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HomeMy WebLinkAboutNC0023884_Permit Issuance_20060828Michael F. Easley; Governor State of North Carolina. Q� QG William G. Ross, Jr., Secretary . �} Department of Environment and Natural Resources Alan W. Klimek, P.E., Director Division of Water Quality August-28, 2006 Mr. Matt Bernhardt .- Salisbury -Rowan Utilities . 1 Water Street Salisbury, North Carolina 28144 - _m Subject: °NPDES Permit Issuance- -Permit NCO023884 Salisbury -Rowan WWTP Rowan County. Dear Mr. Bernhardt: Division personnel have reviewed -and approved_ your application for renewal of the ' subject permit: Accordingly, we are forwarding the- attached NPDES discharge permit.. This permit is issued `pursuant'to the requirements of North Carolina General Statute 143-215.1 and the . Memorandum of . Agreement between -North .Carolina .and the U.S.: Environmental Protection Agency dated May 9, 1994 (or' as subsequently amended): 1 The permit authorizes Salisbury to discharge' up "to 12.5 MGD (as well as an expansion :phase to 20 MGD) of treated wastewater to the Yadkin -River; a ,class WS-V water in. the Yadkin Pee Dee River Basin. The permit includes discharge limitations or monitoring requirements for flow, biochemical oxygen demand (BOD),= total. suspended solids (TSS), ammonia, fecal coliforlm bacteria, total: residual, chlorine, total nitrogen, total phosphorus, selenium, and other parameters. After substantial collaboration and input from the city -of. Salisbury, DWQ; and the EPA, the final NPDES permit includes the following: The uistream waste concentration (IWC) for the Salisbury - Rowan VA has been revised. This is basedon the results of the updated CORMIX'modelf provided by Salisbury staff in January 2006 (and subsequently reviewed by - DWQ stag. The model run included revised stream flow information and.a . naodificationto close two. of the ports on the existing three -port diffuser. (DWQ received confirmation that the modification . of.the diffuser was completed- in* . May. 17, 2006): The other variable included" the critical condition -now, being the lake level of 5 feet below full pool for developing limits for toxicants. Based on the results of the CORMIX model, ' the -instream waste concentrations are 5.3 % at 12.5 MGD and,4% at 20 MGD.. .The addition- of a special condition requiring a dye study be conducted at low and high flows in the Yadkin River when the average discharge flow is equal to 80%.of the design flow of 12.5 MGD. See. Special Condition A. (7). , No Carolina North Carolina Division of Water Quality 1617 Mail Service Center Raleigh, NC 27699-1617 Phone (919) 733-7015 )CtllCQi�1J e Internet: '%immu waterauality.or_ Location: 512 N. Salisbury St. Raleigh, NC 27604 Fax (919) 733-2496 1-817-623-6748 An Equal OpportunilylAffirmOmAction Employer— 5D%Recycledfily%Post Consumer Paper ' Permit NCO023884 STATE OF NORTH CAROLINA �.. DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES DIVISION OF WATER QUALITY. PERMIT TO DISCHARGE WASTEWATER UNDERTHE- NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM In compliance with the provision of North Carolina General Statute '143-215.1, other -lawful standards and regulations promulgated and adopted by the North Carolina Environmental Management Commission, and the Federal Water Pollution Control Act, as amended, the City of Salisbury `.. . is hereby authorized to discharge wastewater from the facilities located at the Salisbury -Rowan WWTP . 1915 Grubb -Ferry Road = Rowan County gi2�l and.. 850 Heiligtown Road East Spencer,. Rowan County to receiving waters designated as the Yadkin River in the Yadkin -Pee Dee River Basin in accordance with effluent limitations, monitoring. requirements; and other conditions set forth in Parts I, II, III, and IV . . hereof. The permit. shall become effective October 1, 2006: This permit and the authorization to discharge shall expire at midnight on June 30, 2009. Signed this day August 28, 2006., Alan W. Klimek, P.E. Division of Water Quality By Authority of the Environmental Management. Commission Permit NC002388.4 . SUPPLEMENT TO PERMIT COVER SHEET All previous NPDES Permits issued to this facility, whether for operation or discharge are hereby revoked, and as of. this issuance, any previousli issued permit bearing this number is no longer effective. Therefore, the exclusive authority to operate and discharge from this facility arises under the permit. conditions, requirements, terms, and provisions included herein. The City of Salisbury is hereby authorized to: 1. Continue to operate and maintain the.existing 7.5 MGD Grant/ Creek Wastewater Treatment Train consisting of ➢ Influent parshall flume_- ➢ Four mechanical bar screens . ➢ - Four grit chambers ➢ Aeration basin with mechanical floating aerators and mixers ➢ Two circular clarifiers and two rectangular clarifiers ➢ Four primary clarifiers ➢ Two trickling filters ➢ Screw pump lift station ➢ Two aerobic digesters ➢ Belt filter press ➢ Standby power generator ➢ Effluent pump station jA�o� ➢ Flow measurement instrumentation Splir� 4oip This treatment train is located on Grubb Ferry Road near S cer in Rowan County. 2. Continue.to operate and maintain the existing 5.0 MGD Town Creek Wastewater Treatment Train consisting of: ➢ Two mechanical bar screens ➢ Two grit and grease removal units ➢ Two aeration basins with fixed mechanical aerators and mixers ➢ Two secondary clarifiers Screw pump lift station ➢ Two aerobic digesters ➢ Standby power generator - ➢ Flow measurement ➢. Sludge dewatering •facilities. ➢ Effluent pump station This treatment train is located on Heiligtown Road near East Spencer in Rowan County.' 3. - Continue to operate and maintain an ultraviolet or sodium hypochlorite disinfection system, cascade post aerator, Parshall flume, effluent sampling station and diffuser at the Yadkin River treatment train. 4.: After receiving an Authorization to Construct from the Division, construct and operate a 20.0 MGD wastewater treatment system. 5. Discharge from said treatment works at the location specified on the attached map through Outfall 001 into the Yadkin River, currently classified WS-V waters in the Yadkin -Pee Dee River Basin. 1 tiF q f �S (/ �) r ✓�. d },- ff�+J J `1 3) k�i \ 1• r( J r I U IC r r t' .. �C (- /. , :�L.�F\" ,4�' it%` ,? t 't ��ri �-./�"'� l`•`VS'� ��' Gi:` �,; 'i5 �/� 4 / •� Iti �=�+♦ Ip�` /i q T \v '! r� a �'Q" -�,�� �%` w '` ) y, l�r ``� �i � �1/1-* � t� r .:fir - . �='� �� , r / c dlri•. � •:��''_/ �` `1 Y L���iJ ` � l•. �,\r / �7,���, �•. 1L!f � � c -� \ � � \ i r �• fir` k �.�1 ' ✓ p . � •� .. �. t �`'���J 'Y:,, �V 'xy/ ` �Yr /% 1 •jam`= �` �� _ / ���, . 1 •,(�.. �_: r�illf� iJ L fi fr (' r � � ,� � • fir_ - \moo �` _' �'4���,.��:~ � '•4 ✓�� l r�. � \:w? � �j`'t,..� �'i�1. o �� � i✓%J.� i'i,l t.,'' ;. 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'e r•1 .a6 1. 1.�,; \'.`trt •.i��.1 _ s <aix'_-d.+�. �'+��-.�.� j�'��\ Wr �.y ��, L/ 'IJ � . ,. •»' �\" ?@�— _ 6 f v� � ter • � ��` "`�..,ti,...��-=;�_ ��� � � - EI JjJ•' ;•1�' lR•`t\ icy- f�• / ! s '.,~ �,,rl�- �St"' _ � �" ��'+t-_ r tJ 1� ,p�, � • �• � `�� ��•'. •� 5! %'`\-^,4[ FAY}Ty�{ -.r (�y/��ia'ift{zJ� �j\��'� • .�:�'r / jj('`'� � ;t-s l __ �[/ �� � 7 d . .' `} i. �' 1L=rr !S�\ �.\ 4.1.E J �• • •�. �•'�ft' /` !%r •'' : V\"••r�..�� f i 1 .r .. -. t {� j Wit_ !:-� • .C�_i J r c r�� / �y 1 tii '�� � i t 'L ",'--}.r 'ref It: C. i'l.• / J i���r.��: t �'� t a�il� •. �I �`•E L }yam} r i��f i � 1� �. ✓�... t..�� r •, r i�2 r �� V '� •T'1 � r _ Salisbury -Rowan WWTP State Gdd/Ouad: E17NW/Salisbury Latitude: 35. 44' 07" N Loneitude: 80.26' 50" W Receivine Stream: Yadkin River Drainmee Basin: Yadkin Stream Class: WS-V Sub -Basin: 03-07-04 ��. - • .moo - � Y ,. .•. . � • - � : m \jam V� ��� � r .r;-�iP i, y� e 1;. t r 1 1�+ `.fit r f -tt L% � \ l � ��: , , 4% f•E `� E 1 r -^ t., � / �[\t /i \..zJ y' .t( h •+•� •,fir t Ripl y Sw �YR r :rn yt� sss Facility Location _ e not to scale NPDES Permit No. NC0023884 iVOrth Rowan County Permit NC0023884 A. (1) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS (12.5 MGD) During the period beginning on, October 1, 2006 and lasting until expansion beyond 12.5_ MGD, the Permittee is authorized to discharge from Outfall 001. Such discharges shall be limited and monitored by the Permittee as specified below. x +wU"y-,., a., fig, f , g � Y v ' a � b,"d' ..Y 1Vlonthly . `T` ;'a*- a.. t.r u =-f2 •,.'F:i1 i°; ,_ IMI,T�AT.[ONS-�t-a rq a£* K t,� - "?*'�' Weekly Dally Maximum= b 3c.^`" ..��. ,: ;yS}r,a °r,,i r, �;3.s.:. '' x.`i".t'"'" d're; ¢;'•�,v.: A MQNiTORTNG QLflT2CM N S � r �„ S3i1 ,h"i#' may... - M®asurement a Sample TypeSadnpteLocatio; µPre uenc 'F i �:�_ ON Flow 12.5MGD6 Continuous Recording Influent or Effluent BOD, 5 day, 20 °C (April 1 to October 31 5 15.0 mg/L. 22.5 mg/L Daily Composite Influent and Effluent BOD, 5 day, 20 °C- November 1 to March 31 5 30.0 mg/L 45.0 mg/L Daily Composite Influent and Effluent Total Suspended Solids5 30.0 mg/L 45.0 mg/L Daily Composite Influent and Effluent- NH3 as N (April 1 to October 31 6.0 mg/L 18.0 mg/I Daily Composite Effluent NH3 as N November 1 to March 31 12.0 mg/L 35.0 mg/I Daily Composite Effluent Dissolved Oxygen2 - Daily Grab Effluent--. Fecal Colifohm geometric mean 200/100 ml 400/100 ml Daily Grab Effluent Temperature Daily - Grab Effluent pH > 6.0 and < 9.0 standard units Daily Grab Effluent Total Residual Chlorine3 28 Ng/L Daily Grab Effluent Total Nitrogen (NO2 + NO3 + TKN) Weekly. Composite Effluent -Total Phosphorus Weekly Composite Effluent Total Silver Monthly Composite Effluent Total Copper Monthly Composite Effluent Total Zinc Monthly Composite Effluent Total Selenium7 Monthly : = Composite Effluent Total Selenium8 95 Ng/L Weekly Composite Effluent Effluent Pollutant Scan9 9 9 Effluent Chronic To)(idty4Quarterly Composite Effluent - Notes: 1. Combined effluent from the Grant Creek and Town Creek treatment trains, except that flow, BOD, and TSS shall be sampled separately at the Town Creek treatment train and the -Grant Creek treatment train. BOD and TSS removal efficiency shall be calculated -by mathematically aggregating the values for the'Grant Creek and the Town Creek treatment train. (Refer to A. (6).) 2. _ The daily average dissolved oxygen effluent concentration shall not be less than 5.0 mg/L. 3. Monitoring only applies if chlorine is added to the treatment system. 4. Chronic Toxicity limit (Ceriadaphnia) at 5.3 % with testing in Maazch, June, September and December (see A. (4)). 5. The monthly average effluent BODS and Total Suspended Solids concentrations shall not exceed 15% of the respective influent value (85% removal)., . 6. 7.5 MGD at Grant Creek treatment train. 5.0 MGD at Town Creek treatment train. 7. Monitoring requirement may be deleted upon written notification from the permitting authority. , 8. The limitation for total selenium will take effect April 1, 2008. -This limit may be deleted upon written notification from the permitting authority. 9. Effluent pollutant scan must be done three times with seasonal variation before next permit application. See A. (8). There shall be no discharge of floating solids or visible foam in other than trace amounts. Permit NCO023884 A. (2) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS (20 MGD) During the period beginning after expansion beyond 12.5 MGD and lasting until expiration, the Pern ittee is - - -authorized to discharge from Outfall 001. Such discharges shall be limited and monitored by the Permittee as specified below )k s 4 vytP3^3XF',. *eG rr yy "�',ie.. _ 4S`F "c y'x'.i �€k '-, Y pAU AMFTER _ F7L E—N,T;U ,, T{ATIONS � MONITORING REQ;YTIREMENTS z C ` '/ A. :.1.°i^•S .Y 7 J t rY .�'•,ih t $mttX^ Y wh1Ch i fr Z i 4-• ; Weekly Daily lYleasurement Samp7eXypey SampleL`ocatfonV # RAIMonthly t .P .., ..:.�. _Avera er .Aver<a a 3- =:1VIazimum, •_ r:Fre uenc . .. z�}� w ..s k .aka Flow r 20 MGD Continuous Recording Effluent BOD, 5 day, 20 °C - 5.0 mg/L 7.5 mg/L Daily Composite . Influent and Effluent (April 1 to October 31 5 _BOD, 5 day, 20 °C 10.0 mg/L 15.0 mg/L _ Daily Composite Influent and Effluent November 1 to March 31 5 Total Suspended Solids5... 30.0 mg/L 45.0 mg/L Daily Composite Influent and Effluent NH3 as N 1.0 mg/L 3.0 mg/L Daily Composite Effluent (April 1 to October 31 NH3. as N - 2.0 mg/L 6.0 mg/L Daily Composite l Effluent Novmber 1 to March 31 _ Dissolved Oxygen2 - Daily Grab Effluent . Fecal Coliform 200/100 ml 400/100 ml Daily Grab Effluent geometric mean Temperature, Daily Grab Effluent pH > 6.0 and < 9.0 standard units Daily Grab . Effluent Total Residual Chlorine3 28 Ng/L = Daily Grab- ° Effluent Total Nitrogen Weekly Composite . _ Effluent (NO2 + NO3 + TKN) Total Phosphorus Weekly Composite Effluent Total Silver Monthly Composite Effluent Total Copper Monthly Composite Effluent . Total Zinc Monthly Grab Effluent Total Selenium6 Monthly Composite Effluent Total Selenium7. 124 pg/L Weekly Grab Effluent Effluent Pollutant Scan8 8 8 Effluent Chronic Toxicity4 Quarterly Composite Effluent. Notes: 1. Sample locations: Effluent -Combined Effluent from Grant Creek/ and Town Creek 2. The daily average dissolved oxygen effluent concentration shall not be less than 5.0 mg/L. 3. 'Monitoring only applies if chlorine is added to the treatment system for disinfection. 4. Chronic Toxicity limit (Ceriodaphnia) at 4 % with tests in March, June, September and December (see A. (5)). 5; The monthly average effluent BODS and Total Suspended Solids concentrations shall not exceed_ 15% of the respective influent value (85% removal). 6. Monitoring requirement may be deleted upon written notification from the permitting authority. 7. The limitation for total selenium will take effect April 1, 2008. This limit may be deleted upon written notification from the permitting authority. 8. Effluent pollutant scan must be done three times with seasonal variation before next permit application. See -A. (8). There shall be no discharge of floating solids or visible foam in other than trace amounts. - Permit NCO023884 A. (3) INSTREAM MONITORING -REQUIREMENTS f,G �t'v` t� }.� Y�` PARAMETER l 'SN"M yr'.. 2*- 'C i y CY 4Y � 1VIOIVITORING3REQUmtEWNTS i .,r rS Y }s�'S yl,"f "k T l'i�' jc"1•`E'"'V3 ''Y - xW vA J 2,NtT� L t x a eT �L. a�Pm 1�can�a ;Dissolved Oxygen- June -September 3/week Grab Upstream & Downstream October -Ma 1/week PH June -September 3/week Grab Upstream & Downstream October -Ma 1/week Temperature - June -September 3/week Grab Upstream & Downstream October -Ma 1/week - - Total Phosphorus - June -September 1/month Grab Upstream & Downstream �NOz+NO3 June -September 1/month Grab U stream & Downstream 'NH3 as N June -September 1/month Grab Upstream & Downstream tTotal K•eldahl Nitrogen . June -September 1/month - Grab . Upstream & Downstream fiChloro h II -a June -September 1/month Grab Downstream . Notes Upstream = at least 200 feet upstream of the discharge. point Downstream = 0.7 miles above Southern Railroad Bridge. As a participant in the Yadkin Pee -Dee River Basin Association, the instieam monitoring requirements as ` stated above are waived: Should your membership in -the agreement be terminated; you shallnotify the Division immediately and the instream monitoring reqwrements specified in your permit shall be reinstated. As per 15A NCAC 2B.0505 (c):(4); stream -sampling may be discontinued at such .time as flow conditions -in the receiving waters or extreme weather conditions will result in a substantial risk -of injury or, death to persons collecting samples. In such. cases, on each. day that sampling is discontinued, written justification... - for the discontinuance shall be, specified in the monitoring report for the month in which the event . occurred. This provision shall be strictly construed and may not .be utilized to avoid the -requirements of 15A NCAC 2B.0500 when performance of these requirements -is attainable. When sampling is discontinued pursuant to this provision, stream. sampling shall be resumed at the -first opportunity after the risk period has ended. Permit NC0023884 A. (4) CHRONIC TOXICITY PERMIT. LIMIT (QRTRLY) at 12.5 MGD The effluent discharge shall at no time exhibit observable inhibition of reproduction or significant mortality to . Ceriodaphnia dubia at an effluent concentration of 5.3%. The permit holder shall per -form at a minimum, u� artery monitoring using test procedures outlined in the "North Carolina Ceriodaphnia Chronic Effluent Bioassay Procedure," Revised February 1998, or subsequent versions or "North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions. The tests will be performed -during the months of March, June, September and December. Effluent sampling for this testing shall be performed at the NPDES permitted final effluent discharge below all treatment processes. If the test procedure performed as the first test of any_ single quarter results in a failure or ChV below the permit limit, then multiple -concentration testing shall be performed at a minimum, in each of the two following months as described in "North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions. The chronic value for multiple concentration tests will be determined using the geometric mean of the highest ` concentration having no detectable impairment of reproduction or survival and the lowest concentration that does s- have a detectable impairment of reproduction or survival. The definition of "detectable impairment," collection methods, exposure regimes, and further statistical methods are specified.in the "North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions. All toxicity testing results required as part of this permit condition will be entered on the Effluent Discharge. Monitoring Form (MR-1) for the months in which tests were performed, using the parameter code TGP3B for the pass/fail results and T_HP3B for the Chronic Value. Additionally, DWQ Form AT-3 (original) is to be sent to the following address: Attention: North Carolina Division -of Water Quality Environmental Sciences Section.. 1621 Mail Service Center Raleigh, North Carolina 27699-1621 -Completed Aquatic Toxicity Test Forms shall be filed with the Environmental Sciences Section rio later than 30 daps after the end of the reporting period for which the report is made. Test data shall be complete, accurate, include all supporting chemical/physical measurements and all concentration/response data, and be certified by laboratory supervisor and ORC or approved designate signature. Total residual chlorine of the effluent toxicity sample must be measured and reported if chlorine is employed for disinfection of the waste stream. Should there be no discharge of flow from the facility during a month in which toxicity monitoring is required, the permittee will complete the information located at the top of the aquatic toxicity (AT) test form indicating the facility name, permit number, pipe number, county, and the month/year of the report with the notation of "No Flow" in the comment area of the form. The report shall be submitted to the Environmental Sciences Section at the address cited above. Should the permittee fail to monitor during a month in which toxicity monitoring is required, monitoring will be required during the following month. Should any test data from this monitoring requirement or tests performed by the North Carolina Division of Water Quality indicate 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, minimum control organism reproduction, and appropriate environmental controls, shall constitute an invalid test and will require immediate follow-up testing to be completed no later than the last day of the month following the month of the -initial -monitoring. Permit NCO023884 A_ (5) CHRONIC TOXICITY PERMIT LIMIT (QRTRLY) at 20 MGD The effluent discharge shall at no time exhibit observable inhibition of reproduction or significant mortality to Ceriodaphnia dubia at an effluent concentration of 4%. The permit holder shall perform at a minimum, u� a?terly monitoring using test procedures outlined in the "North Carolina Ceriodaphnia Chronic Effluent Bioassay Procedure," Revised February 1998, or subsequent versions or "North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions. The tests will be performed during the months of March, June, September and December: Effluent sampling for this testing shallbe performed at the NPDES permitted final effluent discharge below all treatment processes. If the test procedure performed as the first test of any single quarter results in a failure or ChV below the permit limit, then multiple -concentration testing shall be performed" at a minimum, in each of the two following months as described in "North Carolina Phase II Chronic Whole Effluent Toxicity Test _ Procedure" (Revised -February 1998). or subsequent versions. The chronic value for multiple concentration tests will be determined using the geometric mean of the highest . concentration having no detectable impairment of reproduction or survival and the lowest concentration that does ."have a detectable impairment of reproduction or survival. The definition -of "detectable impairment," collection methods, exposure regimes, and further statistical methods are specified in the "North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions. All toxicity testing results required as part of this permit- condition will be entered on the Effluent Discharge Monitoring Form (MR-1) for the months in which tests were performed, using the parameter -code TGP3B for the pass/fail results and THP3B for the Chronic Value. Additionally, DWQ Form AT-3 (original) is to be sent to_the following -address: Attention:. North Carolina Division of Water Quality Environmental Sciences Section - 1621 Mail -Service Center_ Raleigh, North Carolina 27699-1621 _-Completed Aquatic -Toxicity Test Forms shall be filed with the Environmental Sciences Section no later than 30 days after the end of the reporting period for which the -report -is made. --Test data shall be complete, accurate, include all supporting chemical/physical measurements and all concentration/response data, and be certified by laboratory supervisor and ORC or approved designate signature.' -Total residual chlorine'of the effluent toxicity sample must be measured and reported if chlorine is employed for disinfection of the waste stream. Should there be no discharge of flow from the facility during -a month in which toxicity monitoring is required, the permittee will complete the information located at the top of the aquatic toxicity (AT) test form indicating the facility name, permit number, pipe number, county, and the month/year of the report with the notation of "No Flow" in the comment area of the form. The report shall be submitted to the Environmental Sciences Section at the address, cited above. .Should the permittee fail to monitor during a month in which toxicity monitoring is required, -monitoring will be . required during the following month. Should any test data from this monitoring requirement or tests performed by the North Carolina Division of Water Quality indicate 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; minimum control organism reproduction, and appropriate environmental controls, shall constitute an invalid test and will require immediate follow-up testing to be completed no later than the last day of the month following the month of the initial monitoring. Permit NCO023884 A. (6) AGGREGATE CALCULATION OF GRANTS CREEK AND TOWN CREEK TSS AND. BOD REMOVAL EFFICIENCY TSS wwrp Infl = (TSSGC Innfl x F1owGC) + (TSSTC Infl x F1owTc) FlowGc + FlowiC TSS wwTp Effl. _ (TSSGC Effl" x FlowGc) + (TSSTC Effl x Flow rc) FlowGc + F1owTc TSSxEMovAL [1 - (TSSwwrp Effl / TSSwwrp Infl)] x 100% Notes: "Effl" = Effluent "Infl" = Influent Grants Creek Treatment Train "TC" _,-Town Creek Treatment Train "WWTP" = Salisbury -Rowan WWTP A. (7.) DYE STUDY Upon reaching an average discharge flo* equal to 80% of the design flow of 12.5 MGD (approximately 10 - MGD), the city of Salisbury will be required to conduct dye studies under low flow and high flow river conditions to provide information regarding dilution into the Yadkin River (and to confirm the currently used CORMIX model). The city will submit a study plan to the. Division of Water Quality for review and approval prior to beginning the dye study. =Guidance fox planning the study can be -obtained from the EPA or DWQ's Intensive Survey Unit Standard Operating Procedure.- ' Permit NCO023884 A. (8.) EFFLUENT POLLUTANT SCAN " The permittee.shall thr perform ee EffluenrPollutant Scans for all parameters listed in the table below (in accordance with 40 CFR Part_136). The effluent pollutant scan samples shall represent seasonal (summer, winter, (all, spring) variations over the 3-year pern-lif cycle., Unless otherwise indicated, metals shall be analyzed as "total recoverable.'_ Additionally, the method detection level and the minimum level shall be the most sensitive as provided by the appropriate analytical procedure. - Ammonia (as N) - Trans-1,2-dictiloroethylene . Bis (2-chloroethyl) ether _ . Chlorine (total residual, TRC) � �-1.-JAichloroethylene, . Bis (2-chloroisopropyl) ether . u: Dissolved oxygen 1,2-dichloropropane . Bis (2-ethylhekyl) phthalate Nitrate/Nitrite 1,3-dichloropropylene 4-bromophenyl phenyl ether Kjeldahl nitrogen = Ethylbenzene = Butyl benzyl phthalate Oil and grease Methyl bromide . 27chloronaphthalene Phosphorus . - Methyl chloride 4-chlorophenyl phenyl ether Total dissolved solids Methylene chloride Chrysene Hardness 1,1,2,24etrachloroethane Dkn butyl phthalate . Antimony - Tetrachloroethylene Di=n-octyl.phthalate - - Arsenic - Toluene Dibenzo(a,h)anthracene ' '. Beryllium 1,1,14dchloroethane 1,2-diichlorobenzene -;Cadmium 1,1,2-trichloroethane 1,3=dichlorobenzene Chromium_ Tdchloroethylene 1,4-dichlorobenzene_ - Copper Vinyl chloride - 3,3-dichlorobenzidine Lead __ Acid-extractable:compounds: -Diethyl phthalate ' Mercury P-chloro-m-cresol Dimethyl phthalate _ Nickel : ' 2-chlorophenol 2,4=dinitrotoluene Selenium. = _ 2;4-dichlorophenol 2,6-dinitrotoluene Silver 2,4-dimethylphenol 1,2-diphenylhydrazine - Thallium 4,6-dinitro-o-cresol Fluoranthene Zinc - 2,4-dinitrophenol Fluorene 'Cyanide. 2-nitrophenol Hexachlorobenzene - Total phenolic compounds_ 4-nitrophenol Hexachlorobutadiene Volatile organic compounds:: Pentachlorophenol Hexachlorocyclo-pentadiene Acrolein Phenol ' Hexachloroethane "Acrylonitrile 2,4,6-tdchlorophenol --Indeno(1,2,3-cd)pyrene - Benzene Base -neutral compounds: Isophorone Bromoform. '. Acenaphthene Naphthalene _ Carbon tetrachloride Acenaphthylene Nitrobenzene Chloroberizene Anthracene N-nitrosodi-n-propylamine - Chlorodibromomethane Benzidine N-nitrosodimethylamine Chloroethane : Benzo(a)anthracene N-nitrosodiphenylamine 2=chloroethylvinyl ether Benzo(a)pyrene Phenanthrene Chloroform 3A benzofluoranthene Pyrene Dichlorobromomethane. Benzo(ghi)perylene 1,2,4-tdchlorobenzene 1,1-dichloroethane Benzo(k)fluoranthene :1,2-dichloroethane Bis (2-chloroethoxy) methane Test results shall be,reported to the Division in DWQ Form- DMR-PPA1 or in a form approved by the Director, within 90 days of sampling. -A copy of the report shall be submitted to Central Files at the following address: . '. Division of Water Quality,'Surface Water Protection Section, 1617 Mail Service Center, Raleigh, North Carolina 27699-1617. Facility Name: _ Salisbury —Rowan WWTP Receiving Stream: Yadkin River Permitted Flow (MGD): 12.5 MGD Subtiasin: 030704 Facility Class: IV Index No.: Facility Status: Existing Stream Class: W$-V Permit Status: Renewal 303(d) Listed: No County: Rowan Use Support: Regional Office: Mooresville Drainage Area (miz): 3,377 USGS Topo Quad: E17NW Summer 7010 (cfs) 735 cfs " Salisbury, NC Effective 7010 348 cfs (based on 18.9:1 dilution instream) Average Flow (cfs):. 4,879 IwC (°io): 5.28 Facility Name: Salisbury — Rowan WWTP Receiving Stream: Yadkin River Permitted Flow (MGD): 20.0 MGD subbasin: 030704 Facility Class:. IV Index No.: Facility Status: Existing Stream Class: W$-V Permit Status: Renewal 303(d) Listed: No County: Rowan Use Support: Regional Office: Mooresville Drainage Area (m12): 3,377 USGS Topo Quad: E17NW Summer 7010 (cfs) 735 cfs Salisbury, NC Effective 7010 736 cfs (based on 24.8:1 dilution instream) Average Flow (cfs): 4,879 IwC (0io): 4.04 Corrections "to the Factsheet , Per EPA comment the following paragraph should be corrected to include the last sentence: Salisbury has a full pre-treatment program, with 4 SIUs (Significant Industrial Users)" and 5 CIUs (Categorical Industrial Users) per its application. DWQ recommends that Salisbury continue to implement the full pretreatment program and its Long Term Monitoiring Plan through the renewed permitting cycle. Correction to the Permit --A-specialrequiring an annual effluent pollutant scan/priority pollutant analysis for. the City of Salisbury will be added to the final permit. This is an EPA requirement that must be fulfilled with the permit renewal application. Per 40 CFR 122.21` ■ 'The IWC for both wasteflows must be modified.. In January 2006, the City of Salisbury ran an updated CORMIX model. Teresa Rodriguez did .the NPDES review of the CORMIX model: It is attached as an appendix to the amended factsheet. Major changes included a revised 7Q10 flow of 735 cfs, which was. determined by ENSR at the requestof the City of Salisbury. Consultation with USGS indicated that while there is uncertainty determining 7Q10 flows in a lake,. "an estimated. 7Q10 for the Yadkin River between the South Yadkin River confluence and Grants Creek is a range of 750 —800 cfs. This range of estimates does not account for any backwater effects_ of High Rock Lake that may exist during low flow - periods." Although the flow estimate by ENSR is a little lower, NPDES will use the 735 cfs that ENSR generated and that Salisbury used in its CORMIX model run. The model run included revised stream flow information and a proposed modification to close two of the ports -on the existing three -port diffuser. The other variable included the critical condition now being the lake level of 5 feet below full pool for developing, toxic limits. Based on the results of the CORMIX model, the instream waste concentrations are 5.3 % at 12.5 MGD and 4% at 20 MGD. Effective 7Q10 values generated to determine the IWCs are 348 cfs at 12.5 MGD and 736 cfs at 20 MGD. (this is slightly above than the 7Q10 flow of 735 cfs used in the model). Salisbury Comments on the draft permit 1. Request that limitations/monitoring for selenium is dropped: The 35 ug/1 sample in 2004 is not representative of the Salisbury effluent and should not be considered in the analysis of effluent data. All other values are ,below detection. Recommend that it be monitored (quarterly) in the LTMP. DWQ response: The 35 ug/l.sample in May 2004 was reported in an amended DMR submitted by Salisbury in November 2004. Due to problems with instruments, metals and other parameters were not run in time to report on the correct DMR,. The data was reported as part of LTMP. The City did not report that sample was not representative at the time of its submittal. No information from . lab that indicated that sample was contaminated. Recommend that facility have delayed limit for selenium, with 18-month compliance schedule with monthly monitoring for selenium and limit will become effective eighteen months from effective date of the permit" If Salisbury submits a minimum of 12 data points and the data does not show reasonable potential 'to exceed the allowable. concentration then facility can request that DWQ reevaluate the data to determine if the selenium limit/monitoring in the NPDES permit -will be . dropped. Chronic selenium limits of 95 ug/1 and 124. ug/1 were given at 12. 5 MGD. and 20 MGD, respectively. The acute selenium value is based on selenite (+4) and may not be the most prevalent form. Therefore, after consultation with EPA, the chronic selenium limit was placed in the permit. NCO023884 Permit Factsheet Page 2 2. Request that monitoring for mercury is dropped: The hits (0.4 and 0.3 ug/1) in 2002 are not representative of the Salisbury. effluent. Recommend that it be monitored quarterly -in the LIMP. All other values are below detection. EPA response: An interim objection to the permit (rec'd 2/4/2005) due to RPA showing that Hg limit should be given but only Hg, monitoring was included. Also questioned that facility should be using EPA Method 1631 in its analysis:. After discussion of these issues in a January 27 2005 telecon, "EPA recommended that facility have a delayed mercury limit of 0.180 ug/1 with a 18 month compliance schedule, if collected data shows no RP, then limit/monitoring in the NPDES will be ."_ _dropped.. Need to. address the mercury.samphng method" and resolve Updated EPA response 12/1/2005 — re-evaluation of Hg data shows, that since the February 2002 hits, all Hg values (35 datapoints) have been below detection of 0.2 ug/l. EPA agrees that mercury limit may not be needed. EPA will . "concur with quarterly Hg monitoring in the pretreatment . program Long Term Monitoring Program, however Salisbury must use Method 1631. . DWQ response: Concurs with Hg monitoring in the LTMP. Updated DWQ response 01/2006 - with the revised IWCs based on the updated CORMIX model and "closing two ports on the three port diffuser, the new EPA method for Hg monitoring is not required for the Salisbury WWTP. IWCs are 5.3 % at 12.5 MGD and 4%.at 20 MGD. S CONTACT • DATE: NCO023884 Permit Factsheet " Page 3 The City of Salisbury submitted a technical report evaluating the dilution of the existing effluent," diffuser and proposed modifications to the diffuser. The first CORIVIIX model to determine the dilutiori-of the -diffuser was completed in-1995. The -data used in 1995 was different than the data - presented by Salisbury now. When the model was done in 1995 the design of the diffuser was not final and it was subsequently modified. The following table presents the data used in 1995 and 2006. Salisbury estimated new data for stream characteristics including 7Q10_flow and width of the `stream. Data used by the Division in 1995 Data used by Salisbury in 2005 Stream characteristics: Stream characteristics: s7Q101030cfs 29.2 m3/s s7Q10 735cfs 20.8 m3/s temp 25°C. .temp 250C Full Pool: Full Pool: width 490ft 149.4 m width 335ft _ 102A m channel average depth. 8ft 2.4 m channel average depth 10ft 3.0 m . 1/3 width 163ft 49.8 m 1/3 width 111.7ft 34.0 m, 5 ft from full pool: " 5 ft from full pool: width 330ft .100.E m width 295ft 89.9 m channel average depth 4ft 1.2 m channel average depth 5ft . 1.5 m 1/3 width 110ft 33.5 m 1/3 width 98.3ft 30.0m Diffuser: Diffuser: Full pool: Full pool: distance to left bank 138ft 42.1 m distance to left bank 140ft 42.7 m distance to right bank 161 ft 49.1 m distance to right bank 160ft 48.8 m 5' full pool: 5' full pool: distance to left bank 140ft 42.7m distance to left bank 125ft .. 38.1 m distance to right bank 167ft 50.9 m distance to right bank 145ft 44.2 m length 23ft 7.0m length 20ft 6.1 m # ports 3- # ports 3 Port diameter 1.16ft 0.35 m port diameter 1.16ft 0.35 m spacing between openings loft 3.0 m spacing between openings 10ft 3.0 m port height 2.5 ft 0.8 m port height 1 ft 0.3 m . ngles:angles: theta 45deg = theta Odeg gamma 90deg gamma 90deg beta 90 deg., beta 90deg sigma 0deg sigma Odeg Effluent characteristics: Effluent characteristics: flow 12.5 mgd 0.5 m3/s flow 12.5 mgd 0.5 m3/s density 1003 k /m3 density 998 k `lm3 1995 2006 Flow Lake level.... Concentration Flow Concentration MGD _ -.... - % .- Dilution MGD Lake level % Dilution 12.5 full pool 6.83 14.62 12.5. full pool - 9.52 10.5 12.5 5' belowfp 6.85. 14.6 12.5 5' .below fp 9.34 10.7 20 ` ` full pool 6.5 15.46. 20 full pool 8.92 11.2 20 5' below fp 9.3 10.73 20 5' below fp 6.80 14.7 Since the concentration in all cases is above 6 % Salisbury wants to modify the diffuser to obtain concentrations under 6% at the edge of the mixing zone. The mixing zone is established as a plume width of 1/3 of the channel width. Salisbury investigated two options: reducing the size of the ports to 8" and closing two ports, leaving one 14" port open. In both cases they obtained concentrations under 6 %. Salisbury. chose to close two ports on the existing diffuser. The dilution and waste concentration. given by the CORMIX model using one 14" port is as follows: Flow MGD Lake level Concentration % Dilution 12.5 full pool 2.56 39.0 12.5" 5' below full pool 5.28 18.9 20 - full pool 2.28 43.7 20 5' below full pool 4.04 24.8 Mr. Jeff Jones concluded that the dilution given by CORMIX for 12.5 MGD at 5' below full pool is not correct. CORMIX produces a prediction file that displays the information on plume properties by .. modules. Sometimes the program will use a correction factor on the plume width for computation purposes: A message is displayed in the prediction file explaining the use of this correction factor. They interpreted this correction factor as a correction to be done, also on the dilution. As the correction factor is only applied to the plume width it is incorrect to apply it to the pollutant concentration. The report does say that the dilution values should be acceptable. The pollutant concentration of 5.28 % for the configuration of one port at 12.5 mgd should be acceptable as given in the CORMIX session report. At Sa/is,64riry�Plwan August 11, 2006 Ms. Jackie Nowell Division of Water Quality NPDES Unit 1617 Mail Service Center Raleigh, North Carolina 27699 - 1617 RE: Modifications to Salisbury -Rowan WWTP Yadkin River Diffuser Dear Ms. Nowell: On May 17, 2006 the City of Salisbury completed modification of the Yadkin River Diffuser as outlined in the technical report, "Salisbury -Rowan WWTP Yadkin River Diffuser CORMIX Analysis". Alternative 2 in the report consisted of closing two 14-inch outlets on each diffuser line with blind flanges, which leaves a single 14-inch outlet on each diffuser line. CORMIX modeling predicts an Instream Waste Concentration of 5.3% at the regulatory mixing zone boundary with this modified configuration for a discharger flow of 12.5 MGD. If you have further questions, please feel free to contact me at (704) 638-2146 or i j one@salisburync.gov Sincerely, Jeffrey B. Jones, P.E. Senior Engineer �D. j AUG 1 5 2006 i DENR - WATER QUALITY POINT SOURCE BRANCH 1 Water Street Telephone (704) 638-5205 Salisbury, NC 28144 Salisbury -Rowan Utilities Fax (704) 638-8470 J�'JED srl,s UNITED STATES ENVIRONMENTAL PROTECTION AGENCY �m yW REGION 4 o Q A TLANTA FEDERAL CENTER 61 FORSYTH STREET Z�+lq< PROAe to ATLANTA 1GEORGIA 0303-8960 AUG , a zoo Ms. Jackie Nowell North Carolina Department of Environment and Natural Resources Division of Water Quality NPDES Unit 1617 Mail Service Center Raleigh, NC 27699-1617 SUBJ: Draft NPDES Permit Salisbury -Rowan WWTP - NPDES No. NCO023884 Dear Ms. Nowell: _ ;ILIA 2006 DENR WATER QUALITY POINT SOURCENCH In accordance with the EPA/NCDENR MOA, we have completed review of the draft permit referenced above. Contingent on the permit containing a requirement to conduct a dye study during both high and low flow conditions during this next permit term, we have no comments. We request that we be afforded an additional review opportunity only if significant changes are made to the draft permit prior to issuance, or if significant comments objecting to the draft permit are received. Otherwise, please send us one copy of the final permit when issued. Based on the above, EPA's May 3, 2006 interim objection is withdrawn. If you have any questions, please call me at (404) 562-9304. Sincerely, : V�4� Marshall Hyatt, Environmental Scientist Permits, Grants, and Technical Assistance Branch Water Management Division Intemet Address (URL) • http://www.epa.gov Recycled/Recyclable • Primed with Vegetable Oil Based Inks on Recycled Paper (Minimum 30 % Postconsumer) Dear WNO*q: River bfuser as,. �Ofbjindt h sin,� -J. inc, the h' " J I Hari . . h lanpes�,w Tc...,�Abaveg�ja gji�line, If you have or- questiops,,P f fr ee, r' 'I. e at (70-41638�;21 "eq pry, .,54�6.qr N :`28 144, Sa,llsbqiy-Rbwiin Ut,11000 FAi '(704,)'635-8OQ Permit No Subject: Permit No From: Jackie Nowell <jackie.nowell@ncmail.net> Date: Wed, 09 Aug 2006 11:55:11 -0400 To: Teresa Rodriguez <Teresa. Rodrigu ez@ncmail. net> CC: Susan Wilson <susan.a.wilson@ncmail.net> *Just talked to Jeff Jones of Salisbury, they are in agreement to do the dye studies. They are current averaging about 6.5 MGD and they don't anticipate getting to 10 MGD during this permit cycle. Here is a draft of the condition that will be added to the permit. I'm thinking of forwarding it down to Marshall to see if it says what they need. * A. (7.) DYE STUDY* Upon reaching an average discharge flow equal to 80% of the design flow of 12.5 MGD (approximately 10 MGD),4he City of Salisbury will be required to conduct dye studies under low flow and high flow river conditions to provide information regarding dilution into the Yadkin River C (4060 7-6 (anl 2 �l C.ccaaZNrL-'( tits OtO (DAAAO - 4to,2u_ AT- ' ti{ 4(4t(Z!L DES ( g N "Lt-o U1 Content -Type: application/octet-stream 23884 finalpermit2006 Content -Encoding: base64 1 of 1 8/9/2006 12:14 Ply ice: 6ansnury Subject: Re: Salisbury From: Hyatt.Marshall@epamail.epa.gov Date: Tue, 01 Aug 2006 14:24:27 -0400 To: Susan Wilson <susan.a.wilson@ncmail.net> CC: Jackie Nowell <Tackie.Nowell@ncmail.net>, Teresa Rodriguez <Teresa.Rodriguez@ncmail.net> I forwarded your email to Tim and then talked to him. If NC includes a requirement to conduct a dye study during the term of the permit at a higher river flow (and maybe a lowflow condition as well), that is sufficient for us. If you do that, Tim doesn't need to discuss CORMIX temp and conductivitydensity assumptions. 1 of 1 8/1/2006 2:56 PM �a uu i vuauw � a a.� Subject: Draft Permits (12) From: John Giorgino <johrLgiorgino@ncmail.net> Date: Mon, 22 May 2006 14:40:18 -0400 To: Jackie Nowell <Jackie.Nowell@ncmail.net> Jackie, I have reviewed the following permits (I am late getting back to you on some of them, but did not have any comments). Thanks for forwarding them. NCO025321 N00021962 NCO074705 NCO023884 NC0005177 NC0000361 NC0000400 NCO084620 NCO085839 NC0000353 NC0000175 NCO060534 John Giorgino Environmental Biologist North Carolina Division of Water Quality Environmental Sciences Section Aquatic Toxicology Unit Mailing Address: 1621 MSC Raleigh, NC 27699-1621 Office: 919 733-2136 Fax: 919 733-9959 "The real work of men was hunting meat. The invention of agriculture was a giant step in the wrong direction, leading to serfdom, cities, and empire. From a race of hunters, artists, warriors, and tamers of horses, we degraded ourselves to what we are now: clerks, functionaries, laborers, entertainers, processors of information." - Edward Abbey 1 nf 1 51990 06 1.0R PM ' 4q16(, AOL mom — Kruger ,qw Xj C �� 2-6 v fy ) 7'4L Fw: Yadkin River Subject: Fw: Yadkin River From: Hyatt.Marshall@epamail.epa.gov Date: Wed, 03 May 2006 13:03:29 -0400 To: jackie.nowell@ncmail.net, teresa.rodriguez@ncmail.net ----- Forwarded by Marshall Hyatt/R4/USEPA/US on 05/03/2006 01:02 PM Tim Wool/R4/USEPA/US To 05/03/2006 11:26 Marshall Hyatt/R4/USEPA/US@EPA AM cc Subject Yadkin River The CORMIX model was developed to look at dilution zones in advectively driven systems, where water velocity and densities are relatively the same top to the bottom. The application of CORMIX to the Yadkin River close to the reservoir does not meet the model assumptions. There needs to be an analysis conducted to show that the assumptions that are used to drive the CORMIX application yield results that are close to reality. A representative dye study or analysis of previously collected water quality data should be done to prove that CORMIX is an adequate tool for developing and protecting the mixing zone. -------------------------------------------------- -------------------------------------------------- Tim Wool Standards, Monitoring and TMDL Branch US EPA Region 4 Atlanta, Georgia 404.562.9260 wool.tim@epa.gov TMDL Tools: www.epa.gov/athens/wwqtsc 1 of 1 5/8/2006 10:36 AM [Fwd: Re: re CORMIX for Salisbury] Subject: [Fwd: Re: re CORMIX for Salisbury] From: Jackie Nowell <jackie.nowell@ncmail.net> Date: Fri, 28 Apr 2006 15:10:42 -0400 To: Teresa Rodriguez <Teresa.Rodriguez@ncmail.net> FYI. This is the EPA modeler's concern. Subject: Re: re CORMIX for Salisbury From: Hyatt.Marshall@epamail.epa.gov Date: Fri, 28 Apr 2006 15:08:30 -0400 To: Jackie Nowell <jackie.nowell@ncmail.net> the modeler hasn't told me much and hasn't had a lot of time to look. But what he has mentioned is because the discharge pipe design is just a single port, based on the 20 MGD flow, the exit velocity is huge - like 20 m/sec. Content -Type: message/rfc822 Re: re CORMIX for Salisbury;; Content -Encoding: 7bit 1 of 1 5/1/2006 10:12 AM 640 635 630 $ 625 W 620 615 610 0 Cross Section 17 (Looking Downstream) 16.72 Mile Upstream Of High Rock Dam 500 1000 1500 2000 Distance (ft) 2500 3000 3500 HAYadkin\Yadkin-Ras\xsec data L-t-R3.xls\Cht17 12/15/2005 ,y� "�--����e��� +�i�..•� � ice' � S` � yam.++ � �• w . r '�"� . �;M• - y . 1'Y ��w . ! 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Subject: comments on revised draft permit for NCOO23884 - Salisbury -Rowan WWTP From: Hyatt.Marshall@epamail.epa.gov Date: Wed, 05 Apr 2006 16:41:29 -0400 To: jackie.nowell@ncmail.net CC: Belk.Elizabeth@epamail.epa.gov 1. Footnote 1 in A.1 is not repeated as Footnote 1 in A.2. Thus, as drafted, A.6 only applies to the 12.5 MGD discharge and not to the 20 MGD discharge. Is that what you meant? If so, why the difference? 2. In A.6, the title refers to both BOD and TSS, but only TSS % removal calculations are shown. Shouldn't BOD % removal calculations be -shown? Or that it indicate BOD % removal should be calculated substituting for TSS? 3. I was curious to see from the CORMIX modeling that the RWC/IWC was lower at the higher discharge flow. That is not a typical result. Some modelers here conferred when I brought this up. They said that is possible, but that the model assumptions for the difference in temp and density between the effluent and the lake ought to be checked to ensure they are realistic. Because not all of that data are included in Teresa's 2/16/06 memo to you, is that possible to look into? If not, should some type of instream monitoring to confirm the model results be conducted when the discharge expands to 20 MGD - possibly a dye study? 1 of 1 4/13/2006 5:00 PM Salisbury Post AFFIDAVIT OF PUBLICATION NC DEPT OF ENVIROMENT--LEGAL & NATURAL RESOURCES ****************************** NORTH CAROLINA ROWAN COUNTY Before the undersigned a Notary Public of said County and State, duly commisioned, qualified, and authorized by law to administer oaths, personally appeared WINFRED MENTION, who being first duly sworn, deposes and says that he is ASSISTANT ADVERTISING DIRECTOR of the SALISBURY POST, published, issued and entered as second class mail in the City of Salisbury, in said County and State, that he is authorized to make this affidavit and sworn statement,that the notice or other legal advertisement a true copy of which is attached hereto, was published in the SALISBURY POST , on the following dates: 04/02/2006 and that the said newspaper in which such notice, paper documnet or legal advertisement was published, at the time of each and every such publication, a newspaper meeting all the requirements and qualifications of Section I-597 of the General Statutes of North Carolina and was a qualified newspaper within the meaning of Section I-597 of the General Statutes of North Carolina. NO. 53548 PUBLIC NOTICE $81.45 41 ^ i * Sworn and subscribed before me This loth day of April, 2006 NOTARY PUBLIC My Commision Expires ` POST PUBLISHING COMPANY AD INSERTION ORDER (CONTINUED) Salesperson: Legals Printed at 04/10/06 14:29 Acct#: 3227 No.53548 PUBLIC NOTICE State of North Carolina ENVIRONMENTAL MANAGEMENT COMMISSION/NPDES UNIT 1617 Mail Service Center, Raleigh, NC 27699-1617 Notification of Intent to Issue a NPDES Wastewater Permit On the basis of thorough staff review and application of NC General Statue 143.21, Public law 92-500 and other lawful standards and regulations, the North Carolina Environmental Management Commission proposes to issue a National Pollutant Discharge Elimination System (NPDES) wastewater discharge permit to the person(s) listed below effective 45 days from the publish date of this notice. Written comments regarding the proposed permit will be accepted until 30 days after the publish date of this notice. All comments received prior to that date are considered in the final determinations regarding the proposed permit. The Director of the NC Division of Water Quality may decide to hold a public meeting for the proposed permit should the Division receive a significant degree of public interest. Copies of the draft permit and other supporting infor- mation on file used to determine conditions present in the draft permit are available upon request and payment of the costs of reproduction. Mail comments and/or requests for information to the NC Division of Water Quality at the above address or call the Point Source Branch at (919)733-5083, extension 520 or 363. Please include the NPDES permit number (at- tached) in any communication. Interested persons may also visit the Division of Water Quality at 512 N. Salisbury Street, Raleigh, NC 27604-1148 between the hours of 8:00 a.m. and 5:00 p.m. to review infor- mation on file. NPDES Permit Number NC0023884, City of Salis- bury (Salisbury -Rowan WWTP) has applied for a permit renewal for a facility located in Rowan County discharging treated wastewater into the Yadkin River in the Yadkin River Basin. Currently BOD5, ammo- nia, dissolved oxygen, fecal coliform and total residu- al chlorine are water quality limited. This discharge may affect future allocations in this portion of the re- ceiving stream. Ad#: 46865 Status: E Sa/isbaryRdw7'1an Mr. Bob Smet Environmental & Natural Resources Manager APGI Yadkin Division Post Office Box 576 Badin, NC 28009-0576 April 19, 2006 Subject: Notice of Improvements to Salisbury's Diffuser Dear Bob: The City of Salisbury provides this notice to APGI Yadkin Division (Alcoa) pursuant to the provisions of the diffuser easement between Yadkin, Inc. and the City of Salisbury (deed dated December 4, 1997, and recorded at Rowan County Register of Deeds Book 812 Page 912). This notice is being provided more than 24 hours in advance of work on the diffuser, consistent with paragraph (h) of the deed. Salisbury -Rowan Utilities (SRU) has arranged for the installation of fittings on the diffuser pipes. We will notify you once a project date has been determined, and the schedule may vary depending upon weather conditions. If you have any questions, please feel free to give me a call. Sincerely, Matt Bernhardt Assistant City Manager for Utilities City of Salisbury Salisbury -Rowan Utilities cc: Mr. Dave Goodrich, Division of Water Quality Mr. David W. Treme, City of Salisbury Mr. Don Garbrick, J.N. Pease & Associates Mr. V. Randall Tinsley, Brooks, Pierce, McLendon, Humphrey & Leonard, L.L.P. file I Water Street Telephone (704) 638-5205 Salisbury, NC 28144 Salisbury -Rowan Utilities Fax (704) 638-8470 I Stpte;'of North Carolina Dt?pa�irtment of Environment arf,,' Mtural Resources Division of Water Quality Michael F. Easley, Governor William G. Ross, Jr., Secretary Alan W. Klimek, P.E., Director March 29, 2006 MEMORANDUM To: Britt Setzer NC DENR / DEH / Regional Engineer Mooresville Regional Office From: Jackie Nowell Point Source Branch Subject: Review of Draft NPDES Permit NCO023884 Salisbury -Rowan WWTP Rowan County 16TF.1W,A IT 0 0 NCDENR NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES MAR r-9.2 0 Public R 7'. /C1V d Please indicate below your agency's position or viewpoint on the draft permit and return this form by April 29, 2006. If you have any questions on the draft permit, please contact me at the telephone number or e-mail address listed at the bottom of this page. �/f ,�/ 6 G s . w/ 010c-e- I , RESPONSE: (Check one) 6. +,-— j Ira, 4e - & ft- • , 4L ^ d ; , �t J¢% S e iie•✓ p res2 - 2C) XW 6 p I✓L. -r f, �a q�ys r llw � ap 1,s,4� Concur with the issuance of this permit provided the facility is operated and maintained properly, the stated effluent limits are met prior to discharge, and the discharge does not contravene the designated water quality standards. F�Concurs with issuance of the above permit, provided the following conditions are met:d M ❑ Opposes the issuance of the above permit, based on reasons stated below, or attached: 0, 1617 Mail Service Center, Raleigh, North Carolina 27699-1617 919 733-5083, extension 363 (fax) 919 733-0719 VISIT US ON THE INTERNET @ http://h2o.enr.state.nc.us/NPDES Carolyn.bryant@ncmai1.net Salisbury WWTP at 12.5 MGD * updated effective 7Q10- Residual Chlorine 7Q10 (CFS) 348 DESIGN FLOW (MGD) 12.5 DESIGN FLOW (CFS) 19.375 STREAM STD (UG/L) 17.0 UPS BACKGROUND. LEVEL (1 0 IWC (%) 5.27 Allowable Concentration (ugj 322.34 Ammonia as NH3 (summer) 7Q10 (CFS) 348 DESIGN FLOW (MGD) 12.5 DESIGN FLOW (CFS) 19.375 STREAM STD (MG/L) 1.0 UPS BACKGROUND LEVEL 0.22 IWC (%) 5.27 Allowable Concentration (m 15.01 Ammonia as NH3 (winter) 7Q10 (CFS) '48 Fecal Limit 2001100ml DESIGN FLOW (MGD) 12.5 Ratio of 18.0 :1 DESIGN FLOW (CFS) 19.375 STREAM STD (MG/L) 1.8 UPS BACKGROUND LEVEL 0.22 IWC (%) 5.27 Allowable Concentration (m 30.18 3/14/2006 Salisbury WWTP at 20.0 MGD * updated effective 7010 Residual Chlorine Ammonia as NIi3 (summer) 7Q10 (CFS) 736 7010 (CFS) 736 DESIGN FLOW (MGD) 20. DESIGN FLOW (MGD) 20 DESIGN FLOW (CFS) 31 DESIGN FLOW (CFS) 31 STREAM STD (UG/L) 17.0 STREAM STD (MG/L) 1.0 UPS BACKGROUND LEVEL (1 0 UPS BACKGROUND LEVEL 0.22 IWC (%) 4.04 IWC (%) 4.04 Allowable Concentration (ugj 420.61 Allowable Concentration (m 19.52 Ammonia as NIi3 (winter) 7Q10 (CFS) Fecal Limit 200/100ml DESIGN FLOW (MGD) 20 Ratio of 23.7 :1 DESIGN FLOW (CFS) 31 STREAM STD (MG/L) 1.8 UPS BACKGROUND LEVEL 0.22 IWC (%) 8.18 Allowable Concentration (m 19.54 3/14/2006 ' REASONABLE POTENTIAL ANALYSIS Salisbury - Rowan WWTP NCO023884 Time Period 1/2002-9/2005 Qw (MGD) 12.5 WWTP Class IV 7010S (cfs) 348 IWC (%) @ 7Q10S 5.2739 7Q10W (cfs) 0 @ 7Q10W N/A 30Q2 (cfs) 0 @ 30Q2 N/A Avg. Stream Flow, QA (cfs) 4879 @ QA 0.3955 Rec'ving Stream Yadkin River Stream Class WS-V. Outfal 1001 Qw = 12.5 MGD STANDARDS & PARAMETER TYPE CRITERIA (2) POL Units REASONABLE POTENTIAL RESULTS RECOMMENDED ACTION (1) NCWQS/ %FAV/ n NDet. MaxPredCw AllowableCw Chronic Acute Acute: N/A Arsenic NC 50 ug/L 12 0 9.2 -------------------------------------------- Chronic: 948 No action all values belowadetection Acute: 15 Cadmium NC 2 15 ug/L 15 1 5.4 _ _ _ Chronic: _ _ 38 _ No action 14 of 15 values:below detection Acute: 1,022 Chromium NC 50 1,022 ug/L 12 4 309.7 _ _ Chronic: _ _ 948 _ _ _ No action no exceedance of allowable conc Acute: 7 Continue monrtopng reduce to ilmonth due to good tox " Copper NC 7 AL 7.3 ug/L 55 11 79.0 _ _ _ _ results Chronic: 133 k Acute: 22 Drop quarterly monitoring ;; Cyanide NC 5 N 22 10 ug/L 34 1 13.9 _ _ _ _ _ _ Chronic: 95 S Acute: 34 No action, no exceedance of allowable conc Lead NC 25 N 33.8 ug/L 15 2 24.1 _ _ _ _ _ Chronic: 474 Acute: N/A Monthly monitoring recommended based on 35°non detects Mercury NC 0.012 0.0002 ug/L 43 2 0.7304 be' since the Feb 2002 hds � OId Hg monitoring me►hod can_ _ _ _ Chronic: _ _ 0.23 used'because'Md<6/ ' Acute: 261 No.•action noezceedance=of allowable conc Nickel NC 88 261 ug/L 16 1 11.9 _ _ _ _ _ _ Chronic: 1,669 t Acute: 56 AddAaily max limit based on chronic`allowable,'due to dilufic Selenium NC 5.0 56 ug/L 17 2 273,5 Max-pred exceeds allowable conE_Oelayed limit m 18 mon _ _ Chronic: _ _ 95 for facilityto hndsource of`Se Will monitor monthly before delayed limit is',effec6ve. n • Acute: 1 Continue monitorng reduce to 1/month due Ao,good tox Silver NC 0.06 AL 1.23 ug/L 57 3 10.8 _ _ _ _ results _ _ s ; Chronic: 1 Acute: 67 Continue monitoring e reduce to11 1/month due to, good tox Zinc NC 50 AL 67 ug/L 17 13 181.1 _ _ results _ _ _ __ Chronic: 948 �3 Legend. " Freshwater Discharge C = Carcinogenic NC = Non -carcinogenic A =, Aesthetic 23884.rpa12.5mgd.updt012006, rpa 3/14/2006 + l REASONABLE POTENTIAL ANALYSIS Salisbury -Rowan WWTP NCO023884 Time Period 1/2002-9/2005 Qw (MGD) 20 WWTP Class 1V 7Q 10S (cis) 736 1WC (%) @ 7010S 4.0417 701OW (cfs) , 0 @ 7Q 10W N/A 3002 (cfs) 0 @ 3002 N/A Avg. Stream Flow, QA (cfs) 4879 @ QA 0.6314 Rec'ving Stream Yadkin River Stream Class WS-V Outfall 001 Qw = 20 MGD STANDARDS & PARAMETER TYPE CRITERIA (2) PQL Units REASONABLE POTENTIAL RESULTS RECOMMENDED ACTION (1) NCWQS/ %FAV/ n #Det MaxPredCw AllawahleCw Chronic Acute Acute: N/A Arsenic NC 50 ug/L 12 0 9.2 _ _ _ Chronic: _ _ 1,237 _ No action all values below detell ction \t' Acute: 15 Cadmium NC 2 15 ug/L 15 1 5.4 ------------ Chronic: 49 Nd action 14 of 15 values below deter tion Acute: 1,022 Chromium NC 50 1,022 ug/L 12 4 309.7 Chronic: _ _ 1,237 _ _�'' No action no exceedance of allowable, cone Acute: 7 Contln'ue monitoring retluc'eto 1/month due to good tox:'< Copper NC 7 AL 7.3 ug/L 55 11 79.0 _ _ _ _ results _ Chronic: 173 Acute: 22 Drop,quarterlymonitoring , Cyanide - NC 5 N 22 10 ug/L 34 1 13.9 Chronic: 124 _ _ '> � v Acute: 34 No action no exceetlance of aflowabl,e cone Lead NC 25 N 33.8 ug/L 15 2 24.1 _ _ _ _ Chronic: 619 Acute: N/A Monthly monitoring recommended based on 35 non detects Mercury NC 0.012 0.0002 ug/L 43 2 0.7304 _ _-_ _ sm_ce the Feb:2g02 hds O�d Hg monitonng;metfiod ca_n be Chronic: 0.30 used because IWC < 6/ . x' _ r= YF Acute: 261 N&action no-exceedance of allowable cone ?' Nickel NC 88 261 ug/L 16 1 11.9 _ _ Chronic: _ _ 2,177 _ Acute: 56 Add daily max limit based -on chronic allowable due to dllutic Selenium NC 5.0 56 ug/L 17 2 273.5 Max•pred. exceeds allowable conoXelayed,limit in 18>mon _ _ Chronic: _ _ 124 for facility to findsource'of Se Wilt monifor monthly before decayed limitis`effectwe . , Acute: 1 Contirue monitoring reiiuce to 1/month due to good t , ' Silver 0.06 AL 1:23 ug/L 57 3 10.8 _ _ _ _ a results ,____Chronic: kNC 1 Acute: 67 Continue monitoring reduce to-1/month due"to;godtZinc 50 AL 67 ug/L 17 13 181.1 _ _ _ _ results _ Chronic: 1,237 Legend.' " Freshwater Discharge C = Carcinogenic NC = Non -carcinogenic A = Aesthetic 23884.rpa20mgd.updt2012006, rpa 3/14/2006 w r� z0 Afw �-,2e% /8, 9 Y / y, 375- c INC i �17 dY, S 0, 1117rol -/-( . o, o ZSro • 79105 J = / x 3.9 ,?-O ,4jcc-e = 3/ Cd �e3, 7 V -=� ,? Z 8 % O, d 2f6.7?i0 f = /9, j? , o, Y r6/ 7°s = 737 c--4 2,0 A 6,d e G, J Z Z 9 -3/ 3/t79��1 O, 7UG E? f- d,OLt879 1a = 3� J,- 30. Z9 7y�,61 " 13Z 8'O` UJ ZJ?Y c � 31-7.76 o, a �d y = 3/ c4 3/c 9to 3/ v'!v — f • %y7 w7-11717 0 f V e !iU !c, 3e, -t 7Q�>' 19,3,'cif 4! jl?cb �os a� 79lJf : le CO, 0 5-2 e D! vf`v = 3IG6 3/ t 79,( of p, a �� ��31 t �9�u o/ oya y ;1j7wj 2 9, 79L7 7,jc,,- TEE,,7L 41('00 Z3 gVy To: Jackie Nowell From: Teresa Rodriguez Date: February 16, 2006 Subject: Review of Salisbury CORMIX analysis 2oo6 rem"/ The City of Salisbury submitted a technical report evaluating the dilution of the existing effluent diffuser and proposed modifications to the diffuser. The first CORMIX model to determine the dilution of the diffuser was completed in 1995. The data used in 1995 was different than the data presented by Salisbury now. When the model was done in 1995 the design of the diffuser was not final and it was subsequently modified. The following table presents the data used in 1995 and 2006. Salisbury estimated new data for stream characteristics including'7Q10 flow and width of the stream. Data used by the Division in 1995 Data used by Salisbury in 2005 Stream characteristics: Stream characteristics: s7Q101030 cfs 29.2 m3/s s7010 735 cfs 20.8 m3/s temp 25°C temp 25°C Full Pool: Full Pool: width 490ft 149.4m width 335ft 102.1 m channel average depth 8ft 2.4 m channel average depth loft 3.0 m 1/3 width 163ft 49.8m 1/3 width 111.7ft 34.0m ft from full pool: 5 ft from full pool: �-5 width 330ft 100.E m width 295ft 89.9 m channel average depth 4ft 1.2 m channel average depth 5ft 1.5 m 1/3 width 1 loft 33.5 m 1/3 width 98.3 ft 30.0 m _ Diffuser: Diffuser: Full pool: Full pool: distance to left bank 138ft 42.1 m distance to left bank 140ft 42.7 m distance to right bank 161 ft 49.1 m distance to right bank 160ft 48.8 m -5' full pool: 5' full pool: distance to left bank 140ft 42.7 m distance to left bank 125ft 38.1 m distance to right bank 167ft 50.9m distance to right bank 145ft 44.2 m length 23ft 7.0m length 20ft 6.1 m # ports 3 # ports 3 Port diameter 1.16ft 0.35m port diameter 1.16ft 0.35m spacing between openings loft 3.0m spacing between openings loft 3.0m port height 2.5ft 0.8 m port height 1 ft 0.3 m angles:angles: theta 45 deg theta 0 deg gamma 90 deg gamma 90 deg beta 90 deg beta 90 deg sigma 0 deg sigma 0 deg Effluent characteristics: Effluent characteristics: flow 12.5 mgd 0.5 m3/s flow 12.5 mgd 0.5 m3/s density1003 k /m3 densit 998 k /m3 The results obtained by the Division in 1995 and results obtained now by Salisbury are shown on the following table: 1995 2006 Flow Concentration Flow Concentration MGD Lake level % Dilution MGD Lake level % Dilution 12.5 full pool 6.83 14.62 12.5 full pool 9.52 10.5 12.5 5' below fp 6.85 14.6 12.5 5' below fp 9.34 10.7 20 full pool 6.5 15.46 20 full pool 8.92 11.2 20 5' below fp 9.3 10.73 20 5' below fp 6.80 14.7 Since the concentration in all cases is above 6 % Salisbury wants to modify the diffuser to obtain concentrations under 6% at the edge of the mixing zone. The mixing zone is established as a plume width of 1/3 of the channel .width. Salisbury investigated two options: reducing the size of the ports to 8" and closing two ports, leaving one 14" port open. In both cases they obtained concentrations under 6 %. Salisbury chose to close two ports on the existing diffuser. The dilution and waste concentration given by the CORMIX model using one 14" port is as follows: Flow MGD Lake level Concentration % Dilution 12.5 full pool 2.56 39.0 12.5 5' below full pool 5.28 18.9 20 full pool 2.28 43.7 20 5' below full pool 4.04 24.8 11 Mr. Jeff Jones concluded that the dilution given by CORMIX for 12.5 MGD at 5' below full pool is not correct. CORMIX produces a prediction file that displays the information on plume properties by modules. Sometimes the program will use a correction factor on the plume width for computation purposes. A message is displayed in the prediction file explaining the use of this correction factor. They interpreted this correction factor as a correction to be done also on the dilution. As the correction factor is only applied to the plume width it is incorrect to apply it to the pollutant concentration. The report does say that the dilution values should be acceptable. The pollutant concentration of 5.28 % for the configuration of one port at 12.5 mgd should be acceptable as given in the CORMIX session report. i Salisbury CORMIX Model Data used in 1995 Stream characteristics: s7010 1030 cfs 29.2 m3/s temp 25 °C Full Pool width 490 ft 149.4 m channel average depth 8 ft 2.4 m 1 /3 width 163 ft 49.8 m -5 ft from full pool water elevation 330 ft 100.6 m channel average depth 4 ft 1.2 m 1 /3 width 110 ft 33.5 m Diffuser: length 23 ft 7.0 m # ports 3 port diameter 1.16 ft 0.35 m spacing between openings 10 ft 3.0 m angles: theta 45 deg gamma 90 deg beta 90 deg sigma 0 deg port height 2.5 ft 0.8 m full pool: distance to left bank 138 ft 42.1 m distance to right bank 161 ft 49.1 m -5' full pool: distance to left bank ft 0.0 m distance to right bank ft 0.0 m Effluent characteristics: flow 12.5 mgd 0.5 m3/s density 1003 k /m3 Udld OdIJUUI Y GVVO Stream characteristics: s7Q10 735 cfs 20.8 m3/s temp 25 °C Full Pool width 335 ft 102.1 m channel average depth 10 ft 3.0 m 1 /3 width 111.7 ft 34.0 m -5 ft from full pool width 295 ft 89.9 m channel average depth 5 ft 1.5 m 1 /3 width 98.3 ft 30.0 m Diffuser: length 20 ft 6.1 m # ports 3 port diameter 1.16 ft 0.35 m spacing between openings 10 ft 3.0 m angles: theta 0 deg gamma 90 deg beta 90 deg sigma 0 deg port height 1 ft 0.3 m full pool: distance to left bank 140 ft 42.7 m distance to right bank 160 ft 48.8 m -5' full pool: distance to left bank 125 ft 38.1 m distance to right bank 145 ft 44.2 m Effluent characteristics: flow 12.5 mgd 0.5 m3/s density 998 k /m3 -ao rn5d 0.2-4 mj/S ?; Salisbury CORMIX Model Data used in 1995 Stream characteristics: s7Q10 1030 cfs 29.2 m3/s temp 25 °C Full Pool width 490 ft 149.4 m channel average depth 8 ft 2.4 m 1 /3 width 163 ft 49.8 m -5 ft from full pool water elevation 330 ft 100.6 m channel average depth 4 ft 1.2 m 1 /3 width 110 ft 33.5 m Diffuser: length 23 ft 7.0 m # ports 3 port diameter 1.16 ft 0.35 m spacing between openings 10 ft 3.0 m angles: theta 45 deg gamma 90 deg beta 90 deg sigma 0 deg port height 2.5 ft 0.8 m distance to left bank 138 ft 42.1 m distance to right bank 161 ft 49.1 m Effluent characteristics: flow 12.5 mgd 0.5 m3/s temp °C Data 2005 Stream characteristics: s7Q10 833 cfs 23.6 m3/s temp 25 °C Full Pool width 335 ft 102.1 m channel average depth 10 ft 3.0 m 1 /3 width 102.1 ft 31.1 m -5 ft from full pool , water elevation ft 0.0 m channel average depth ft 0.0 m 1 /3 width 0.0 ft 0.0 m Diffuser: length 21.3 ft 6.5 m # ports 3 port diameter 1.16 ft 0.35 m spacing between openings 10 ft 3.0 m angles: theta 0 deg gamma 91 deg beta 90 deg sigma 0 deg port height 0.9 ft 0.3 m distance to left bank 140 ft 42.7 m distance to right bank 100 ft 30.5 m Effluent characteristics: flow 12.5 mgd 0.5 m3/s temp °C bOAK JI I n i ' I 1 �v �^' o _ I I I ' � I I I I I _ i -- - - - -- - -i _ 1 I I - I _ _L__ I i i i i I I i _ r -- , Y2 J I '; _ \ i _i i I I I � �� L- --- - -- � ' - � �`r'�+.,,� i - -- I - I --I----. I - I i --f _- I _.. _ - � ---- - -- - I' I 1.- - •_ - ' I 1 I` - -- - i I I I I I r t I I I I _ I I-i -- -.. _ . _ - - - - - j _ _ - - - --- 1 i _j- --J I I I I Ili A. - c -- 1 � Appendix 10 Alternate 2 Configuration 5lIe Por� IMF" 12.5 MGD Effluent Discharge High Rock Lake Full Pond Q CORMIX SESSION REPORT: XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX CORMIX MIXING ZONE EXPERT SYSTEM CORMIX-GI Version 4.3GT HYDR01:Version-4.3.0.2 June,2005 SITE NAME/LABEL: SRU Yadkin River Diffuser DESIGN CASE: Alt 2-12.5 MGD-Full Pond FILE NAME: C:\Program Files\CORMIX-GI \3\MyFiles\SRU Diffuser.prd Using subsystem CORMIXI: Submerged Single Port Discharged Start of session: 01/16/2006--12:48:38 SUMMARY OF INPUT DATA: ---------------------- AMBIENT PARAMETERS: Cross-section = bounded Width BS = 102.11 m Channel regularity ICHREG = 1 Ambient flowrate QA = 20.81 m^3/s Average depth HA = 3.05 m , Depth at discharge HD = 3.05 m. Ambient velocity UA = 0.0669 m/s Darcy-Weisbach friction factor F = 0.0487 Calculated from Manning's n = 0.03 Wind velocity UW = 2 m/s Stratification Type STRCND = U Surface temperature = 25 degC Bottom temperature = 25 degC Calculated FRESH -WATER DENSITY values: Surface density Bottom density ---------------------------------- DISCHARGE PARAMETERS: Nearest bank Distance to bank Port diameter Port cross -sectional area Discharge velocity Discharge flowrate Discharge port height Vertical discharge angle Horizontal discharge angle Discharge density Density difference Buoyant acceleration Discharge concentration Surface heat exchange coeff Coefficient of decay ----------------------------- RHOAS = 997.0456 kg/m^3 RHOAB = 997.0456 kg/m^3 ------------------------------- Submerged Single Port Discharge = left DISTB = 42.67 m DO = 0.3557 m AO = 0.0994 m^2 UO = 5.51 m/s- QO = 0.547658 m^3/s HO = 0.30 m THETA = 0 deg SIGMA = 0 deg RH00 = 998 kg/m^3 DRHO =-0.9544 kg/m^3 GPO =-0.0094 m/s^2 CO = 100 % KS = 0 m/s KD ------------------------------------ = 0 /s DISCHARGE/ENVIRONMENT LENGTH SCALES: LQ = 0.32 m Lm = 25.98 m Lb = 17.19 m LM = 31.94 m Lm' = 99999 m Lb' = 99999 m ---------------------------------------------------------------------- NON-DIMENSIONAL PARAMETERS: Port densimetric Froude number FRO = 95.37 Velocity ratio R = 82.41 a ---------------------------------------------------------------- MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS: Toxic discharge = no Water quality standard specified = no Regulatory mixing zone = yes Regulatory mixing zone specification = width Regulatory mixing zone value = 34.03 m (m^2 if area)_ 17•n� Region of interest = 2000 m ***************************************************************************** HYDRODYNAMIC CLASSIFICATION: *------------------------* FLOW CLASS = NH5 *------------------------* This flow Configuration applies to a layer corresponding to the full water depth at the discharge site. Applicable layer depth = water depth = 3.05 m ***************************************************************************** MIXING ZONE EVALUATION (hydrodynamic and regulatory summary): ----------------------------------------------------------------------------- X-Y-Z Coordinate system: Origin is located at the bottom below the port center: 42.67 m from the left bank/shore. Number of display steps NSTEP = 25 per module. ----------------------------------------------------------------------------- NEAR-FIELD REGION (NFR) CONDITIONS : Note: The NFR is the zone of strong initial mixing. It has no regulatory implication. However, this information may be useful for the discharge designer because the mixing in the NFR is usually sensitive to the discharge design conditions. Pollutant concentration at edge of.NFR = 2.3415 % Dilution at edge of NFR = 42.7 NFR Location: x = 183.65 m (centerline coordinates) y = 0 m z = 0 m NFR plume dimensions: half -width = 14.90 m thickness = 3.05 m Cumulative travel time: 2724.6472 sec. ----------------------------------------------------------------------------- Buoyancy assessment: The effluent density is greater than the surrounding ambient water density at the discharge level. Therefore, the effluent is NEGATIVELY BUOYANT and will tend to sink towards the bottom. ----------------------------------------------------------------------------- Near-field instability behavior: The discharge flow will experience instabilities with full vertical mixing in the near -field. There may be benthic impact of high pollutant concentrations. ----------------------------------------------------------------------------- FAR-FIELD MIXING SUMMARY: Plume becomes vertically fully mixed ALREADY IN NEAR -FIELD at 0 m downstream and continues as vertically mixed into the far -field. ----------------------------------------------------------------------------- PLUME BANK CONTACT SUMMARY: Plume in bounded section contacts nearest bank at 0 m downstream. Plume contacts second bank at 0 m downstream. ************************ TOXIC DILUTION ZONE SUMMARY ************************ No TDZ was specified for this simulation. ********************** REGULATORY MIXING ZONE SUMMARY *********************** The plume conditions at the boundary of the specified RMZ are as follows: Pollutant concentration = 2.563877 % Corresponding dilution = 39.0 Plume location: x = 183.65 m — (centerline coordinates) y = 42.67 m z = 0 m Plume dimensions: half -width = 3.05 m thickness = 3.05 m Cumulative travel time < 2724.6472 sec. (RMZ is within NFR) ********************* FINAL DESIGN ADVICE AND COMMENTS ********************** REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known technique is NOT AN EXACT SCIENCE. Extensive comparison with field and laboratory data has shown that the CORMIX predictions on dilutions and concentrations (with associated plume geometries) are reliable for the majority of cases and are accurate to within about +-50a (standard deviation). As a further safeguard, CORMIX will not give predictions whenever it judges the design configuration as highly complex and uncertain for prediction. CORMIXI PREDICTION FILE: 11111111111111111111111111111111111111111111111111111111111111111111111111111 CORMIX MIXING ZONE EXPERT SYSTEM Subsystem CORMIXI: Submerged Single Port Discharges CORMIX-GI Version 4.3GT HYDROI Version 4.3.0.2 June 2005 ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- CASE DESCRIPTION Site name/label: SRU Yadkin River Diffuser Design case: Alt 2-12.5 MGD-Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU_Diffuser.prd Time stamp: Mon Jan 16 12:48:38 2006 ENVIRONMENT PARAMETERS (metric units) Bounded section BS = 102.11 AS = 311.23 QA = 20.81 ICHREG= 1 HA = 3.05 HD = 3.05 UA = 0.067 F = 0.049 USTAR =0.5219E-02 UW = 2.000 UWSTAR=0.2198E-02 Uniform density environment STRCND= U RHOAM = 997.0456 DISCHARGE PARAMETERS (metric units) BANK = LEFT DISTB = 42.67 DO = 0.356 AO = 0.099 HO = 0.30 THETA = 0.00 SIGMA = 0.00 UO = 5.511 QO = 0.548 =0.5477E+00 RHO0 = 998.0000 DRHOO =-.9544E+00 GPO =-.9387E-02 CO =0.1000E+03 CUNITS= % IPOLL = 1 KS =0.0000E+00 KD =0.0000E+00 FLUX VARIABLES (metric units) QO =0.5477E+00 MO =0.3018E+01 JO =-.5141E-02 SIGNJO= -1.0 Associated length scales (meters) LQ = 0.32 LM = 31.94 Lm = 25.98 Lb = 17.19 Lmp = 99999.00 Lbp = 99999.00 NON -DIMENSIONAL PARAMETERS FRO = 95.37 R = 82.41 FLOW CLASSIFICATION 111111111111111111111111111111111111111111 1 Flow class (CORMIXI) = NH5 1 1 Applicable layer depth HS = 3.05 1 111111111111111111111111111111111111111111 MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS CO =0.1000E+03 CUNITS= o NTOX = 0 NSTD = 0 REGMZ = 1 REGSPC= 2 XREG = 0.00 WREG = XINT = 2000.00 XMAX = 2000.00 X-Y-Z COORDINATE SYSTEM: 34.03 AREG = 0.00 ORIGIN is located at the bottom and below the center of the port: 42.67 m from the LEFT bank/shore. X-axis points downstream, Y-axis points to left, Z-axis points upward. NSTEP = 25 display intervals per module -------------------------------------------------------------------------- -------------------------------------------------------------------------- BEGIN MOD101: DISCHARGE MODULE COANDA ATTACHMENT immediately following the discharge. X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.25 END OF MOD101: DISCHARGE MODULE ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION Bottom -attached jet motion. UNSTABLE NEAR -FIELD: Jet/plume will mix over full layer depth. Following MOD133 will include recirculation into jet region. Profile definitions: B = Gaussian 1/e (37%) half -width, normal to trajectory Half wall jet, attached to bottom. S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.18 1.16 0.00 0.00 1.0 0.975E+02 0.31 2.32 0.00 0.00 1.5 0.689E+02 0.43 3.47 0.00 0.00 1.9 0.533E+02 0.55 4.66 0.00 0.00 2.3 0.432E+02 0.68 5.82 0.00 0.00 2.7 0.364E+02 0.80 6.98 0.00 0.00 3.2 0.315E+02 0.92 8.17 0.00 0.00 3.6 0.276E+02 1.04 9.33 0.00 0.00 4.1 0.247E+02 1.16 10.49 0.00 0.00 4.5 0.223E+02 1.28 11.67 0.00 0.00 4.9 0.203E+02 1.40 12.83 0.00 0.00 5.4 0.186E+02 1.51 13.99 0.00 0.00 5.8 0.172E+02 1.63 15.18 0.00 0.00 6.3 0.160E+02 1.74 16.34 0.00 0.00 6.7 0.149E+02 1.86 17.50 0.00 0.00 7.1 0.140E+02 1.97 18.65 0.00 0.00 7.6 0.132E+02 2.08 19.84 0.00 0.00 8.0 0.125E+02 2.19 21.00 0.00 0.00 8.5 0.118E+02 2.30 22.16 0.00 0.00 8.9 0.112E+02 2.41 23.35 0.00 0.00 9.4 0.107E+02 2.52 24.51 0.00 0.00 9.8 0.102E+02 2.63 25.66 0.00 0.00 10.3 0.974E+01 2.73 26.85 0.00 0.00 10.7 0.932E+01 2.84 28.01 0.00 0.00 11.2 0.895E+01 2.95 29.17 0.00 0.00 11.6 0.860E+01 3.05 Cumulative travel time = 24.8216 sec 0 END OF CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING Control volume inflow: X Y Z S C B 29.17 0.00 0.00 11.6 0.860E+01 3.05 Profile definitions: BV = layer depth (vertically mixed) BH = top -hat half -width, in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic average (bulk) dilution C = average (bulk) concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 26.12 0.00 0.00 11.6 0.860E+01 0.00 0.00 0.00 0.00 26.73 0.00 0.00 11.6 0.860E+01 3.05 0.82 3.05 0.00 27.34 0.00 0.00 11.6 0.860E+01 3.05 1.15 3.05 0.00 27.95 0.00 0.00 11.6 0.860E+01 3.05 1.41 3.05 0.00 28.56 0.00 0.00 11.6 0.860E+01 3.05 1.63 3.05 0.00 29.17 0.00 0.00 11.6 0.860E+01 3.05 1.83 3.05 0.00 29.78 0.00 0.00 12.3 0.812E+01 3.05 2.00 3.05 0.00 30.39 0.00 0.00 13.8 0.724E+01 3.05 2.16 3.05 0.00 31.00 0.00 0.00 15.2 0.659E+01 3.05 2.31 3.05 0.00 31.6L 0.00 0.00 15.9 0.628E+01 3.05 2.45 3.05 0.00 32.22 0.00 0.00 16.3 0.615E+01 3.05 2.58. 3.05 0.00 Cumulative travel time = 38.7985 sec END OF MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING -------------------------------------------------------------- -------------------------------------------------------------- BEGIN MOD153: VERTICALLY MIXED PLUME IN CO -FLOW Phase 1: Vertically mixed, Phase 2: Re -stratified Phase 1: The plume is VERTICALLY FULLY MIXED over the entire layer depth. Profile definitions: BV = layer depth (vertically mixed) BH = Gaussian 1/e (37%) half -width in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 32.22 0.00 0.00 16.3 0.615E+01 3.05 2.52 3.05 0.00 38.27 0.00 0.00 18.1 0.553E+01 3.05 3.08 3.05 0.00 44.33 0.00 0.00 19.7 0.507E+01 3.05 3.63 3.05 0.00 50.39 0.00 0.00 21.3 0.470E+01 3.05 4.17 3.05 0.00 56.45 0.00 0.00 22.7 0.441E+01 3.05 4.71 3.05 0.00 62.50 0.00 0.00 24.0 0.416E+01 3.05 5.24 3.05 0.00 68.56 0.00 0.00 25.3 0.396E+01 3.05 5.76 3.05 0.00 74.62 0.00 0.00 26.5 0.378E+01 3.05 6.28 3.05 0.00 80.67 0.00 0.00 27.6 0.362E+01 3.05 6.79 3.05 0.00 86.73 0.00 0.00 92.79 0.00 0.00 98.85 0.00 0.00 104.90 0.00 0.00 110.96 0.00 0.00 117.02 0.00 0.00 123.08 0.00 0.00 129.13 0.00 0.00 135.19 0.00 0.00 141.25 0.00 0.00 147.30 0.00 0.00 153.36 0.00 0.00 159.42 0.00 0.00 165.48 0.00 0.00 171.53 0.00 0.00 177.59 0.00 0.00 183.65 0.00 0.00 Cumulative travel time = 28.7 0.348E+01 3.05 7.30 3.05 0.00 29.8 0.335E+01 3.05 7.80 3.05 0.00 30.8 0.324E+01 3.05 8.30 3.05 0.00 31.8 0.314E+01 3.05 8.79 3.05 0.00 32.8 0.305E+01 3.05 9.28 3.05 0.00 33.7 0.296E+01 3.05 9.77 3.05 0.00 34.6 0.289E+01 3.05 10.25 3.05 0.00 35.5 0.281E+01 3.05 10.73 3.05 0.00 36.4 0.275E+01 3.05 11.20 3.05 0.00 37.2 0.268E+01 3.05 11.67 3.05 0.00 38.1 0.263E+01 3.05 12.14 3.05 0.00 38.9 0.257E+01 3.05 12.61 3.05 0.00 39.7 0.252E+01 3.05 13.07 3.05 0.00 40.5 0.247E+01 3.05 13.53 3.05 0.00 41.2 0.243E+01 3.05 13.99 3.05 0.00 42.0 0.238E+01 3.05 14.44 3.05 0.00 42.7 0.234E+01 3.05 14.90 3.05 0.00 2724.6475 sec Entire region is occupied by Phase 1. Plume does not re -stratify in this flow region. END OF MOD153: VERTICALLY MIXED PLUME IN CO -FLOW -------------------------------------------------------------------------- ** End of NEAR -FIELD REGION (NFR) ** The initial plume WIDTH values in the next far -field module will be CORRECTED by a factor 3.75 to conserve the mass flux in the far -field! The correction factor is quite large because of the small ambient velocity relative to the strong mixing characteristics of the discharge! This indicates localized RECIRCULATION REGIONS and internal hydraulic JUMPS. Width predictions show discontinuities, dilution values should be acceptable. In this design case, the discharge is located CLOSE TO BANK/SHORE. Some boundary interaction occurs at end of near -field. This may be related to a design case with a very LOW AMBIENT VELOCITY. The dilution values in one or more of the preceding zones may be too high. Carefully evaluate results in near -field and check degree of interaction. Consider locating outfall further away from bank or shore. In the next prediction module, the plume centerline will be set to follow the bank/shore. The LIMITING DILUTION (given by ambient flow/discharge ratio) is: 39.0 This value is below the computed dilution of 42.7 at the end of the NFR. Mixing for this discharge configuration is constrained by LOW AMBIENT FLOW! The previous module predictions are unreliable since the limiting dilution cannot be exceeded for this shallow water discharge configuration. A subsequent module (MOD181) will predict the properties of the cross -sectionally fully mixed plume with limiting dilution and will compute a POSSIBLE UPSTREAM WEDGE INTRUSION. BEGIN MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION The DOWNSTREAM flow field for this unstable shallow water discharge is VERTICALLY FULLY MIXED. The mixing is controlled by the limiting dilution = 39.0 Channel DENSIMETRIC FROUDE NUMBER (FCHAN) for this mixed flow = 2.47 No upstream wedge intrusion takes place since FCHAN exceeds the critical value of 0.7. X Y Z S C BV BH ZU ZL 183.65 42.67 0.00 39.0 0.256E+01 3.05 102.11 3.05 0.00 Cumulative travel time = 2724.6472 sec VERTICALLY AND LATERALLY FULLY MIXED over layer depth: END OF SIMULATION! END OF MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION ----------------------------------------------------------------------------- ** REGULATORY MIXING ZONE BOUNDARY is within the Near -Field Region (NFR) ** In this prediction interval the TOTAL plume width meets or exceeds the regulatory value = 34.03 m. This is the extent of the REGULATORY MIXING ZONE. ----------------------------------------------------------------------------- CORMIXI: Submerged Single Port Discharges End of Prediction File 11111111111111111111111111111111111111111111111111111111111111111111111111111 NFR = 0t Appendix 11 Alternate 2 Configuration 12.-5 MGD Effluent Discharge High Rock Lake 5 ft below Full Pond CORMIX SESSION REPORT: XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX CORMIX MIXING ZONE EXPERT SYSTEM CORMIX-GI Version 4.3GT HYDR01:Version-4.3.0.2 June,2005 SITE NAME/LABEL: SRU Yadkin River Diffuser DESIGN CASE: Alt 2-12.5 MGD-5 ft below Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU Diffuser.prd Using subsystem CORMIXI: Submerged Single Port Discharges Start of session: 01/16/2006--12:52:17 SUMMARY OF INPUT DATA: AMBIENT PARAMETERS: Cross-section Width BS Channel regularity ICHREG Ambient flowrate QA Average depth HA Depth at discharge HD Ambient velocity UA Darcy-Weisbach friction factor F Calculated from Manning's n Wind velocity UW Stratification Type STRCNC Surface temperature degC Bottom temperature Calculated FRESH -WATER DENSITY values: Surface density RHOAS Bottom density ---------------------------------------- RHOAB DISCHARGE PARAMETERS: Nearest bank Distance to bank Port diameter Port cross -sectional area Discharge velocity Discharge flowrate Discharge port height Vertical discharge angle Horizontal discharge angle Discharge density Density difference Buoyant acceleration Discharge concentration Surface heat exchange coeff Coefficient of decay ----------------------------- = bounded = 89.92 m = 1 20.81 m^3/s 1.52 m-11 1.52 m" 0.1519 m/s 6.0614 0.03 2 m/s U 25 = 25 degC = 997.0456 kg/m^3 = 997.0456 kg/m^3 Submerged Single Port Discharge = left DISTB = 38.10 m DO = 0.3557 m-- AO = 0.0994 m^2 UO = 5.51 m/s QO = 0.547658 m^3/s HO = 0.30 m - THETA = 0 deg SIGMA = 0 deg RHO0 = 998 kg/m^3 DRHO =-0.9544 kg/m^3 GPO =-0.0094 m/s^2 CO = 100 % KS = 0 m/s KD = 0 / s DISCHARGE/ENVIRONMENT LENGTH SCALES: LQ = 0.32 m Lm = 11.44 m LM = 31.94 m Lm' = 99999 m NON -DIMENSIONAL PARAMETERS: Port densimetric Froude number FRO Velocity ratio R Lb = 1.47 m Lb' = 99999 m ---------------- = 95.37 = 36.29 ----------------------------------------------------------------------------- MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS: Toxic discharge = no Water quality standard specified = no Regulatory mixing zone = yes Regulatory mixing zone specification = width I q8 Regulatory mixing zone value = 29.97 m (m^2 if area), -- Region of interest = 2000 m HYDRODYNAMIC CLASSIFICATION: ------------------------ FLOW CLASS = NH5 I ------------------------ This flow configuration applies to a layer corresponding to the full water depth at the discharge site. Applicable layer depth = water depth = 1.52 m ***************************************************************************** MIXING ZONE EVALUATION (hydrodynamic and regulatory summary): ----------------------------------------------------------------------------- X-Y-Z Coordinate system: Origin is located at the bottom below the port center: 38.10 m from the left bank/shore. Number of display steps NSTEP = 25 per module. ----------------------------------------------------------------------------- NEAR-FIELD REGION (NFR) CONDITIONS : Note: The NFR is the zone of strong initial mixing. It has no regulatory implication. However, this information may be useful for the discharge designer because the mixing in the NFR is usually sensitive to the discharge design conditions. Pollutant concentration at edge of NFR = 5.2882 % Dilution at edge of NFR = 18.9 NFR Location: x = 71.18 m (centerline coordinates) y = 0 m z = 0 m NFR plume dimensions: half -width = 5.78 m thickness = 1.52 m Cumulative travel time: 455.0359 sec. ----------------------------------------------------------------------------- Buoyancy assessment: The effluent density is greater than the surrounding ambient water density at the discharge level. Therefore, the effluent is NEGATIVELY BUOYANT and will tend to sink towards the bottom. ----------------------------------------------------------------------------- Near-field instability behavior: The discharge flow will experience instabilities with full vertical mixing in the near -field. There may be benthic impact of high pollutant concentrations. ----------------------------------------------------------------------------- FAR-FIELD MIXING SUMMARY: Plume is vertically fully mixed WITHIN NEAR -FIELD (or a fraction thereof), but RE -STRATIFIES LATER. Plume becomes.vertically fully mixed again at 0 m downstream. ----------------------------------------------------------------------------- PLUME BANK CONTACT SUMMARY: Plume in bounded section does not contact bank. ************************ TOXIC DILUTION ZONE SUMMARY ************************ No TDZ was specified for this simulation. ********************** REGULATORY MIXING ZONE SUMMARY *********************** The plume conditions at the boundary of the specified RMZ are as follows: Pollutant concentration = 5.288208 % Corresponding dilution=-1_8:9 - Plume location: x = 71.18 m (centerline coordinates) y = 0 m z = 0 m Plume dimensions: half -width = 1.52_m thickness = 1.52 m Cumulative travel time < 455.0359 sec. (RMZ is within NFR) ********************* FINAL DESIGN ADVICE AND COMMENTS ********************** REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known technique is NOT AN EXACT SCIENCE. Extensive comparison with field and laboratory data has shown that the CORMIX predictions on dilutions and concentrations (with associated plume geometries) are reliable for the majority of cases and are accurate to within about +-50% (standard deviation). As a further safeguard, CORMIX will not give predictions whenever it judges the design configuration as highly complex and uncertain for prediction. CORMIXI PREDICTION FILE: 11111111111111111111111111111111111111111111111111111111111111111111111111111 CORMIX MIXING ZONE EXPERT SYSTEM Subsystem CORMIXI: Submerged Single Port Discharges CORMIX-GI Version 4.3GT HYDR01 Version 4.3.0.2 June 2005 ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- CASE DESCRIPTION Site name/label: SRU Yadkin River Diffuser Design case: Alt 2-12.5 MGD-5 ft below Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU_Diffuser.prd Time stamp: Mon Jan 16 12:52:18 2006 ENVIRONMENT PARAMETERS (metric units) Bounded section BS = 89.92 AS = 137.03 QA = 20.81 ICHREG= 1 HA = 1.52 HD = 1.52 UA = 0.152 F = 0.061 USTAR =0.1330E-01 UW = 2.000 UWSTAR=0.2198E-02 Uniform density environment STRCND= U RHOAM = 997.0456 DISCHARGE PARAMETERS (metric units) BANK = LEFT DISTB = 38.10 DO = 0.356 AO = 0.099 HO = 0.30 THETA = 0.00 SIGMA = 0.00 UO = 5.511 QO = 0.548 =0.5477E+00 RHOO = 998.0000 DRHOO =-.9544E+00 GPO =-.9387E-02 CO =0.1000E+03 CUNITS= % IPOLL = 1 KS =0.0000E+00 KD =0.0000E+00 FLUX VARIABLES (metric units) QO =0.5477E+00 MO =0.3018E+01 JO =-.5141E-02 SIGNJO= -1.0 Associated length scales (meters) l LQ = 0.32 LM = 31.94 Lm = 11.44 Lb = 1.47 Lmp = 99999.00 Lbp = 99999.00 NON -DIMENSIONAL PARAMETERS FRO = 95.37 R = 36.29 FLOW CLASSIFICATION 1111111111111111111111111111111111.11111111 1 Flow class (CORMIXI) = NH5 1 1 Applicable layer depth HS = 1.52 1 111111111111111111111111111111111111111111 MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS CO =0.1000E+03 CUNITS= o NTOX = 0 NSTD = 0 REGMZ = 1 REGSPC= 2 XREG = 0.00 WREG = 29.97 AREG = XINT = 2000.00 XMAX = 2000.00 X-Y-Z COORDINATE SYSTEM: 1 11 ORIGIN is located at the bottom and below the center of the port: 38.10 m from the LEFT bank/shore. X-axis points downstream, Y-axis points to left, Z-axis points upward. NSTEP­ 25 display intervals per module ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD101: DISCHARGE MODULE COANDA ATTACHMENT immediately following the discharge. X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.25 END OF MOD101: DISCHARGE MODULE ------------------------------------------------------------- ------------------------------------------------------------- BEGIN CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION Bottom -attached jet motion. UNSTABLE NEAR -FIELD: Jet/plume will mix over full layer depth. Following MOD133 will include recirculation into jet region. Profile definitions: B = Gaussian 1/e-(37%) half -width, normal to trajectory Half wall jet, attached to bottom. S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C `✓ 0.00 0.00 0.00 1.0 0.100E+03 0.18 0.55 0.00 0.00 1.0 0.100E+03 0.24 1.11 0.00 0.00 1.0 0.994E+02 0.30 1.68 0.00 0.00 1.2 0.824E+02 0.36 2.24 0.00 0.00 1.4 0.704E+02 0.41 2.79 0.00 0.00 1.6 0.616E+02 0.47 .3.35 0.00 0.00 1.8 0.545E+02 0.53 3.92 0.00 0.00 2.0 0.489E+02 0.59 4.48 0.00 0'.00 2.3 0.444E+02 0.64 5.03 0.00 0.00 2.5 0.407E+02 0.70 5.59 0.00 0.00 2.7 0.374E+02 0.75 6.16 0.00 0.00 2.9 0.347E+02 0.81 6.72 0.00 0.00 3.1 0.323E+02 0.86 7.28 0.00 0.00 3.3 0.302E+02 0.91 7.83 0.00 0.00 3.5 0.284E+02 0.97 8.40 0.00 0.00 3.7 0.268E+02 1.02 8.96 0.00 0.00 3.9 0.253E+02 1.07 9.52 0.00 0.00 4.2 0.240E+02 1.12 10.07 0.00 0.00 4.4 0.229E+02 1.17 10.64 0.00 0.00 4.6 0.218E+02 1.23 11.20 0.00 0.00 4.8 0.208E+02 1.28 11.77 0.00 0.00 5.0 0.199E+02 1.33 12.33 0.00 0.00 5.2 0.191E+02 1.38 12.88 0.00 0.00 5.4 0.183E+02 1.43 13.44 0.00 0.00 5.7 0.176E+02 1.48 14.01 0.00 0.00 5.9 0.170E+02 1.52 - Cumulative travel time = 6.3210 sec END OF CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION ------------------------------------------------------------------------- ------------------------------------------------------------------------- BEGIN MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING Control volume inflow: X Y Z S C B 14.01 0.00 0.00 5.9 0.170E+02 1.52 Profile definitions: BV = layer depth (vertically mixed) BH = top -hat half -width, in horizontal plane normal to trajectory ZU = upper p ume oundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic average (bulk) dilution C = average (bulk) concentration (includes reaction effects, if any) X Y Z S C BV QBD ZU ZL 12.48 0.00 0.00 5.9 0.170E+02 0.00 0.00 0.00 0.00 12.79 0.00 0.00 5.9 0.170E+02 1.52 0.40 1.52 0.00 13.09 0.00 0.00 5.9 0.170E+02 1.52 0.57 1.52 0.00 13.40 0.00 0.00 5.9 0.170E+02 1.52 0.70 1.52 0.00 13.70 0.00 0.00 5.9 0.170E+02 1.52 0.81 1.52 0.00 14.01 0.00 0.00 5.9 0.170E+02 1.52 0.90 1.52 0.00 14.31 0.00 0.00 6.2 0.161E+02 1.52 0.99 1.52 0.00 14.62 0.00 0.00 7.0 0.143E+02 1.52 1.07 1.52 0.00 14.92 0.00 0.00 7.7 0.130E+02 1.52 1.14 1.52 0.00 15.22 0.00 0.00 8.1 0.124E+02 1.52 1.21 1.52 0.00 15.53 0.00 0.00 8.2 0.121E+02 1.52 1-28 1.52 0.00 Cumulative travel time = 9.7727 sec END OF MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD153: VERTICALLY MIXED PLUME IN CO -FLOW_ Phase 1: Vertically mixed, Phase 2: Re -stratified Phase 1: The plume is VERTICALLY FULLY MIXED over the entire layer depth. Profile definitions: BV = layer depth (vertically mixed) BH = Gaussian l/e (37%) half -width_in hori.z.ont.al-p_laae,-normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 15.53 0.00 0.00 8.2 0.121E+02 1.52 1.26 1.52 0.00 17.76 0.00 0.00 8.9 0.112E+02 1.52 1.46 1.52 0.00 19.98 0.00 0.00 9.5 0.105E+02) 1.52 1.66 1.52 0.00 22.21 0.00 0.00 10.1 0.987E+01 1.52 1.86 1.52 0.00 24.43 0.00 0.00 10.7 0.936E+01 1.52 2.05 1.52 0.00 26.66 0.00 0.00 11.2 0.892E+01 1.52 2.24 1.52 0.00 28.89 0.00 0.00 11.7 0.853E+01 1.52 2.43 1.52 0.00 31.11 0.00 0.00 12.2 0.819E+01 1.52 2.62 1.52 0.00 33.34 0.00 0.00 12.7 0.789E+01 1.52 2.81 1.52 0.00 35.57 0.00 0.00 13.1 0.762E+01 1.52 2.99 1.52 0.00 37.79 0.00 0.00 13.6 0.738E+01 1.52 3.18 1.52 0.00 40.02 0.00 0.00 14.0 0.716E+01 1.52 3.36 1.52 0.00 42.24 0.00 0.00 14.4 0.695E+01 1.52 3.54 1.52 0.00 44.47 0.00 0.00 14.8 0.677E+01 1.52 3.72 1.52 0.00 46.70 0.00 0.00 15.2 0.659E+01 1.52 3.90 1.52 0.00 48.92 0.00 0.00 15.5 0.643E+01 1.52 4.07 1.52 0.00 51.15 0.00 0.00 15.9 0.628E+01 1.52 4.25 1.52 0.00 53.38 0.00 0.00 16.3 0.614E+01 1.52 4.42 1.52 0.00 55.60 0.00 0.00 16.6 0.601E+01 1.52 4.60 1.52 0.00 57.83 0.00 0.00 17.0 0.589E+01 1.52 4.77 1.52 0.00 60.05 0.00 0.00 17.3 0.578E+01 1.52 4.94 1.52 0.00 62.28 0.00 0.00 17.6 0.567E+01 1.52 5.11 1.52 0.00 64.51 0.00 0.00 18.0 0.557E+01 1.52 5.28 1.52 0.00 66.73 0.00 0.00 18.3 0.547E+01 1.52 5.45 1.52 0.00 68.96 0.00 0.00 ._-18.6 0.538E+01_ 1.52 5.62 1.52 0.00 71.18 0.00 0.00 �18.9 0.529E+O1 1.52 5.78- 1.52- 0.00 Cumulative aveI time = 455.0360 sec Entire region is occupied by Phase 1. Plume does not re -stratify in this flow region. END OF MOD153: VERTICALLY MIXED PLUME IN CO -FLOW ----------------------------------------------------------------------------- ** End of NEAR -FIELD REGION (NFR) ** The initial plume WIDTH values in the next far -field module will be CORRECTED by a factor �7 to conserve the mass flux in the far -field! The correction factor is quite large because of the small ambient velocity relative to the strong mixing characteristics of the discharge! This indicates localized RECIRCULATION REGIONS and internal hydraulic JUMPS. Width predictions show discontinuities, dilution values should be acceptable. ** REGULATORY MG_.ZONE_..8O.UNDARY is within the Near -Field Region (NFR) ** In this prediction interval the TOTAL plume width meets or exceeds the regulatory value = 29.97 m. This is the extent of the REGULATORY MIXING ZONE. ----------------------------------------------------------------------------- BEGIN MOD141: BUOYANT AMBIENT SPREADING Profile definitions: BV = top -hat thickness, measured vertically BH = top -hat half -width, measured horizontally in Y-direction ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic average (bulk) dilution C = average (bulk) concentration (includes reaction effects, if any) Plume Stage 1 (not bank attached): X Y Z S C BV B14 ZU ZL 71.18 0.00 0.00 18.9 0.529E+01 1.52 ;21.80 1.52 0.00 71.75 0.00 0.00 19.0 0.528E+01 1.52 1.52 0.00 72.32 0.00 0.00 19.0 0.526E+01 1.52 21.91 1.52 0.00 72.89 0.00 0.00 19.0 0.525E+01 1.52 21.96 1.52 0.00 73.46 0.00 0.00 19.1 0.524E+01 1.52 22.02- 1.52 0.00 74.03 0.00 0.00 19.1 0.523E+01 1.52 22.08 1.52 0.00 74.59 0.00 0.00 19.2 0.521E+01 1.52 22.13 1.52 0.00 75.16 0.00 0.00 19.2 0.520E+01 1.52 22.19 1.52 0.00 75.73 0.00 0.00 19.3 0.519E+01 1.52 22.24 1.52 0.00 76.30 0.00 0.00 19.3 0.518E+01 1.52 22.30 1.52 0.00 76.87 0.00 0.00 19.4 0.516E+01 1.52 22.35 1.52 0.00 77.44 0.00 0.00 19.4 0.515E+01 1.52 22.41 1.52 0.00 78.00 0.00 0.00 19.5 0.514E+01 1.52 22.46 1.52 0.00 78.57 0.00 0.00 19.5 0.513E+01 1.52 22.52 1.52 0.00 79.14 0.00 0.00 19.6 0.511E+01 1.52 22.57 1.52 0.00 79.71 0.00 0.00 19.6 0.510E+01 1.52 22.63 1.52 0.00 80.28 0.00 0.00 19.6 0.509E+01 1.52 22.68 1.52 0.00 80.85 0.00 0.00 19.7 0.508E+01 1.52 22.74 1.52 0.00 81.41 0.00 0.00 19.7 0.507E+01 1.52 22.79 1.52 0.00 81.98 0.00 0.00 19.8 0.505E+01 1.52 22.85 1.52 0.00 82.55 0.00 0.00 19.8 0.504E+01 1.52 22.90 1.52 0.00 83.12 0.00 0.00 19.9 0.503E+01 1.52 22.95 1.52 0.00 83.69 0.00 0.00 19.9 0.502E+01 1.52 23.01 1.52 0.00 84.26 0.00 0.00 20.0 0.501E+01 1.52 23.06 1.52 0.00 84.82 0.00 0.00 20.0 0.499E+01 1.52 23.12 1.52 0.00 85.39 0.00 0.00 20.1 0.498E+01 1.52 23.17 1.52 0.00 Cumulative travel time = 546.1778 sec END OF MOD141: BUOYANT AMBIENT SPREADING ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD161: PASSIVE AMBIENT MIXING IN UNIFORM AMBIENT Vertical diffusivity (initial value) = 0.406E-02 m^2/s Horizontal diffusivity (initial value) = 0.508E-02 m^2/s Profile definitions: BV = Gaussian s.d.*sgrt(pi/2) (46%) thickness, measured vertically = or equal to layer depth, if fully mixed BH = Gaussian s.d.*sgrt(pi/2) (46%) half -width, measured horizontally in Y-direction ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) Plume Stage 1 (not bank attached): X Y Z S C BV BH ZU ZL 85.39 0.00 0.00 20.1 0.498E+01 1.52 23.17 1.52 0.00 161.98 0.00 0.00 20.2 0.494E+01 1.52 23.34 1.52 0.00 238.,56 0.00 0.00 20.4 0.490E+01 1.52 23.51 1.52 0.00 315.15 0.00 0.00 20.5 0.487E+01 1.52 23.67 1.52 0.00 391.73 0.00 0.00 20.7 0.484E+01 1.52 23.84 1.52 0.00 468.31 0.00 0.00 20.8 0.480E+01 1.52 24.00 1.52 0.00 544.90 0.00 0.00 21.0 0.477E+01 1.52 24.16 1.52 0.00 621.48 0.00 0.00 21.1 0.474E+01 1.52 24.3.3 1.52 0.00 698.07 0.00 0.00 21.2 0.471E+01 1.52 24.49 1.52 0.00 774.65 0.00 0.00 21.4 0.468E+01 1.52 24.65 1.52 0.00 851.24 0.00 0.00 21.5 0.465E+01 1.52 24.80 1.52 0.00 927.82 0.00 0.00 21.7 0.462E+01 1.52 24.96 1.52 0.00 1004.40 0.00 0.00 21.8 0.459E+01 1.52 25.12 1.52 0.00 1080.99 0.00 0.00 21.9 0.456E+01 1.52 25.27 1.52 0.00 1157.57 0.00 0.00 22.1 0.453E+01 1.52 25.43 1.52 0.00 1234.16 0.00 0.00 22.2 0.451E+01 1.52 25.58 1.52 0.00 1310.74 0.00 0.00 22.3 0.448E+01 1.52 25.73 1.52 0.00 1387.33 0.00 0.00 22.5 0.445E+01 1.52 25.89 1.52 0.00 1463.91 0.00 0.00 22.6 0.443E+01 1.52 26.04 1.52 0.00 1540.49 0.00 0.00 22.7 0.440E+01 1.52 26.19 1.52 0.00 1617.08 0.00 0.00 22.8 0.438E+01 1.52 26.34 1.52 0.00 1693.66 0.00 0.00 23.0 0.435E+01 1.52 26.49 1.52 0.00 1770.25 0.00 0.00 23.1 0.433E+01 1.52 26.63 1.52 0.00 1846.83 0.00 0.00 23.2 0.430E+01 1.52 26.78 1.52 0.00 1923.42 0.00 0.00 23.4 0.428E+01 1.52 26.93 1.52 0.00 2000.00 0.00 0.00 23.5 0.426E+01 1.52 27.07 1.52 0.00 Cumulative travel time = 12828.7568 sec Simulation limit based on maximum specified distance = 2000.00 m. This is the REGION OF INTEREST limitation. END OF MOD161: PASSIVE AMBIENT MIXING IN UNIFORM AMBIENT ----------------------------------------------------------------------------- --------------------=-------------------------------------------------------- CORMIXI: Submerged Single Port Discharges End of Prediction File 11111111111111111111111111111111111111111111111111.111111111111111111111111111 Z Y" 72 M Appendix 12 Alternate 2 Configuration 0RA- Pr ICCI 20 MGD Effluent DischarrV17% ge High Rock Lake Full Pond CORMIX SESSION REPORT: XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX CORMIX MIXING ZONE EXPERT SYSTEM CORMIX-GI Version 4.3GT HYDRO1:Version-4.3.0.2 June,2005 SITE NAME/LABEL: SRU Yadkin River Diffuser DESIGN CASE: Alt 2-20 MGD-Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU Diffuser.prd Using subsystem CORMIXI: Submerged Single Port Discharges Start of session: 01/16/2006--12:50:46 SUMMARY OF INPUT DATA: ----------------------------------------------------------------------------- AMBIENT PARAMETERS: Cross-section = bounded Width BS = 102.11 m Channel regularity ICHREG = 1 Ambient flowrate QA = 20.81 m^3/s Average depth HA = 3.05 m Depth at discharge HD = 3.05 m Ambient velocity UA = 0.0669 m/s Darcy-Weisbach friction factor F = 0.0487 Calculated from Manning's n = 0.03 Wind velocity UW = 2 m/s Stratification Type STRCND = U Surface temperature = 25 degC Bottom temperature = 25 degC Calculated FRESH -WATER DENSITY values: Surface density RHOAS = 997.0456 kg/m^3 Bottom density RHOAB = 997.0456 kg/m^3 ----------------------------------------------------------------------------- DISCHARGE PARAMETERS: Submerged Single Port Discharge Nearest bank = left Distance to bank DISTB = 42.67 m Port diameter DO = 0.3557 m Port cross -sectional area AO = 0.0994 m^2 Discharge velocity UO = 8.82 m/s Discharge flowrate QO = 0.876253 m^3/s Discharge port height HO = 0.30 m Vertical discharge angle THETA = 0 deg Horizontal discharge angle SIGMA = 0 deg Discharge density RHO0 = 998 kg/m^3 Density difference DRHO = -0.9544 kg/m^3 Buoyant acceleration GPO = -0.0094 m/s^2 Discharge concentration CO = 100 % Surface heat exchange coeff. KS = 0 m/s Coefficient of decay KD = 0 /s ----------------------------------------------------------------------------- DISCHARGE/ENVIRONMENT LENGTH SCALES: LQ = 0.32 m Lm = 41.57 m Lb='27.50 m LM = 51.10 m Lm' = 99999 m Lb' = 99999 m NON -DIMENSIONAL PARAMETERS: Port densimetric Froude number FRO = 152.60 Velocity ratio R = 131.86 ----------------------------------------------------------------------------- MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS: Toxic discharge = no Water quality standard specified = no Regulatory mixing zone = yes Regulatory mixing zone specification = width Regulatory mixing zone value = 34.03 m (m^2 if area) Region of interest = 2000 m ***************************************************************************** HYDRODYNAMIC CLASSIFICATION: ------------------------ FLOW CLASS = NHS ------------------------ This flow configuration applies to a layer corresponding to the full water depth at the discharge site. Applicable layer depth = water depth = 3.05 m ***************************************************************************** MIXING ZONE EVALUATION (hydrodynamic and regulatory summary): ----------------------------------------------------------------------------- X-Y-Z Coordinate system: Origin is located at the bottom below the port center: '42.67 m from the left bank/shore. Number of display steps NSTEP = 25 per module. ----------------------------------------------------------------------------- NEAR-FIELD REGION (NFR) CONDITIONS : Note: The NFR is the zone of strong initial mixing. It has no regulatory implication. However, this information may be useful for the discharge designer because the mixing in the NFR is usually sensitive to the discharge design conditions. Pollutant concentration at edge of NFR = 1.506 % Dilution at edge of NFR = 66.4 NFR Location: x = 459.89 m (centerline coordinates) y = 0 m z = 0 m NFR plume dimensions: half -width = 37.88 m thickness = 3.05 m Cumulative travel time: 7210.2446 sec. ----------------------------------------------------------------------------- Buoyancy assessment: The effluent density is greater than the surrounding ambient water density at the discharge level. Therefore, the effluent is NEGATIVELY BUOYANT and will tend to sink towards the bottom. ----------------------------------------------------------------------------- Near-field instability behavior: The discharge flow will experience instabilities with full vertical mixing in the near -field. There may be benthic impact of high pollutant concentrations. ----------------------------------------------------------------------------- FAR-FIELD MIXING SUMMARY: Plume becomes vertically fully mixed ALREADY IN NEAR -FIELD at 0 m downstream and continues as vertically mixed into the far -field. ----------------------------------------------------------------------------- PLUME BANK CONTACT SUMMARY: Plume in bounded section contacts nearest bank at 0 m downstream. Plume contacts second bank at 0 m downstream. ************************ TOXIC DILUTION ZONE SUMMARY ************************ No TDZ was specified for this simulation. ********************** REGULATORY MIXING ZONE SUMMARY *********************** The plume conditions at the boundary of the specified RMZ are as follows: Pollutant concentration = 2.289918 % Corresponding dilution = 43.7 Plume location: x = 202.56 m (centerline coordinates) y = 0 m z = 0 m Plume dimensions: half -width = 3.05 m thickness = 3.05 m Cumulative travel time < 7210.2446 sec. (RMZ is within NFR) ********************* FINAL DESIGN ADVICE AND COMMENTS ********************** REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known technique is NOT AN EXACT SCIENCE. Extensive comparison with field and laboratory data has shown that the CORMIX predictions on dilutions and concentrations (with associated plume geometries) are reliable for the majority of cases and are accurate to within about +-500 (standard deviation). As a further safeguard, CORMIX will not give predictions whenever it judges the design configuration as highly complex and uncertain for prediction. CORMIXI PREDICTION FILE: 11111111111111111111111111111111111111111111111111111111111111111111111111111 CORMIX MIXING ZONE EXPERT SYSTEM Subsystem CORMIXI: Submerged Single Port Discharges CORMIX-GI Version 4.3GT HYDR01 Version 4.3.0.2 June 2005 ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- CASE DESCRIPTION Site name/label: SRU Yadkin River Diffuser Design case: ,Alt 2-20 MGD-Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU_Diffuser.prd Time stamp: Mon Jan 16 12:50:46 2006 ENVIRONMENT PARAMETERS (metric units) Bounded section BS = 102.11 AS = 311.23 QA = 20.81 ICHREG= 1 HA = 3.05 HD = 3.05 UA = 0.067 F = 0.049 USTAR =0.5219E-02 UW = 2.000 UWSTAR=0.2198E-02 Uniform density environment STRCND= U RHOAM = 997.0456 DISCHARGE PARAMETERS (metric units) BANK = LEFT DISTB = 42.67 DO = 0.356 AO = 0.099 HO = 0.30 THETA = 0.00 SIGMA = 0.00 UO = 8.818 QO = 0.876 =0.8763E+00 RH00 = 998.0000 DRH00 =-.9544E+00 GPO =-.9387E-02 CO =0.1000E+03 CUNITS= o IPOLL = 1 KS =0.0000E+00 KD =0.0000E+00 FLUX VARIABLES (metric units) QO =0.8763E+00 MO =0.7727E+01 Associated length scales (meters) LQ = 0.32 LM = 51.10 NON -DIMENSIONAL PARAMETERS FRO = 152.60 R = 131.86 JO =-.8226E-02 SIGNJO= -1.0 Lm = 41.57 Lb = 27.50 Lmp = 99999.00 Lbp = 99999.00 FLOW CLASSIFICATION 111111111111111111111111111111111111111111 1 Flow class (CORMIXI) = NH5 1 1 Applicable layer depth HS = 3.05 1 111111111111111111111111111111111111111111 MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS CO =0.1000E+03 CUNITS= o NTOX = 0 NSTD = 0 REGMZ = 1 REGSPC= 2 XREG = 0.00 WREG = 34.03 AREG = XINT = 2000.00 XMAX = 2000.00 X-Y-Z COORDINATE SYSTEM: 1 11 ORIGIN is located at the bottom and below the center of the port: 42.67 m from the LEFT bank/shore. X-axis points downstream, Y-axis points to left, Z-axis points upward. NSTEP = 25 display intervals per module -------------------------------------------------------------------------- -------------------------------------------------------------------------- BEGIN MOD101: DISCHARGE MODULE COANDA ATTACHMENT immediately following the discharge. X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.25 END OF MOD101: DISCHARGE MODULE ---------------------------------------------------------- ---------------------------------------------------------- BEGIN CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION Bottom -attached jet motion. UNSTABLE NEAR -FIELD: Jet/plume will mix over full layer depth. Following MOD133 will include recirculation into jet region. Profile definitions: B = Gaussian 1/e (370) half -width, normal to trajectory Half wall jet, attached to bottom. S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.18 1.10 0.00 0.00 1.0 0.997E+02 0.30 2.23 0.00 0.00 1.4 0.706E+02 0.42 3.35 0.00 0.00 1.8 0.547E+02 0.54 4.45 0.00 0.00 2.2 0.448E+02 0.66 5.58 0.00 0.00 2.6 0.378E+02 0.78 6.71 0.00 0.00 3.1 0.326E+02 0.90 7.80 0.00 0.00 3.5 0.288E+02 1.02 8.93 0.00 0.00 3.9 0.257E+02 1.14 10.06 0.00 0.00 4.3 0.232E+02 1.25 11.19 0.00 0.00 4.7 0.212E+02 1.37 12.28 0.00 0.00 5.1 0.195E+02 1.48 13.41 0.00 0.00 5.6 0.180E+02 1.60 14.54 0.00 0.00 6.0 0.167E+02 1.72 15.64 0.00 0.00 6.4 0.157E+02 1.83 16.76 0.00 0.00 6.8 0.147E+02 1.94 17.89 0.00 0.00 7.2 0.138E+02 2.06 19.02 0.00 0.00 7.7 0.131E+02 2.17 20.12 0.00 0.00 8.1 0.124E+02 2.28 21.24 0.00 0.00 8.5 0.118E+02 2.39 22.37 0.00 0.00 8.9 0.112E+02 2.50 23.47 0.00 0.00 9.3 0.107E+02 2.61 24.60 0.00 0.00 9.8 0.102E+02 2.72 25.73 0.00 0.00 10.2 07.980E+01 2.83 26.85 0.00 0.00 10.6 0.941E+01 2.94 27.95 0.00 0.00 11.0 0.905E+01 3.05 Cumulative travel time = 14.7010 sec END OF CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION --------------------------------------------------------------------- --------------------------------------------------------------- BEGIN MOD133 LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING Control volume inflow: X Y Z S C B 27.95 0.00 0.00 11.0 0.905E+01 3.05 Profile definitions: BV = layer depth (vertically mixed) BH = top -hat half -width, in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic average (bulk) dilution C = average (bulk) concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 24.90 0.00 0.00 11.0 0.905E+01 0.00 0.00 0.00 0.00 25.51 0.00 0.00 11.0 0.905E+01 3.05 0.84 3.05 0.00 26.12 0.00 0.00 11.0 0.905E+01 3.05 1.18 3.05 0.00 26.73 0.00 0.00 11.0 0.905E+01 3.05 1.45 3.05 0.00 27.34 0.00 0.00 11.0 0.905E+01 3.05 1.67 3.05 0.00 27.95 0.00 0.00 11.0 0.905E+01 3.05 1.87 3.05 0.00 28.56 0.00 0.00 11.7 0.855E+01 3.05 2.05 3.05 0.00 29.17 0.00 0.00 13.1 0.762E+01 3.05 2.22 3.05 0.00 29.78 0.00 0.00 14.4 0.694E+01 3.05 2.37 3.05 0.00 30.39 0.00 0.00 15.1 0.661E+01 3.05 2.51 3.05 0.00 31.00 0.00 0.00 15.5 0.647E+01 3.05 2.65 3.05 0.00 Cumulative travel time = 23.8939 sec END OF MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD153: VERTICALLY MIXED PLUME IN CO -FLOW Phase 1: Vertically mixed, Phase 2: Re -stratified Phase 1: The plume is VERTICALLY FULLY MIXED over the entire layer depth. Profile definitions: BV = layer depth (vertically mixed) BH,= Gaussian 1/e (370) half -width in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 31.00 0.00 0.00 15.5 0.647E+01 3.05 2.51 3.05 0.00 48.15 0.00 0.00 20.1 0.496E+01 3.05 4.17 3.05 0.00 65.31 0.00 0.00 23.9 0.418E+01 3.05 5.79 3.05 0.00 82.47 0.00 0.00 27.2 0.368E+01 3.05 7.38 3.05 0.00 99.62 0.00 0.00 30.1 0.332E+01 3.05 8.94 3.05 0.00 116.78 0.00 0.00 32.8 0.305E+01 3.05 10.47 3.05 0.00 133.93 0.00 0.00 35.2 0.284E+01 3.05 11.98 3.05 0.00 151.09 0.00 0.00 37.5 0.267E+01 3.05 13.46 3.05 0.00 168.24 0.00 0.00. 39.7 0.252E+01 3.05 14.93 3.05 0.00 185.40 0.00 0.00 41.7 0.240E+01 3.05 116.38' 3.05 0.00 ** REGULATORY MIXING ZONE BOUNDARY is within the Near, -Field Region (NFR) ** In this prediction interval the TOTAL plume width meets or exceeds the regulatory value = 34.03 m. This is the extent of the REGULATORY MIXING ZONE. 202.56 0.00 0.00 43.7 0.229E+01 3.05 17.82 3.05 0.00 219.71 0.00 0.00 45.5 0.220E+01 3.05 19.24 3.05 0.00 236.87 0.00 0.00 47.3 0.211E+01 3.05 20.65 3.05 0.00 254.02 0.00 0.00 49.1 0.204E+01 3.05 22.04 3.05 0.00 271.18 0.00 0.00 50.7 0.197E+01 3.05 23.42 3.05 0.00 288.33 0.00 0.00 52.4 0.191E+01 3.05 24.78 3.05 0.00 305.49 0.00 0.00 53.9 0.185E+01 3.05 26.14 3.05 0.00 322.65 0.00 0.00 55.4 0.180E+01 3.05 27.48 3.05 0.00 339.80 0.00 0.00 56.9 0.176E+01 3.05 28.82 3.05 0.00 356.96 0.00 0.00 58.4 0.171E+01 3.05 30.14 3.05 0.00 374.11 0.00 0.00 59.8 0.167E+01 3.05 31.45 3.05 0.00 391.27 0.00 0.00 61.2 0.163E+01 3.05 32.76 3.05 0.00 408.42 0.00 0.00 62.5 0.160E+01 3.05 34.05 3.05 0.00 425.58 0.00 0.00 63.8 0.157E+01 3.05 35.34 3.05 0.00 442.74 0.00 0.00 65.1 0.154E+01 3.05 36.61 3.05 0.00 459.89 0.00 0.00 66.4 0.151E+01 3.05 37.88 3.05 0.00 Cumulative travel time = 7210.2446 sec Entire region is occupied by Phase 1. Plume does not re -stratify in this flow region. END OF MOD153: VERTICALLY MIXED PLUME IN CO -FLOW ** End of NEAR -FIELD REGION (NFR) ** The initial plume WIDTH values in the next far -field module will be CORRECTED by a factor 3.62 to conserve the mass flux in the far -field! The correction factor is quite large because of the small ambient velocity relative to the strong mixing characteristics of the discharge! This indicates localized RECIRCULATION REGIONS and internal hydraulic JUMPS. Width predictions show discontinuities, dilution values should be acceptable. The LIMITING DILUTION (given by ambient flow/discharge ratio) is: 24.8 This value is below the computed dilution of 66.4 at the end of the NFR. Mixing for this discharge configuration is constrained by LOW AMBIENT FLOW! The previous module predictions are unreliable since the limiting dilution cannot be exceeded for this shallow water discharge configuration. A subsequent module (MOD181) will predict the properties of the . cross -sectionally fully mixed plume with limiting dilution and will compute a POSSIBLE UPSTREAM WEDGE INTRUSION. --------------------------------------------------------------------------- BEGIN MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION The DOWNSTREAM flow field for this unstable shallow water discharge is VERTICALLY FULLY MIXED. The mixing is controlled by the limiting dilution = 24.8 Channel DENSIMETRIC FROUDE NUMBER (FCHAN) for this mixed flow = 1.97 No upstream wedge intrusion takes place since FCHAN exceeds the critical value of 0.7. X Y Z S C BV BH ZU ZL 459.89 42.67 0.00 24.8 0.404E+01 3.05 102.11 3.05 0.00 Cumulative travel time = 7210.2446 sec VERTICALLY AND LATERALLY FULLY MIXED over layer depth: END OF SIMULATION! END OF MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION ---------------------------------------------------------------------------- CORMIXI: Submerged Single Port Discharges End of Prediction File 11111111111111111111111111111111111111111111111111111111111111111111111111111 Rbqa _.� 2-Oq m Appendix' 13 Alternate 2 Configuration 20 MGD Effluent Discharry ge High Rock Lake 5 ft below Full Pond CORMIX SESSION REPORT: XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX CORMIX MIXING ZONE EXPERT SYSTEM CORMIX-GI Version 4.3GT HYDRO1:Version-4.3.0.2 June,2005 SITE NAME/LABEL: SRU Yadkin River Diffuser DESIGN CASE: Alt 2-20 MGD-5 ft below Full Pond FILE NAME: C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU Diffuser.prd Using subsystem CORMIXI: Submerged Single Port Discharges Start of session: 01/16/2006--12:53:43 SUMMARY OF INPUT DATA: ------------------- AMBIENT PARAMETERS: Cross-section = bounded Width BS = 89.92 m Channel regularity ICHREG = 1 Ambient flowrate QA = 20.81 m^3/s/ Average depth HA = 1.52 m Depth at discharge HD = 1.52 m Ambient velocity UA = 0.1519 m/s Darcy-Weisbach friction factor F = 0.0614 Calculated from Manning's n = 0.03 Wind velocity UW = 2 m/s Stratification Type STRCND = U Surface temperature = 25 degC Bottom temperature Calculated FRESH -WATER DENSITY values: Surface density RHOAS Bottom density RHOAB ---------------------------------------- = 25 degC = 997.0456 kg/m^3 = 997.0456 kg/m^3 -------------------------- DISCHARGE PARAMETERS: Submerged Single Port Discharge Nearest bank = left Distance to bank DISTB = 38.10 m Port diameter DO = 0.3557 m Port cross -sectional area AO = 0.0994 m^2 Discharge velocity UO = 8.82 m/s Discharge flowrate QO = 0.876253 m^3/s Discharge port height HO = 0.30 m Vertical discharge angle THETA = 0 deg Horizontal discharge angle SIGMA = 0 deg Discharge density RHO_0 = 998 kg/m^3 Density difference DRHO = -0.9544 kg/m^3 Buoyant acceleration GPO = -0.0094 m/s^2 Discharge concentration CO = 100 % Surface heat exchange coeff. KS = 0 m/s Coefficient of decay KD = 0 /s ----------------------------------------------------------------- DISCHARGE/ENVIRONMENT LENGTH SCALES: LQ = 0.32 m Lm = 18.30 m Lb = 2.35 m LM = 51.10 m Lm' = 99999 m Lb' = 99999 m ----------------------------------------------------------------- NON-DIMENSIONAL PARAMETERS: Port densimetric Froude number FRO = 152.60 Velocity ratio R = 58.06 MIXING ZONE / TOXIC DILUTION ZONE / AREA OF INTEREST PARAMETERS: Toxic discharge = no Water quality standard specified = no Regulatory mixing zone = yes Regulatory mixing zone specification = width Regulatory mixing zone value = 29.97 m (m^2 if area) Region of interest = 2000 m HYDRODYNAMIC CLASSIFICATION: *----------------* FLOW CLASS = NH5 ------------------------ This flow configuration applies to a layer corresponding to the full water depth at the discharge site. Applicable layer depth = water depth = 1.52 m ***************************************************************************** MIXING ZONE EVALUATION (hydrodynamic and regulatory summary): ----------------------------------------------------------------------------- X-Y-Z Coordinate system: Origin is located at the bottom below the port center: 38.10 m from the left bank/shore. Number of display steps NSTEP = 25 per module. ----------------------------------------------------------------------------- NEAR-FIELD REGION (NFR) CONDITIONS : Note: The NFR is the zone of strong initial mixing. It has no regulatory implication. However, this information may be useful for the discharge designer because the mixing in the NFR is usually sensitive to the discharge design conditions. Pollutant concentration at edge of NFR = 3.4144 % Dilution at edge of NFR = 29.3 NFR Location: x = 178.21 m (centerline coordinates) y = 0 m z = 0 m NFR plume dimensions: half -width = 14.69 m thickness = 1.52 m Cumulative travel time: 1225.1016 sec. ----------------------------------------------------------------------------- Buoyancy assessment: The effluent density is greater than the surrounding ambient water density at the discharge.level. Therefore, the effluent is NEGATIVELY BUOYANT and will tend to sink towards the bottom. ----------------------------------------------------------------------------- Near-field instability behavior: The discharge flow will experience instabilities with full vertical mixing in the near -field. There may be benthic impact of high pollutant concentrations. ----------------------------------------------------------------------------- FAR-FIELD MIXING SUMMARY: Plume becomes vertically fully mixed ALREADY IN NEAR -FIELD at 0 m downstream and continues as vertically mixed into the far -field. ----------------------------------------------------------------------------- PLUME BANK CONTACT SUMMARY: Plume in bounded section contacts nearest bank at 0 m downstream. Plume contacts second bank at 0 m downstream. ************************ TOXIC DILUTION ZONE SUMMARY ************************ No TDZ was specified for this simulation. ********************** REGULATORY MIXING ZONE SUMMARY *********************** The plume conditions at the boundary of the specified RMZ are as follows: Pollutant concentration = 4.040054 % Corresponding dilution = 24.8 Plume location: x = 178.21 m (centerline coordinates) y = 38.10 m z = 0 m Plume dimensions: half -width = 1.52 m thickness = 1.52 m Cumulative travel time < 1225.1016 sec. (RMZ is within NFR) ********************* FINAL DESIGN ADVICE AND COMMENTS ********************** REMINDER: The user must take note that HYDRODYNAMIC MODELING by any known technique is NOT AN EXACT SCIENCE. Extensive comparison with field and laboratory data has shown that the CORMIX predictions on dilutions and concentrations (with associated plume geometries) are reliable for the majority of cases and are accurate to within about +-50% (standard deviation). As a further safeguard, CORMIX will not give predictions whenever it judges the design configuration as highly complex and uncertain for prediction. CORMIXI PREDICTION FILE: 11111111111111111111111111111111111111111111111111111111111111111111111111111 CORMIX MIXING ZONE EXPERT SYSTEM Subsystem CORMIXI: Submerged Single Port Discharges CORMIX-GI Version 4.3GT HYDROI Version 4.3.0.2 June 2005 ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- CASE DESCRIPTION Site name/label Design case: FILE NAME: Time stamp: SRU Yadkin River Diffuser Alt 2-20 MGD-5 ft below Full Pond C:\Program Files\CORMIX-GI 4.3\MyFiles\SRU_Diffuser.prd Mon Jan 16 12:53:43 2006 ENVIRONMENT PARAMETERS (metric units) Bounded section BS = 89.92 AS = 137.03 QA = 20.81 ICHREG= 1 HA = 1.52 HD = 1.52 UA = 0.152 F = 0.061 USTAR =0.1330E-01 UW = 2.000 UWSTAR=0.2198E-02 Uniform density environment STRCND= U RHOAM = 997.0456 DISCHARGE PARAMETERS (metric units) BANK = LEFT DISTB = 38.10 DO = 0.356 AO = 0.099 HO = 0.30 THETA = 0.00 SIGMA = 0.00 UO = 8.818 QO = 0.876 =0.8763E+00 RHOO = 998.0000 DRHO0 =-.9544E+00 GPO =-.9387E-02 CO =0.1000E+03 CUNITS= o IPOLL = 1 KS =0.0000E+00 KD =0.0000E+00 FLUX VARIABLES (metric units) QO =0.8763E+00 MO =0.7727E+01 JO Associated length scales (meters) LQ = 0.32 LM = 51.10 Lm Lmp NON -DIMENSIONAL PARAMETERS FRO = 152.60 R = 58.06 FLOW CLASSIFICATION 111111111111111111iiiiii111111111111111111 1 Flow class (CORMIXI) = NH5 1 1 Applicable layer depth HS = 1.52 1 111111111111111111111111111111111111111111 =-.8226E-02 SIGNJO= -1.0 18.30 Lb = 2.35 99999.00 Lbp = 99999.00 MIXING ZONE / TOXIC DILUTION / REGION OF INTEREST PARAMETERS CO =0.1000E+03 CUNITS= o NTOX = 0 NSTD = 0 REGMZ = 1 REGSPC= 2 XREG = 0.00 WREG = XINT = 2000.00 XMAX = 2000.00 X-Y-Z COORDINATE SYSTEM: 29.97 AREG = 0.00 ORIGIN is located at the bottom and below the center of the port: 38.10 m from the LEFT bank/shore. X-axis points downstream, Y-axis points to left, Z-axis points upward. NSTEP = 25 display intervals per module ----------------------------------------------------------------------------- ----------------------------------------------------------------------------- BEGIN MOD101: DISCHARGE MODULE COANDA ATTACHMENT immediately following the discharge. X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.25 END OF MOD101: DISCHARGE MODULE --------------------------------------------------------- BEGIN CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION Bottom -attached jet motion. UNSTABLE NEAR -FIELD: Jet/plume will mix over full layer depth. Following MOD133 will include recirculation into jet region. Profile definitions: B = Gaussian 1/e (37%) half -width, normal to trajectory Half wall jet, attached to bottom. S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C B 0.00 0.00 0.00 1.0 0.100E+03 0.18 0.52 0.00 0.00 1.0 0.100E+03 0.24 1.05 0.00 0.00 1.0 0.100E+03 0.29 1.58 0.00 0.00 1.2 0.849E+02 0.35 2.12 0.00 0.00 1.4 0.728E+02 0.41 2.65 0.00 0.00 1.6 0.637E+02 0.46 3.19 0.00 0.00 1.8 0.566E+02 0.52 3.72 0.00 0.00 2.0 0.509E+02 0.57 4.25 0.00 0.00 2.2 0.463E+02 0.63 4.79 0.00 0.00 2.4 0.424E+02 0.68 5.32 0.00 0.00 2.6 0.391E+02 0.74 5.85 0.00 0.00 2.8 0.363E+02 0.79 6.39 0.00 0.00 3.0 0.338E+02 0.85 6.92 0.00 0.00 3.2 0.317E+02 0.90 7.44 0.00 0.00 3.3 0.299E+02 0'.95 7.97 0.00 0.00 3.6 0.282E+02 1.01 8.50 0.00 0.00 3.8 0.267E+02 1.06 9.04 0.00 0.00 4.0 0.253E+02 1.11 9.57 0.00 0.00 4.2 0.241E+02 1.16 10.10 0.00 0.00 4.4 0.230E+02 1.22 10.64 0.00 0.00 4.6 0.219E+02 1.27 11.17 0.00 0.00 4.8 0.210E+02 1.32 11.70 0.00 0.00 5.0 0.202E+02' 1.37 12.24 0.00 0.00 5.2 0.194E+02 1.42 12.77 0.00 0.00 5.4 0.186E+02 1.47 13.30 0.00 0.00 5.6 0.180E+02 1.52 Cumulative travel time = 3.7028 sec END OF CORJET (MOD110): JET/PLUME NEAR -FIELD MIXING REGION ------------------------------------------------------------------ ---------------------------------------------------------------- BEGIN MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING Control volume inflow: X Y Z S C B 13.30 0.00 0.00 5.6 0.180E+02 1.52 Profile definitions: BV = layer depth (vertically mixed) BH = top -hat half -width, in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic average (bulk) dilution C = average (bulk) concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 11.78 0.00 0.00 5.6 0.180E+02 0.00 0.00 0.00 0.00 12.09 0.00 0.00 5.6 0.180E+02 1.52 0.42 1.52 0.00 12.39 0.00 0.00 5.6 0.180E+02 1.52 0.59 1.52 0.00 12.69 0.00 0.00 5.6 0.180E+02 1.52 0.72 1.52 0.00 13.00 0.00 0.00 5.6 0.180E+02 1.52 0.83 1.52 0.00 13.30 0.00 0.00 5.6 0.180E+02 1.52 0.93 1.52 0.00 13.61 0.00 0.00 5.9 0.170E+02 1.52 1.02 1.52 0.00 13.91 0.00 0.00 6.6 0.151E+02 1.52 1.10 1.52 0.00 14.22 0.00 0.00 7.3 0.138E+02 1.52 1.18 1.52 0.00 14.52 0.00 0.00 7.6 0.131E+02 1.52 1.25 1.52 0.00 14.83 0.00 0.00 7.8 0.128E+02 1.52 1.32 1.52 0.00 Cumulative travel time = 5.9833 sec END OF MOD133: LAYER BOUNDARY IMPINGEMENT/FULL VERTICAL MIXING ---------------------------- 7------------------------------------------------ ----------------------------------------------------------------------------- BEGIN MOD153: VERTICALLY MIXED PLUME IN CO -FLOW Phase 1: Vertically mixed, Phase 2: Re -stratified Phase 1: The plume is VERTICALLY FULLY MIXED over the entire layer depth. Profile definitions: BV = layer depth (vertically mixed) BH = Gaussian 1/e (370) half -width in horizontal plane normal to trajectory ZU = upper plume boundary (Z-coordinate) ZL = lower plume boundary (Z-coordinate) S = hydrodynamic centerline dilution C = centerline concentration (includes reaction effects, if any) X Y Z S C BV BH ZU ZL 14.83 0.00 0.00 7.8 0.128E+02 1.52 1.26 1.52 0.00 21.36 0.00 0.00 9.6 0.104E+02 1.52 1.88 1.52 0.00 27.90 0.00 0.00 11.2 0.896E+01 1.52 2.49 1.52 0.00 34.43 0.00 0.00 12.5 0.800E+01 1.52 3.09 1.52 0.00 40.97 0.00 0.00 13.7 0.729E+01 1•.52 3.68 1.52 0.00 47.51 0.00 0.00 14.8 0.674E+01 1.52 4.26 1.52 0.00 54.04 0.00 0.00 15.9 0.630E+01 1.52 4.84 1.52 0.00 60.58 0.00 0.00 16.8 0.594E+01 1.52 5.40 1.52 0.00 67.11 0.00 0.00 17.8 0.563E+01 1.52 5.96 1.52 0.00 73.65 0.00 0.00 18.6 0.536E+01 1.52 6.51 1.52 0.00 80.18 0.00 0.00 19.5 0.513E+01 1.52 7.06 1.52 0.00 86.72 0.00 0.00 20.3 0.493E+01 1.52 7.60 1.52 0.00 93.25 0.00 0.00 21.1 0.475E+01 1.52 8.13 1.52 0.00 99.79 0.00 0.00 21.8 0.459E+01 1.52 8.66 1.52 0.00 106.32 0.00 0.00 22.5 0.444E+01 1.52 9.18 1.52 0.00 112.86 0.00 0.00 23.2 0.431E+01 1.52 9.70 1.52 0.00 119.39 0.00 0.00 23.9 0.419E+01 1.52 10.22 1.52 0.00 125.93 0.00 0.00 24.6 0.407E+01 1.52 10.73 1.52 0.00 132.47 0.00 0.00 25.2 0.397E+01 1.52 11.24 1.52 0.00 139.00 0.00 0.00 25.8 0.387E+01 1.52 11.74 1.52 0.00 145.54 0.00 0.00 26.4 0.378E+01 1.52 12.24 1.52 0.00 152.07 0.00 0.00 27.0 0.370E+01 1.52 12.74 1.52 0.00 158.61 0.00 0.00 27.6 0.362E+01 1.52 13.23 1.52 0.00 165.14 0.00 0.00 28.2 0.355E+01 1.52 13.72 1.52 0.00 171.68 0.00 0.00 28.7 0.348E+01 1.52 14.21 1.52 0.00 178.21 0.00 0.00 29.3 0.341E+01 1.52 14.69 1.52 0.00 Cumulative travel time = 1225.1018 sec Entire region is occupied by Phase 1. Plume does not re -stratify in this flow region. END OF MOD153: VERTICALLY MIXED PLUME IN CO -FLOW ----------------------------------------------------------------------------- ** End of NEAR -FIELD REGION (NFR) ** The initial plume WIDTH values in the next far -field module will be CORRECTED by a factor 3.62 to conserve the mass flux in the far -field! The correction factor is quite large because of the small ambient velocity relative to the strong mixing characteristics of the discharge! This indicates localized RECIRCULATION REGIONS and internal hydraulic JUMPS. Width predictions show discontinuities, dilution values should be acceptable. The LIMITING DILUTION (given by ambient flow/discharge ratio) is: 24.8 This value is below the computed dilution of 29.3 at the end of the NFR. Mixing for this discharge configuration is constrained by LOW AMBIENT FLOW! The previous module predictions are unreliable since the limiting dilution cannot be exceeded for this shallow water discharge configuration. A subsequent module (MOD181) will predict the properties of the cross -sectionally fully mixed plume with limiting dilution and will compute a POSSIBLE UPSTREAM WEDGE INTRUSION. --------------------------------------------------------------------------- BEGIN MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION The DOWNSTREAM flow field for this unstable shallow water discharge is VERTICALLY FULLY MIXED. The mixing is controlled by the limiting dilution = 24.8 Channel DENSIMETRIC FROUDE NUMBER (FCHAN) for this mixed flow = 6.32 No upstream wedge intrusion takes place since FCHAN exceeds the critical value of 0.7. X Y Z S C BV BH ZU ZL 178.21 38.10 0.00 24.8 0.404E+01 1.52 89.92 1.52 0.00 Cumulative travel time = 1225.1016 sec VERTICALLY AND LATERALLY FULLY MIXED over layer depth: END OF SIMULATION! END OF MOD181: MIXED PLUME/BOUNDED CHANNEL/POSSIBLE UPSTREAM WEDGE INTRUSION ** REGULATORY MIXING ZONE BOUNDARY is within the Near -Field Region (NFR) ** In this prediction interval the TOTAL plume width meets or exceeds the regulatory value = 29.97 m. This is the extent of the REGULATORY MIXING ZONE. ----------------------------------------------------------------------------- CORMIXI: Submerged Single Port Discharges End of Prediction File 11111111111111111111111111111111111111111111111111111111111111111111111111111 f; ;. Ro Low -flow characterisOcs'for Yadkin River in vicinity of Salisbury Subject: Low -flow characteristics for Yadkin River in vicinity of Salisbury From: John C Weaver <jcweaver@usgs.gov> Date: Thu, 9 Feb 2006 08:34:23 -0500 To: jackie.nowell@ncmail.net CC: John C Weaver <jcweaver@usgs.gov> Jackie, In response to your request for a review of recent information and correspondence pertaining to the 7Q10 low -flow discharge for Yadkin River near Salisbury intake and discharge points, the following is provided: (1) The 7Q10 discharge of 1,030 cfs for Yadkin River at U.S. Highway 29 near Salisbury (station id 02121031, drainage area 3,452 sqmi) is based on the flow characteristics at a discontinued gaging station Yadkin River near Salisbury (station id 02121000, drainage area 3,450 sqmi), operated 1895-1927. According to information in our annual data reports, High Rock Lake was put into operation in November 1927, obviously being the cause of the gage's discontinuation. Considering also that W. Kerr Scott Reservoir did not exist until January 1963, this flow estimate would be reflective of more natural -flow conditions in the river at that location. With regard to an updated 7Q10 discharge for the Hwy 29 location (station 02121031), the site is within the upper end of High Rock Lake, meaning that flow dynamics are affected more by the circulation patterns of the lake as opposed to the riverine-type dynamics. Therefore, the 7Q10 discharge should not regarded as a proper measure of low -flow characteristics in this type of setting. (2) 1 reviewed the memorandum you forwarded from ENSR. The information presented in Table 1 is consistent with that provided by myself to ENSR in Fall 2003. However, I could not duplicate part of the information presented in Tables 2 and 3, although the concept described in the memorandum appears to be consistent with the USGS methods for ungaged sites (that is, pro -rating flow characteristics by drainage area). That may be due to differences in drainage -area values that we have in our office and those used by ENSR. For instance, in Table 2, the scaling factor for Yadkin College is listed as 1.03, compared to 1.08 based on information here at the USGS (2460 sqmi just above S Yadkin confluence / 2280 sqmi at 02116500 Yadkin College gage). The inclusion of drainage -area values at the "point of prediction" mentioned in the memorandum would help to make further comparisons as needed. (3) When estimating the low -flow characteristics for locations having large drainage areas, one of the challenges in applying the method of pro -rated low -flow yields is how much "detail" should be included when assessing the available upstream gages. For instance, should one just pro -rate using the closest upstream gage -or- divide the drainage area according to the available streamgages within the basin before pro -rating low -flow yields. The memorandum indicates that the latter approach was used by ENSR, regarded by USGS as an acceptable approach. (4) In April 1993, the USGS estimated low -flow characteristics for Yadkin River near Ellis Crossroads (station id 0212084025, drainage area 3,370 sqmi), located about 0.75 mile upstream from Grants Creek. The estimates were based on the low -flow yields at the Yadkin College gage and South Yadkin River near Mocksville gage (station id 02118000) combined with regional regression relations provided in USGS Water -Supply Paper 2403 "Low -flow characteristics of streams in North Carolina". The 7Q10 was estimated at 872 ,cfs, and the low -flow yields applied in this determination are reflective of the period of records prior to the 1998-2002 drought. Applying updated post -drought 7Q10 low -flow discharges for the upstream gages while using the same computational approach, the 7Q10 is estimated to be 754 cfs, very comparable to the 735 cfs estimated by ENSR for the discharge location below the confluence. 1 of 2 2/9/2006 9:13 AM Low -flow characteristics for Yadkin River in vicinity of Salisbury (5) Two other approaches that involves pro -rating the South Yadkin basin on the basis of the Mocksville gage and Hunting Creek near Harmony (station id 02128500, drainage area 155 sgmi) result in 7Q10 estimates ranging from 780 to 791 cfs. (6) As previously discussed, no information is, -immediately available to determine how far upstream the headwaters of High Rock Lake extend up the Yadkin River and possibly the South Yadkin River. Examination of USGS topographic data using mapping software suggest that some backwater influence at normal lake levels may exist at the confluence. However, it is plausible to consider that, during 7Q10 flow conditions during extended dry periods, the lake levels would likely be lower as well, meaning the reach of Yadkin River between the confluence and Grants Creek may not be in the backwater of the lake. In summary, it appears the most appropriate determination of a reasonable and updated 7Q10 for the Yadkin River between the South Yadkin River confluence and Grants Creek is a range from 750 to 800 cfs. This range of estimates does not account for any backwater effects of High Rock Lake that may exist during low -flow periods. Hope this information is helpful. Please feel free to contact me if you have questions or need further discussion. Thank you. Curtis Weaver *********************************************************************** J. Curtis Weaver, Hydrologist, PE USGS North Carolina Water Science Center 3916 Sunset Ridge Road Raleigh, NC 27607 Telephone: (919) 571-4043 H Fax: (919) 571-4041 E-mail address -- jcweaver@usgs.gov Internet address -- http://nc.water.usgs.gov/ 2 of 2 2/9/2006 9:13 AM Awox A, A-coll Ali- w"� iw) Iz+t( �1✓ Ma,� wsnl. D 444- 3 AI�C'k �636 za-w SfA'(1 Ln.d 1 G'� /,*r 5 TECHNICAL REPORT Salisbury -Rowan WWTP Yadkin River Diffuser CORMIX Analysis January 2006 Background In order to assign an in -stream waste concentration (IWC) used in the NPDES permit for Salisbury -Rowan WWTP, NCDENR uses CORMIX to establish a dilution factor. Based on recent CORMIX analysis, there is strong evidence that the existing Yadkin River Diffuser (Diffuser) is designed for flows much greater than those included in Salisbury -Rowan WWTP NPDES Permit. This technical report is directed at evaluating modifications to the Diffuser that improve effluent mixing based on CORMIX modeling. Data and Methodology The CORMIX model uses input data and parameters classified into four categories: Stream Characteristics, Effluent Characteristics, Diffuser Characteristics and Regulatory Mixing Zone. Stream Characteristics: The Yadkin River at the Diffuser was modeled as having a uniform, bounded cross-section with steady, unidirectional flow of 735 cubic feet per second (cfs). Attached in Appendix 1 is a 2003 report prepared by ENSR to evaluate low flow conditions on the Yadkin River at Salisbury's Water Intake and at the Diffuser. Default values were used for Manning N, wind velocity and water temperature. NCDENR requested Salisbury -Rowan Utilities (SRU) to evaluate stream characteristics based on conditions with High Rock Lake at full pond (623.9 feet NGVD 29) and with High Rock Lake 5 feet below full pond. From 1997 Alcoa Bathymetry and Diffuser record drawings, the average bottom elevation is approximately 614 feet. This gives an average water depth of 10 feet at High Rock Lake full pond and average water depth of 5 feet at High Rock Lake 5 feet below full pond. Using 2003 aerial photography, the cross-section width was measured to be 335 feet at full pond and 295 feet at 5 feet below full pond. The stream characteristic inputs are summarized in Table I below: Table 1 Stream Characteristics Flow Rate (cfs) Manning Wind Velocity (m/s) Water Temp (°C) Depth (ft) Width (ft) Bounded Cross-Section/Uniform Steady Flow Rate 735 0.03 2 25 10 5 335 295 Effluent Characteristics: Salisbury -Rowan WWTP's NPDES permit has two discharge limits, 12.5 million gallons per day (mgd) and 20 mgd. Laboratory analysis documents the effluent density to be 998 kg/m3. The effluent is not diluted before discharge to ,the Yadkin River, therefore a discharge concentration of 100% was used. The effluent characteristic inputs are summarized in Table 2 below. Table 2 Effluent Characteristics Flow Rate (mgd) Density (kg/m3) Concentration (%) 12.5 20 998 998 100 100 Diffuser Characteristics: The Diffuser record drawings were used to complete the diffuser characteristic inputs. The nearest bank is to the left looking downstream. The port height is approximately 1 foot above the sand bottom. The closest port to the left bank is 140 feet at full pond and 125 feet at 5 feet below full pond. The diffuser is configured with three 14-inch ports with separation of 10 feet on -center for a diffuser length of 20 feet. The farthest port from the left bank is 160 feet at full pond and 145 feet at 5 feet below full pond. The diffuser pipe is cross -current for a gamma angle of 90°. Each port has one nozzle that is pointed horizontally downstream (theta is 0°, sigma is 0°) and is oriented at 90' relative to the diffuser pipe (beta). To improve effluent mixing, the diffuser modifications considered were (1) the replacement of the three 14" ports with three 8" ports and (2) cap two ports to leave a single 14" port. The diffuser characteristic inputs are summarized in Table 3 below. Table 3 Diffuser Characteristics Nearest Bank Port Height (ft) Nearest Endpoint (ft) Type Length (ft) Farthest Endpoint (ft) Port Diameter (ft) (in) Number of Ports Nozzles per Port Gamma (deg) Theta (deg) Sigma (deg) Beta (deg) Left 1 140 125 Multi Multi Single Multi Multi Single 20 20 - 20 20 - 160 160 - 145 145 - 1.167 (14) 0.667 (8) 1.167 (14) 1.167 (14) 0.667 (8) 1.167 (14) 3 3 1 3 3 1 1 1 - 1 1 - 90 90 - 90 90 - 0 0 0 0 0 0 0 0 0 0 0 0 90 90 - 90 90 - Regulatory Mixing Zone: Based on review of previous CORMIX models for the Diffuser and discussions with NCDENR, it was agreed that the appropriate measure for the regulatory mixing zone is a plume width to channel width ratio of 1/3. Page 2 of 4 Results and Conclusions A total of 12 CORMIX models were run to cover the combinations of water level, effluent discharge and diffuser configuration. When evaluating the regulatory mixing zone based on plume to channel width, the plume widths reported in the session reports were incorrect giving inaccurate pollutant concentrations; therefore the regulatory mixing zone reported in the prediction files were used for the summary tables below. Current Diffuser Configuration: A series of four models were executed using the current diffuser configuration (three 14" ports) to cover flows of 12.5 mgd and 20 mgd and water levels of High Rock Lake full pond and High Rock Lake 5 feet below full pond. The session reports and prediction files are included in Appendices 2-5 and are summarized in Table 4 below. Table 4 Pollutant Concentration (%) Dilution Factor Discharge Velocity (m/s) 12.5 mgd 12.5 mgd 20 MGD 20 MGD Full Pond 5 ft below FP Full Pond 5 ft below FP 8.4 9.6 6.4 6.8 11.9 10.4 15.7 14.7 1.84 1.84 2.94 2.94 Alternate 1 Configuration: A series of four models were executed using Alternate 1 diffuser configuration (three 8" ports) to cover flows of 12.5 mgd and 20 mgd and water levels of High Rock Lake full pond and High Rock Lake 5 feet below full pond. The session reports and prediction files are included in Appendices 6-9 and are summarized in Table 5 below. Table 5 Pollutant Concentration (%) Dilution Factor Discharge. Velocity (m/s) 12.5 mgd 12.5 mgd 20 MGD 20 MGD Full Pond 5 ft helow FP Full Pond 5 ft below FP 2.7 3.8 3.0 4.3 36.7 26.6 33.4 23.5 5.62 5.62 9.0 9.0 Alternate 2 Configuration: A series of four models were executed using Alternate 2 diffuser configuration (single 14" port) to cover flows of 12.5 mgd and 20 mgd and water levels of High Rock Lake full pond and High Rock Lake 5 feet below full pond. 'The session reports and prediction files are included in Appendices 10-13 and are summarized in Table 6 below. Table 6 Pollutant Concentration (%) Dilution Factor Discharge Velocity (m/s) 12.5 mgd 12.5 mgd 20 MGD 20 MGD Full Pond 5 ft below FP Full Pond 5 ft below FP 2.3 5.3* 2.4 3.4 42.7 18.9 41.7 29.3 5.51 5.51 8.82 8.82 * This result as reported in the model is incorrect. The correct concentration is 3.2%. Page 3 of 4 Conclusions: It is evident from the results in Table 4 that more complete mixing occurs at higher effluent discharge rates, illustrating that the existing configuration was designed for flows much greater than those included in the Salisbury -Rowan WWTP NPDES permit. To improve effluent mixing, the two alternatives considered are to reduce the port size or to reduce the number of ports. From the results in Tables 5 and 6, it is clear that either solution will achieve nearly equally desirable results. It is interesting to note the inconsistency in the result for 12.5 mgd effluent flow with water depth at 5 feet below High Rock Lake full pond, which is reported as a pollutant concentration of 5.3%. This occurs at a calculation segment boundary that increases the plume width by a factor of 3.77 (from 11.6 m to 43.6m) to conserve mass flux for the next calculation segment (see appendix 11). Considering the change in effluent concentration in the other 5 pairs where water level is changed, but flow is held constant; the correct concentration works out to be 3.2%. When cost, discharge velocity and mixing performance are considered, Salisbury -Rowan Utilities proposes to make improvements to the Yadkin River Diffuser consistent with the modifications modeled in Alternative 2. Two of the existing ports will be capped, leaving one existing 14" diffuser port. The port nearest the center of channel will remain in service. Based on the proposed modifications, SRU calculates the new in -stream waste concentration to be 3.2% (31.3 dilution factor) for 12.5 mgd effluent discharge. If the same diffuser configuration were used for 20 mgd effluent discharge, the in -stream waste concentration will be 3.4% (29.3 dilution factor). Page 4 of 4 REASONABLE POTENTIAL ANALYSIS Salisbury - Rowan WWTP NCO023884 Time Period 112003-10/2004 Qw (MGD) 12.5 WWTP Class IV 7Q10S (cfs) 263.5 IWC (%) @ 7QIOS 6.8493 7Q10W(cfs) 0 ®7Q10W WA 30Q2 (cfs) 0 ® 30Q2 WA Avg. Stream Flow, QA (cfs) 4879 @ QA 0.3955 Rec'ving Stream Yadkin River Stream Class WS-V Outfall 001 Qw=12.5MGD STANDARDS & PARAMETER TYPE CRITERIA (2) POL Units REASONABLE POTENTIAL RESULTS PRELIM. RESULTS RECOMMENDED ACTION- i1I NC WQS1 ➢,FAV( a /Dot. MaxPredCw Allowable Cw Chronic Acute Acute: N/A No acute standard or 112 FAV Arsenic NC 50 ug/L 12 0 9.2 _ _ ___ __ Chronic: 730 ___ _ _ _WA_ _ _ __ MaxPredCw < Chronic No action all values telow, detection MONITOR? Acute: 15 MaxPredCw < Acute Cadmium NC 2 15 ug/L 15 1 5.4 MONITO_RT_ _ _ ___ __ Chronic: 29 ___ _ _ __ MaxPredCw < Chronic No action 14 of 15values below detaction ' MONITOR? Acute: 1,022 MaxPredCw < Acute Chromium NC 50 1,022 ug/L 12 4 309.7 MONITOR? _ Chronic: 730 _ MaxPredCw < Chronic No action no exceedance of allowableconc MONITOR? Acute: 7 MaxPredCw > Acute Conknue'2/mohth rnondornng - Copper NC 7 AL 7.3 ug/L 55 11 79.0 D_AIL_Y MAX_LIM_IT? __ _ ___ _ Chronic: 102 __ MaxPredCw < Chronic __ MONITOR? Acute: 22 MaxPredCw < Acute Drop quarterlyinonitonng Cyanide NC 5 N 22 10 ug/L 34 1 13.9 MONITOR? ___ __ Chronic: 73 ___ _ _ __ MaxPredCw< Chronic MONITOR? _ Acute: 34 MaxPredCw < Acute No action no exceedance of allowable conc: , - -. Lead NC 25 N 33.8 'ug/L 15 2 24.1 _ _ __ MONITOR? __ Chronic: 365 ___ _ _ __ MaxPredCw < Chronic _ MONITOR? -^s Acute: N/A No acute standard or 1/2 FAV Mercury NC 0.012 0.0002 ug/L 16 2 12452 ------------------WA----------- Chronic: 0.18 MaxPredCw >Chronic Add 2/month mondormg unLIDWQ strategy finalized MO AVG LIMIT? Acute: 261 MaxPredCw <Acute No action no exbeedahce of allowable conc ,, Nickel NC 88 261 ug/L 16 1 11.9 MONITOR? _ _ ___ __ Chronic: 1,285 ___ _ _ __ MaxPredCw < Chronic _ __"' MONITOR? Acute: 56 MaxPredCw > Acute Add' dailymaxtmum'limitmax. pred Exceeds allowable col Selenium NC 5.0 56 ug/L 15 2 300.0 D_AIL_Y M_AX_LIM_IT7 _ Chronic: 73 __ MaxPredCw > Chronic _ $ �'. MO AVG LIMIT? Acute: - 1 - MaxPredCw > Acute Continue 2/month monitoring Silver NC 0.06 AL 1.23 ug/L 57 3 10.8 DAILY MAX __ _ ___ __ Chronic: 1 ____ MaxPredCw>Chronic MO AVG LIMIT?i s Acute: 67 MaxPredCw > Acute Add 2Jmonth monitonr g Zinc NC 50 AL 67 ug/L 17 13 181.1 ------------------DAILY-- MAX_LIM_IT? __ __;� =_ _ - �> •Q`; Chronic: 730 MaxPredCw < Chronic .. MONITOR? Legend: " Freshwater Discharge C = Carcinogenic NC = Non -carcinogenic A = Aesthetic 23884.rpa2004, rpa 11/14/2005 d4j) City of Salisbury Permit Meeting November 15, 2005 Archdale Building Raleigh NC Introductions • City of Salisbury • Division of Water Quality Discussion on NPDES Permit Comments • Treatment train description • Selenium limit/monitoring ✓ 7j y�. w�'� ,,,�✓ • Mercury limit/monitoring • Instream Waste Concentration/ 7Q10 IWC calculated from dilution of CORMIX model J ..�f At 12.5 MGD, dilution of 14.6:1, 1/14.6 *100 = 6.85% At 20 MGD, dilution of 15.5:1, 1/15.5* 100=6.45% 7Q10 flow used in 1995 CORMIX model — 1030 cfs Calculation of effective 7Q10 — a back calculation from the dilution ratio Final Decisions Conclusion/Remarks s�� `f d'�?I�,•rC7n�i �rrvC�T� 16 pAr �lf Gib% at ?V,441"✓ put-i. S , ����At City of Salisbury Permit Meeting November 15, 2005 Archdale Building Raleigh NC I. Introductions ■ City of Salisbury ■ Division of Water Quality II. Discussion of draft NPDES Permit Y ■ Treatment train description ■ Added four primary clarifiers and two tricklingfilters ilters V ■ Copper, silver and zinc monitoring reduction ■ Because of your good toxicity test results, recommend reduction from 2/month to 1/month monitoring v ■ Selenium delayed limit/monitoring A delayed daily maximum limit of 56 u 1 will begiven. Facility will be given a 15/18 month compliance schedule to find sources of Se. Will sample monthly during this schedule. Can resubmit Se data (12 datapoints) for reevaluation of RPA to see if limit would still be needed. v ■Annual effluent pollutant scan Per 40 CFR 122.21, Spec.cond. will be added to permit requiring_ pollutant scans so that data can be submitted at next permit renewal. and it. EPA o Reevaluation shows that hits in Feb. 2002 but 35 below detects since that time. EPA has agreed that facility does have to limit but must monitor for at least 12 months at the Method 1631E for reevaluation of RPA. JM Dilution/IWC City of Salisbury Permit Meeting November 15, 2005 Archdale Building Raleigh NC I. Introductions ■ City of Salisbury ■ Division of Water Quality . II. Discussion of draft NPDES Permit ■ Treatment train description ■ Copper, silver and zinc monitoring reduction ■ Selenium delayed limit/monitoring ■ Annual effluent pollutant scan ■ Dilution and Mercury monitoring III. Final Remarks/Conclusion US M. Final Remarks/Conclusion G144-8 ojf,� -K Y� � Z61, uo a `"45r tt r 14, 1 "4s ,5ul,94� ;�ai�z r Cv4,- 71. dj,4.� Js aft G�� r a WW tw ov -- --d �- lip U -- j cJkw— //, tt �-ie. �c E✓rtic t 9¢= Kruger Amended Fact Sheet - NPDES Permit Salisbury -Rowan WWTP NPDES No. NCO023884 Faculty; Receivina Stream Facility Name: Salisbury — Rowan WW,I,P Receiving Stream: Yadkin Rivet Permitted Flow (MGD): 12.5 MGD Subbasin: 030704 Facility Class: IV Index No.: Facility Status: Existing Stream Class: WWS-V Permit Status: Renewal 303(d) Listed: No County: Rowan Use Support: Regional Office: Mooresville Drainage Area (m12): 3,377 USGS Topo Quad: E17NW Summer 7010 (cfs) 1030 cfs Salisbury, NC Effective 7010 263.5 cfs (based on 14.6:1 dilution instream) Average Flow (cfs): 4,879 IWC (%): 6.85 Facf ht Receiving .Stream Facility Name: Salisbury — Rowan WW,� Receiving Stream:- Yadkin Rivet Permitted Flow (MGD): 20.0 MGD Subbasin: 030704 Facility Class: IV Index No.: Facility Status: Existing Stream Class: CIS-V Permit Status: Renewal 303(d) Listed: No County: Rowan Use Support: Regional Office: Mooresville Drainage Area (mi2): 3,377 USGS Topo Quad: E17NW Summer 7070 (cfs) 1030 cfs Salisbury, NC Effective 7010 449.5 cfs (based on 15.5:1 dilution instream) Average Flow (cfs): 4,879 IwC (%): 6.45 E Corrections to the Factsheet Per EPA comment the following paragraph should be corrected to include the last sentence: Salisbury has a full pre-treatment program, with 4 SIUs (Significant Industrial Users) and 5 CIUs (Categorical Industrial Users) per its application. DWQ recommends that Salisbury continue to implement the full pretreatment program and its Long Term Monitoiring Plan through the renewed permitting cycle. Salisbury Comments on the draft permit 1. Request that limitations/monitoring for selenium is dropped: The 35 ug/l sample in 2004 is not representative of the Salisbury effluent and should not be considered in the analysis of effluent data. All other values are below detection. Recommend that it be monitored (quarterly) in the LTMP. DWQ response: The 35 ug/1 sample in May 2004 was reported in an amended DMR submitted by Salisbury in November 2004. Due to problems with instruments, metals and other parameters were not run in time to report on the correct DMR. The data was reported as part of LIMP. The City did not report that sample was not representative at the time of its submittal. No information from lab that indicated that sample was contaminated. Recommend that facility have delayed limit for selenium, with 12-month compliance schedule with monthly monitoring for selenium and limit will become effective twelve months from effective date of the permit. If Salisbury submits 12 data points and the data does not show reasonable potential to exceed the allowable concentration then selenium limit/monitoring in the NPDES permit will be dropped. 2. Request that monitoring for mercury is dropped: The hits (0.4 and 0.3 ug/1) in 2002 are not representative of the Salisbury effluent. Recommend that it be monitored quarterly in the LTMP. All other values are below detection. EPA response: Interim objection to the permit (rec'd 2/4/2005) due to RPA showing that Hg limit should be given but only monitoring given and question that facility should be using Method 1631E in its analysis. After discussion of these issues in a January 27 2005 telecon, EPA recommended that facility have a delayed mercury limit of 0.180 ug/1 with a 18 month compliance schedule, if collected data shows no RP, then limit/monitoring in the NPDES will be dropped. Need to address the mercury sampling method and resolve. DWQ response: Recommend a delayed mercury limit with a 12-month compliance schedule, if collected data shows no RP, then limit/monitoring in the NPDES will be dropped. 3. Correction of the instream waste concentration based on a normal calculation that reflects the actual, documented riverine conditions at the diffuser and the 7Q10 of 833 cfs at the diffuser. DWQ response: Background on development of Salisbury effluent limits. CORMIX model used by DWQ in 1995. Objective was to predict mixingand develop effluent limits for alternative outfall designs. Design conditions: combination of riverine and lacustrine conditions 7Q10 = 1030 cfs (29.1 m3/s) Full pool scenario used to develop toxics limits. Mixing zone not to exceed 1 /3 of channel width. Standard must be met at edge of mixing zone. 6 Toxics limits based on dilution at the edge of mixing zone. To improve mixing between the effluent and the Yadkin River. Salisbury constructed a 3 port diffuser with a minimum 14.6 :1 dilution ratio at 12.5 MGD. At 12.5 MGD, dilution is 14.6:1 (based on CORMIX model results), Dilution = 1/IWC , IWC = 0.0685 * 100 = 6.85% The effective 7Q10 at 14.6:1 is 263.5 cfs, which is backcalculated from the dilution ratio. This effective 7Q10 is used as input for analysis of metals limits. At 20 MGD, dilution is 15.5:1 (based on CORMIX model results), Dilution = 1 /IWC, IWC = 0.0645 * 100 = 6.45% The effective 7Q10 at 15.5:1 dilution ratio, is 449.5 cfs, which is backcalculated from the dilution ratio. This effective 7Q10 will be used as input for analysis of metals limits. Therefore, at 12.5 MGD, the IWC=7% and at 20 MGD, the IWC is 6%. Note: An error was made in the previous permit when the effective 7Q10 of 263.5 cfs (instead of 449.5 cfs) was also used for the expansion flow of 20 MGD. The incorrect IWC of 10.5% at 20 MGD was listed in the previous permit and whole toxicity testing requirement. The correct IWC of 6.45% —6% will now be used. 4.Correction of the description of the Grant Creek Treatment train. DWQ response: Will include four (4) primary clarifiers and two (2) trickling filters on the permit supplement cover page. Jmn—11/14/2005 7 Additional info for Salisbury -Rowan WWTP permit 1/27/05 - Call to Marshall Hyatt at EPA, Region IV, Marshall had reviewed the mercury strategy develop by Tom Belnick and it made sense. l Craig ??? looked at the TMDL p.37 last paragraph indicated that limits will be given. EPA recommended solutions: 1) Do a delayed limit of 18 months 2) Sample influent (source water) and effluent Hg levels to show that they are not adding Hg to the stream. Salisbury — has dilution allowed into the Yadkin River. Need to used method 16313 Offer a delayed limit for 18 months. If they are below 180 ng/l, then the limit will be removed. In Region IV, everyone is doing (?) — method 1631 ??? • Resolve the 163le issue with Salisbury • Run quickly and get the data points. Tom B. asked if there were any variances for Hg with other states. ---Marshall did not know the answer to that question. Final result: DWQ is going to receive an interim objection letter for Salisbury NPDES received a copy of objection letter (dated Jan. 31, 2005) on Feb. 4, 2005. Salisbury cc'd on letter. 2/17/2005- Received Salisbury comments on the draft permit. 1) want Hg and Se monitoring deleted 2) Want the Se limit deleted. 3) Want IWC based on normal calculations and to reflect the riverine conditions and the 7Q10 = 733 cfs. They do not want to run the CORMIX. The Division has said that a CORMIX model needs to be run. REASONABLE POTENTIAL ANALYSIS Salisbury - Rowan WWTP NCO023884 Time Period 112002-5/2005 Qw (MGD) 20 7Q10S (cls) 449.5 7Q10W (C/s) 0 3002 (Cis) 0 Avg. Stream Flow, QA (cis) 4879 RecWng Stream Yadkin River WW FP Class IV IWC(%) ®7010S 6.4516 ® 7Q10W N/A ® 3002 N/A ® QA 0.6314 Stream Class WS-V Outfal 1001 Ow=20MGD STANDARDS& PARAMETER TYPE CRITERIA (2) POL Units REASONABLE POTENTIAL RESULTS PRELIM. RESULTS RECOMMENDED ACTION NC WQS/ Yi FAVr n ADet. MaxPredCw Allowable Cw (1) Chronic Acote Acute: N/A No acute standard or 1/2 FAV Arsenic NC 50 ug/L 12 0 9.2 WA ------' - - =----------- ------------ ----------- Chronic: 775 ----'—'—'----------- MaxPredCw . Chronic No action, all values below detection MONITOR? Acute: 15 MaxPredCw < Acute Cadmium NC 2 15 ug/L 15 1 5.4 MONITOR? _ ___ _ _ _ _ _ _ _ ------------- _ Chronic: 31 ___ _ MaxPredCw < Chronic No action, 14 of 15 values below. detection MONITOR? Acute: 1,022 MaxPredCw < Acute - - Chromium NC 50 1.022 ug/L 12 4 309.7 MONITOR? --'—'---'—' Chronic: 775 '-----------------'— MaxPredCw < Chronic -------'---------------------'---- No action, noexceedance of allowable conc. MONITOR? Acute: 7 MaxPredCw > Acute Continue 2/monthmonitoring Copper NC 7 AL 7.3 ug/L 55 11 79.0 ----------- DAILY MAX LIMIT? --—'—'—'—'—'----- — ------ ------------- --'=-----_- Chronic: 109 MaxPredCw . Chronic , MONITOR? Acute: 22 MaxPredCw < Acute Drop quarterly monitoring -. Cyanide NC 5 N 22 10 ug/L 34 1 13.9 ---- MONITOR? ----------------- - ------------------------------ ------ Chronic: 78 MaxPredCw < Chronic MONITOR? Acute: 34 MaxPredCw < Acute No action, no exceedanca of allowable conc.. Lead NC 25 N 33.8 ug/L 15 2 24.1 MONITOR? -_-_-__________ - -------- -__- __-___-___-__--____ _____-_-___ Chronic: 388 __ MaxPredCw. Chronic MONITOR? - Acute: N/A No acute standard or 1/2 FAV - - Mercury NC 0.012 0.0002 ug/L 16 2 1.2452 ...................... WA _ _ _ _ ------------------------------- Chronic: 0.19 MaxPredCw > Chronic Add 2/month monitoring, until DWO strategy finalized.. MO AVG LIMIT? Acute: 261 .MaxPredCw. Acute Noaction, no exceedance,of. allowable conc. .. Nickel NC 88 261 ug/L 16 1 11.9 ----------- MONITOR? ------'-'-T ------ Chronic: 1,364 MaxPredCw .Chronic --=-------.------.---------------- MONITOR? - Acute: 56 MaxPredCw > Acute Add daily maximum limit, max. pred. Exceeds allowable coi Selenium NC 5.0 56 ug/L 15 2 292.5 DAILY MAX LIMIT? ----------'—'—'----- - --'---'---' Chronic: 78 MaxPredCw>Chronic -----------'---------------------'- MO AVG LIMIT? Acute: 1 MaxPredCw > Acute Continue 2/month monitoring ,. Silver NC 0.06 AL 1.23 ug/L 57 3 10.8 ----------- DAILY MAX LIMIT? --'-'-'-'----------- " ----- ------------------------- Chronic: 1 MaxPredCw > Chronic - MO AVG LIMIT? Acute: 67 MaxPredCw > Acute Add 21month monitoring Zinc NC 50 AL 67 ug/L 17 13 181.1 DAILY MAX LIMIT? _ - Chronic: 775 MaxPredCw . Chronic MONITOR? ;,- Legend: " Freshwater Discharge C = Carcinogenic NC = Non -carcinogenic A = Aesthetic 23884.rpa20mgd.updteff7g10, rpa 11/14/2005