow (rng/1) Mi lepnint Reach # (mg/1) (mg/1) (mg/1) (rngd) Segment 1 5.91 3.74 1 Reach 1 413.40 331.65 0.00 0.60000 T '1/446 `A" "(13 14 C.&OD: BoD5 : (� W d v51-- (A. - I cc: Permits and Engineering Technical Support Branch County Health Dept. Central Files WSRO SOC PRIORITY PROJECT: Yes No _X_ To: Permits and Engineering Unit Water Quality Section Attention: Susan Robson Date: December 19, 1994 NPDES STAFF REPORT AND RECOMMENDATION County Surry Permit No. NC0006548 PART I - GENERAL INFORMATION 1. Facility and Address: Wayne Poultry P.O. Box 383 Dobson, N.C. 27107 2. Date of Investigation: December 15, 1994 3. Report Prepared by: Allan Smith, Environmental Tech. IV 4. Persons Contacted and Telephone Number: Rob Poindexter (910) 386-8151. 5. Directions to Site: From Winston-Salem, take Hwy. 52 N to Mt. Airy. From Mt. Airy take 601 S to Dobson. Turn right onto the Dobson exit and turn right off of the exit ramp onto SR 1100 (Atkins St.). The Wayne Poultry plant is located on SR 1100 on the left approx. 0.2 mile from the Hwy. 601 exit ramp. 6. Discharge Points(s), List for all discharge points: Latitude: 36° 24' 37" Longitude: 80° 41' 28" U.S.G.S. Quad No. B16NW U.S.G.S. Quad Name Dobson 7. Site size and expansion area consistent with application ? X Yes No If No, explain: 8. Topography (relationship to flood plain included): Facility is located on level ground well above flood plain. 9. Location of nearest dwelling: No buildings within 100' of discharge pipe. A 10. Receiving stream or affected surface waters: Fisher River a. Classification: "C" b. River Basin and Subbasin No.: 03-07-02 c. Describe receiving stream features and pertinent downstream uses: Consistent with its "C" classification. Part II - DESCRIPTION OF DISCHARGE AND TREATMENT WORKS 1. a. Volume of Wastewater to be permitted: 0.600 MGD (Ultimate Design Capacity) b. What is the current permitted capacity of the Waste Water Treatment facility? 0.480 MGD c. Actual treatment capacity of the current facility (current design capacity)? Unknown. The system was permitted at 0.510 MGD at one time because the facility requested that quantity for discharge. However, when it jumped the facility up to a grade 3, they lowered the permitted capacity to 0.480 MGD to remain a grade 2. d. Date(s) and construction activities allowed by previous Authorizations to Construct issued in the previous two years. None e. Please provide a description of existing or substantially constructed wastewater treatment facilities; The existing treatment system consists of 2 primary rotary screens, a secondary rotary screen, a 35' diameter dissolved air flotation unit, chemical addition (lime) for pH adjustment, an aerated lagoon, gas chlorination, and a continuous flow meter. f. Please provide a description of proposed wastewater treatment facilities. None g. Possible toxic impacts to surface waters: Chlorine. h. Pretreatment Program: Wayne Farms is considering a pretreatment program to,remove oil and grease if it continues to be a problem. A, ,) in development X approved should be required not needed NPDES Permit Staff Report Version 10/92 Page 2 2. Residuals handling and utilization/disposal scheme: a. If residuals are being land applied, please specify DEM Permit No. WO0004609. Residuals Contractor AMSCO. Telephone No. (910) 766-0328 b. Residuals stabilization: PSRP X PFRP Other c. Landfill: d. Other disposal/utilization scheme (Specify): 3. Treatment plant classification (attach completed rating sheet) . 3 1 4. SIC Code(s): 20/7 Primary 23 Secondary Main Treatment Unit Code: 0 5 0 3 PART III - OTHER PERTINENT INFORMATION 1. Is this facility being constructed with Construction Grant Funds or are any public monies involved. (municipals only)? NA 2. Special monitoring or limitations (including toxicity) requests: None 3. Important SOC, JOC or Compliance Schedule dates: (Please indicate) NA 4. Alternative Analysis Evaluation: Has the facility evaluated all of the non -discharge options available. Please provide regional perspective for each option evaluated. Spray Irrigation: Wayne Farms has a 5000 GPD spray irrigation permit (WQ0009826). They do not have enough land to handle all the waste product. Connection to Regional Sewer System: Quantity too great. Subsurface: Not feasible- NPDES Permit Staff Report Version 10/92 Page 3 PART IV - EVALUATION AND RECOMMENDATIONS Wayne Farms wants a 25% increase in chicken production. Their actual treatment capacity is unknown but Cabe Associates, Inc. has stated that their treatment system can handle the increase from 0.48 MPD to 0.60 MGD. This office has no objections to the production increase or subsequent increase in wastewater discharge as long as permit limits are met. Jo, Signature of report preparer 1.071/ Water Quality egional SuPervisor Date NPDES Permit Staff Report Version 10/92 Page 4 • • RATING SCALE FOR CLASSIFICATION OF WATER POLLUTION CONTROL SYSTEMS Name of Facility: 10 QY n 4. t—ar n` 5 Owner or Contact Person: Rob ? a; ft de x 4-e r : Mailing Address: P o• ?CA 3 g 3 Dobson , Al : C. On e ci County: S U K R Telephone; lee to) 3 8 (c. - S t$ i Present Classification; zrr New Facility Existing Facility_,,_ NPDES Per. No. N000 b G T y R Nondisc. Per. No.WQ ('GAG' LiteC 9 Health DeptPer No. Rated by: R il an Sm.-1-4 Telephone: (�'c) 177/ -yGCO. Date; fzf 'y `114 - Reviewed by:. Health Dept. Telephone: ' l- 11./ Regional Office Telephone:7 —44144 • Central Office Telephone: ORC; *PG b Po;i dex-J Grade: Telephone: <A L -ALL' Check Classification(s): _ Subsurface )_ Spr Irrigation ./'. , Land Application Wastewater Classification: (Circle Ono) 1 II IV Total Points: 57 , 14,PL NT PROCESSES AND MATED CONTROL EOUIPM 'JT WI4 CH ARE AN INTEGRAL PART OP INDUSTRIAL PPODUC'TM j;C SIDFRED WASTE TREATMENT FOR SHE PURPOSE OF CIASSi%&T1ON_ ALSO SEPTIC TAN{ SYSTEMS CONSISTING ONLY OF SEP11C IF►Mi ANDA 3AVRY_NORFICA►TION LINES APEDCEMPT MOM CtASSIFICATIGW. -�..�M-MIS--/�-�� �MM---M'�-MM-.. OMINIM _M SPRAY RRIGATbN CLIS9FlCAlletd $LS6t. AcE (checkall units that apply) 1... .all units apply) 1�pretlminary treatment (definition tea 22 ) ..._.�..sepak tSanks =,_.��� s,.._�..1PumP Was! septic (antis !`,_�siphoei or PumP'd°aing_systsms 4.�_Pump Was 4`,_�sand fattens 11`_9r•aso trap/Interceptor 1._—of/weter separators 6._� d hers 7._.—..grevity subsurface treatment and disposal: trapAntsrospler �, S,`_eressurs subsurfacesubsurfacetreatment and disposal: ,oC/watsr •opa:Woes S. ,disinfection 10.,,_.ohemic•1 addition for nutrientiatgae control gt�_,spraY irrigation of wastewater In addition to the shove classifications. pretreatment of wastewater In ith excess of these components stio shell ass be toted using the point tsting system and will require en operator appropriate 1st• MK APPLICATION/RESIDUALS CLASSIFICATION (Apples only to permit holder) 1. Land application of biosoilds. residuals or contaminated soils on a designated eke. - tit Or the technology k Ynua'u:iiy The following systems shall be assigned a Class f classification. ypltSS It* flow is of • signilicard quantity complex. to require consideration by the Commission on • case -by -case bask: (Chock 1 Appropriate) • 1,...Oil/water Separator Systems consisting only ol physical separation, pumps and dispose% `_Septic Tan lSend Finer Systems consisting only of septic tanks. dosing apparatus. pumps.s•nd filters. disinradion and direct discharge; lagoons, pumps. disinledbn. necessary chemical teeabrsen! for S_—Lregoon Systems cenststng only of pretlmtnary t»atmeed. lag algae or nutrierd control. end direct discharge; 41.__C1ased-loop Recycle Systems; air -stripping. carbon adsorpt disinfection b�__,_.Groundwater Remedsation Systems consisting only of oilhrater separators. pumps. and drspos* S`_.Aqu•culture operations with discharge to surface enters; 7..___Water Plant sludge handling and back -wash water treatment 5,,,___Sealood processing consisting of screening end disposal v�iiq dassilied : permitted alter July 1. 0.__�Singto•famiIy discharging systems. with the exception of Aerobic Treatment Units. 1903 or it upon Inspection by the Division. 2 Is found that the system is not bolosadequately rated or maintained. d• Such systems will be notifiedofthe etassgiecaEon or reclassification by the Commission.„ welting. WASTEWATERTREATM94T FACIUTYCIASSIFICAMN - The following scale Is used for rating wastewater treatment facilities: (circle appropriate points) ITEM POINTS 11) (2) Industrial Ptstrssatnsnt links or Industrial Pretreatment Program (see delhlkion No. 33).WWNWN.WNWN.N.WN.NWWNWNr4 DESIGN FLOW OF PLANT IN gpd (not applicable to rant contaminated cooing waters. *kedgehanding facilities for water puriicadon plants, totally dosed cycle systsms(see definition No.11), and facilities oorristing only of item (4Xd) or Items (4)(d) and (11)(d)) p,001 - 50.OW»».Y.ww.....ww.......................N»w»..w.........». ••.........w.W........NN2 50.001 - 100.00/0�./»»W..Yw..»w.w.WW.N«ww.».»»»»wN......... ....... . .»......»w.ww.w.3` 1100,001 •/��0.0/V�Y»»»w..»wN»w..»W.»..N.w.».w.ww.».NW......»»...•»...... Y•'•"'rr•u.•uw..•.......w..»».w.A 250.001 • 500.000•.MOO w.w.»w•W.»•.»w.»»N.•.Nowe w.wN»W....w..».».w•.N.»..».Y•••••• •».w.w.«•....»..¢ 60000001 - 100t;/0/..0�0/0•••»»».Y•...w..»...»»W»»w...........»....«».....»w....W»»«-Y»•••w• WN••••• 'M'�� 1.000.001 - 20000.000»w.wwwN..w....ww.•..W...W.«....w...•Ww...•wW.w...•••••»w•wOHO ••••••w•N•N•N•10 2,000.001 (and up) rate 1 point additional for each 200.000 rxxd capacity up to a maximum of W.••NwN•.•.30 Dsslgn Flaw (ppd) (3) PRELIMINAFIY UNITS/PRDC ES (see deli:Won Noa2) (a) Bar Screens Ww.•.WYN....wWwwwwW»•Y•••w•...wwww•.WWN.•••w•.••.....»•«N. .Z (b) oMec Mechanical Screens, Static Screens or Comminuting Dayton - ..wW...N..N� (c) GA Re rxtval»wwwY.••••••••wwww•••w» » o (d) MsdhsrrlcalorMn�atyedGrit Removal .»•»•»Y•YWWY. •.M..NNNN NwW»» ..•.wwNw2 (s) I Dowloe— •....••. ........ 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(1) Ytbn.wwW«•••w•••.....•N.w (4) PRIP MRYTRE1►1MBdTtNtISIPf10CGSSES (a) Ssptk Tank (see definition No. 43) b) Smolt Ta Nw•Y•YwYYW«•Y•••••Y•N•»..w»•.»..•.Nw.........w•...•w»w.w.N....Ww.Nww.•NN»Nw..S (c) Primary C1 �is.•»»Nww».»••...•..•••••.•..»w»w.»••.....•..•.•••.••••••••••••••••.••.•••.•...•.••••..••••w»•.••••w»WwwWw.A d) Settling Ponds or Setting Tanks for Inorganic Non -toxic Matertsls (sludge handling facMiss for water purfficatton plants, sand. gravel. stone, and other mining operatiors except recreational activities such as gem or goal mining) •NwwwN••••NW»•wwwwww»w»ww ••••••..••••••••••••••••••• » ....•••••• » 2 (5) (1) Instrumented Flow Measurement-..».... -- Y „ ,~~.W.. W«•»•»»»»•»»»• SECONDARY (a) Carbonaceous Stage (I) Asratbn•Iiigh Purity Oxygen S Diffused Air System Mechanical Air System (fixed. floating or rotor) - (b) ••N W•WNNw••••Y.Y.»•...•••••Y••••••Y•••••••N Separate Sludge (0) Udell? Finer MlghRate— MN. «.•...•N.•o..Nw.....wo..w--...•+«.«N••••• .w ....Nw.......+.+......»N.7 Standard Rya��ts•.«N.»««WN«...»W».....Nw....wN...N.»w».w.N••N•»•»••»••N«•W«•5 Packed Tour•...........NN..«.N.«««w.NNN..N« .N».NW..NN.5 Biological Aerated Filter or Aerated Bbbgkal Piker .N.W..N.«N.N»NW»-..N»....«.-N..•.....«-•10 Aerated Lagoon�s1......W.....««.....«WNw.....-..........»-.»...N.---.......«W««.NNW«.Ww10 Rotating Bbb lcal Contactors•••..WNWWWWNNN»•N«•W..•••N.« 10 «.N»..«WwW. Sand Fitters • ermlttent biological. _ -- ..YNN...»...«»N....NW2 Recirculating biological.......w.....«»YNN««»•WN•••-»N«N••W•«N• ......••, Stabilization Lagoons WWwNWWw.N .__ N .»•••» CIrlin.••.wWM.M .«MWWWN. .NNWN••YwWW W.NNN.« .1� Y••••Y•Y•••YNNYWN.•W.Yw Y.N� WWW«.N Single stage system for combined carbonaceous removal of SOD and nitrogenous removal nitrification (sae definition No. 12)(Points for this kern have to be in addition to kerns (5)(a)(1) through (5)(a)(vl). utilizing the extended aeration process (see definition No.3a) Y•Y»»..»WYw•..WNWW...NW2 utdlztng other than the extended aeration p x) Nutrient addlirons toenhance BOD mmoia'»N..YN...N.wW.YNM.wY.WMW.NWWw«wWW xi) Biological Culture ('Super Bugs')addition.NNN..Y•W..•N.•Y.••»•••w•NN.NWWNW.•••NWwwNJS nous Stage in • Aeration - high Purity Oxygen System - Diffused Air System.-....•..»--- •••••N.•••.N•YWNw••••NWYwN.N Mechanical Air System (fixed, ftoating or rot Separate Sludge Reasratbn (g) Trkixlirg Flttsr•Iggh Rate 7 Standard Rate...........».YwN••.•N».»w»...w.Yw...-.N.««»N.».....Y.»N..wY.»»«•»•N.»»•»• •S Packed Tower.... N»....»NWN••Y«W.WW«w........•....—.N...N»••.M•»-NWNN --5 Biological Aerated Filter or Aerated Biological Filet NN.W...1 0 Rotating Biological Contactors................Ww.N----.................--............10 Sand Fitter • Intermittent bkrlogkal.NwN.Y.».YWWM-w N••••••WW..2 .1 «•W«Www•M•••••• Y....Y•..MM«W«••••wN . W W Y►»W•Ww•NN•.NYW•WNN•••••w»N•N•«•wwW» - - 0 »10 2 a Recirculating biological __ .---.—................----1 C'wY..wwWNN»•N•W N• W«••N»wY••»W W wwWN 1ERTIARYORADVANCEDTREND/ENT LW1 SIPRDCESSES (a) Activated Carbon Beds - (b) FY) (vl) without carbon nageneraston..»»N.N..Y.....WwWWNw with carbon agsneatbn.N.w...».».NY....WW»W Powdsrsd or Granular Activated Carbon Tied - without carbon regene rattonNW.N..«NwW».N.N.W..N»YY»Y..Y. WW� N.NM•Y.w•»«•W W «wWN.b .«W.....wwa ...WWNN15 with carbon regsners on»WW.»»W«.wWN»»«wWWNNNwNW.M.Y.Y•MN.Y•«..•WWN••••wWY»5 o) Air /�s�t/rip/piin}erg! WWWfYN•wN•.NWW«•.•YwWN..wYWww.NYN.Y•«••••wwWN•YMNM.Y.YMY•►••••«WwWWYN•a • d Denktfficla ,Y�•M..Y«»Y».N«.WW«WW»...wWa.W«wN.YW.w...•W....WN.»N...Y..M..NN»•...«.W«W».....»� • Electrodlalysb. f) Foam .Separation.N..NN.w.N.»•N•N«w..NN.NNN.N•....N•WWWwNwNN.•.N•N•w•NNNw.NY.•NNW.N•N••••NWNwwM1RR NN.N.NNN wNWN.«NwN•••»NNN•NNWWN•»N..•N•w•S N.N.«NNN.•WY•MN•.Y (h) Land Application of Treated Effluent (sits definition No. 22b) (not applicable for sand. gravel. stone and other similar mining operations) by high rats k�iltratlon. N»WNW»Nw.N...».•»»••••••••••�••••� Mkroscrssns..N'..N.N..N«..N N•.WN«NNN/��w•..NNNQ��•J_/���NNNW NN•twNW.N•NN•N•.••NWN.WNw.••••••••••••Y••••••� Phosphorous Removal by Bbbgfcat PmOcesses (S.o defWtlon No. 2a)N•...N......Ww««.wN.wNNNNWW«WW20 Polls g Ponds - without aeration.... .. YWNNNww .N •••-•»»•Y• with asratlonN«.».Y............»...»»Y«».Y»..».W..»N»»»......».....YNW».»...N.N.«Y»».........a g) ion Exchange......»WNW IDS diffused or mechanical.......».........». 2 (m) R'ev-./eeJrs�e Osmosis .N.N... ......N....N.N.N 5 (n) Sand Y. M1x MNYia i e.• - 1�1...N.NNI.NN.N.N.Y..»N.»NNNY....N.NN....NN.N....N....NN. N....NN..N.»w..wwZ (0) Treatment processes for removal of metal or cyanide nigh rate ... .51 (p) treatment processes for removal of toxic materials other than metal or cyranWs........NN.»...NN.Y.:.NN.»N.NY.N.15 (7) SLUOGETREATMBNt• (a) Sludge Digestion Tank Heated (anaerobic). — Aerobic N.NN.N..NN M.N.NN.MN..N.NN..NN..NNN..N.N.NN.Y. N....N». ..NNN.N»w. 15� Unheated (anae c).N....N.NN.NN..N......NN.N..».NN..NN...... N..NN..NN.».».N...N.N.».....NN...... NNNMi (b) Sludge Stabilization (chemical or thermat)..w.N..»..N.».N.N.N»..........N... ...N....»..N...»... 5 (e) Sludge Drying Beds - Gravity.......NN.NN.N.N.N.N..N...NN.»..w..........NY.N.NN.N..........N....N.NN.N..N».w.N.N2 Vacuum Assfated........N.N.N.».NN..»......».N...N. N..NN. 5 (d) Sludge Elutrlatlon....»N. N........N...».... N.N. »....N.NM (s) Sludge Condltlonsr (chemical or thermal).--.--- NN.N.NN.NNNN...NNNNNNNNN..S (f) Sludge Thickener (gravity) Dissolved Alt Flotation Unit (not applicable to a unit rated as (3)(I)J (h) Sludge Gas Utilization (including gas storage)....»... ......... N....N.NN.....N..w (I) Sludge Holding Tank - Aerated ...NN..NN..N...N.N.......NN»N..Y»NN..M Non -aerated 5 ..». N. 5 2 (j) Sludge Incinerator (not including activated carbon regeneration 0 (9) RESIDUALS UriLummTIONr, Centrifuge. POSALl.� orJFitter Press or other similar dewatertng devices.. ur incinerated ash) .N.. (a) Lagoons 2 (b) Land Application (surface and subsurface) (see definition 22a) by contracting to a land application operator or landfill operator who holds the land apptkation permit or landfill permit...w....N N.., N...10 (c) • Dedicated Landfill(burial) by the permittas of the wastewater treatment facltltyw.N......... ....N.N..N.N..N.N..N.Y5 (a) Chlotinatbn..».»..NN.N......... N..... N.N.NNN.N..N.NN.N.».N..NNN.N.......N.................. N..NN.N....N.N.N.N......... (b) ■■//D����.��rfn�M..N......N...»NN.NNNN...N....NN.N.N.N.N. N..NN...N..NN.N.»NN.N ......NN. 5 (c) r.ZOne...N.NNN.NNN..».N.»..NN........NNN.NNN..N.N.N.N..NNN.NN.NN...N.NNN.N..N.-NNNN.N......N.N.NN......N. Sid (d) Radiation ... N.N.N..NN..NN..N».N.N.N..N NN..N.N ... ...M CHEMICAL ADDITION SYSTEMS) ( sea dsftnalon No. 9) (not applicable to chemical additions rated as Um (3)(J). (5)(a)(xt). (6)(a)• (6)(b) (7)(b), (7)(e). (9a). (9)(b) or (9)(c) 6 points each: Ust�N �d�.�;f�a+....N....N...N.N..N....NN.N.N.N:NN....»........N.N«.N N.N....N....N...»........NY.N.... �����T....NNNN...........NN.NNN.............NN..N..N.N..N..NN..NN ... NNNNN..N.NNNNNNN.N.. .N»»..NNNN. (11) MISCELLANEOUS Uk TSIPFCCESSES • (a) Holding Ponds. Holding Tanks or Settling Ponds for Organic or Toxic Materials including wastes from mining operations containing nitrogen or phosphorus compounds in amounts significantly greater than is common for domestic wastewater (b) Effluent Flow Equalization (not applicable to storage basins which an inherent In land application systems)...) (c) Stage Discharge (not applicable to storage basins inherent in land application systems)------- d) PumpsNN..................N.N...N...... ..... ...NNNN.....N.N. N.N.N..N N.N..N N.N.» .... (e) Stand -By Power Supply ...N..N N.N.N.NN.....NN.N..NN...N.N..... NN..N..N.....N Thermal �M���333191JJJ/ it) Poflutbn Control Device .NN..N...N.NN.���N�N.N.N..NNN..N...N.N..N.N..N .N.N...N. S TOTAL POINTS..»N.NN..N.NN....»N....... ...N.NN.N..NNNL `'' .NNN..NNNN...NN»NNN.N»»»N..N.N»N........ ......... NN............... 5 NYA S T C Gass IN.N.N.N.NN►.N.N.NN.N.NN..NN.N..».N» N.N.N 5-25 Points Class IL.NN.....NN.NNN►NN.N.N............... NwNN.N..N»N.N.NNN.NN»N.N»26.50 Points Ctassill .N.N..» N.NNNN....N.NN..N.NN.N.N.N.NN.N.N.N.N.NN.N.N....N.N..NNN.51.65 Points CtaR71 11/00.N.N.N.NN.NN.N..N.N.NN.N.NN.N.N.N.......N.N...N..»N.N..»N.N66-tp Points Facilities having a rating of one through four points. Inclusive. do not require a certified operator. Facilities having an activated sludge proosss wtil be assigned a mlnimum classification of Class IL Fadxftiss having treatment processes for the removal of metal or cyanid, will be assigned a minimum dasslfkation of Class IL Fadntiss having treatment processes for the biological removal of phosphorus wtA be assigned a minimum classification of Class III. .0004 DEFINITIONS The following definitions shall apply throughout this Subchapter. (1) Activated Carbon Beds. A physkaVc hemkal method for reducing soluble organic material from wastewater effluent; The column -type beds used In this method will have a flow rate varying from two to eight gallons per minute per square foot and may be either upflow or downflow carbon beds. Carbon may or may not be regenerated on the wastewater treatment plant she; (2) Aerated Lagoons. A basin in which ail solids are maintained in suspension and by which biological oxidation or organic matter Is reduced through artificially accelerated transfer of oxygen on a flow -through bask; (3) Mratbn. A process of bringing about intimate contact between aft or Ngh purity oxygen in a liquid by spraying. agttatbn or di fusion.(3a) Extended Aeration. An activated sludge process utilizing a mdnlmum hydraulic detention time of 10 hours. (4) Agriculturally managed site. Any she on which a crop is produced. managed. and harvested (Crop includes grasses. grains. trees, eta); (5) Air Stripping. A process by which the ammonium ion is first cornerted to dissolved ammonia (pH adjustment) with the ammonia then released to the atmosphere by physical means; or other similar processes which remove petroleum products such as benzene. toluene. and xylem,; (t3�nReRege ratlon. The regeneration d exhausted carbon by the use of a firma to provide extremey Ngh temperatures which volatilize and oxidize the abs(7) Carbonaceous Stage. A stage of wastewater treatment designed to'actievs affluent limits; (a) Centrifuge. A mechanical device In which centrifugal force Is used to separate solids from liquids or to separate liquids of different denstt1es (a) Chemical Addition Systems- The addition of chemical(s) to wastewater at an application point for purposes d improving solids removal. pH adjustment. alkalinity control. eta; the capability to experiment with different chemicals and different application points to achieve a spectnc result win be considered one system; the capability to add chemical(s) to dual units win be rated as one system; capability to add a chemical at a different application points for different purposes will result in the systems being rated as separate systems; (10) Chemical Sludge Condtibning. The addition of a chemical compound such as lime. Ionic chbtide. or a polymer to wet sludge to coalesce the mass prior to is application to a dewaterff g device; (11) Closed Cyds Systems. Use of holding ponds or holding tanks for containment of wastewater contalntng Inorganic, non -toxic matertak from sand. gravel, crushed stone or other similar operations. Such systems shag carry a maximum of two points regardless of pumping facilities or any other appurtenances; (12) Combined Removal of Carbonaceous BOD and Nitrogenous Removal by Nttrtfkatbn. A single stage system required to achieve permit effluent limits on BOD and ammonia narogsn within the same biological reactor. (13) Dechbrtnatbn. The partial or complete reduction of residual ctiortne in a liquid by arty chemical or physkai process; (14) Denitr[fkatbn Process. The conversion of nitrate -nitrogen b nitrogen gas; - • 1263 523 • •:, 11J V i:. 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