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HomeMy WebLinkAboutNC0024236_Permit (Issuance)_20001228NPDE!► DOCUMENT SCANNING COVER SHEET NPDES Permit: NC0024236 Kinston Regional WWTP Document Type: Permit Issuance Wasteload Allocation Authorization to Construct (AtC) Permit Modification Complete File - Historical Engineering Alternatives (EAA) Correspondence Owner Name Change Monitoring Report Instream Assessment (67b) Speculative Limits Environmental Assessment (EA) Document Date: December 28, 2000 This document is printed on reuse paper - ignore any content on the reYerse side a Sate of North Carolina Department of Environment and Natural Resources Division of Water Quality James B. Hunt, Jr., Governor Bill Holman, Secretary Kerr T. Stevens, Director WA NCDENR NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES December 28, 2000 Mr. Henry D. McLean, Asst. Director of Public Utilites City of Kinston P.O. Box 339 Kinston, North Carolina 28501 Subject: Dear Mr. McLean: NPDES Permit Issuance Kinston Wastewater Treatment Plants Peachtree WWTP NPDES Permit Number NC0020541 Northside WWTP NPDES Permit Number NC0024236 Lenoir County In accordance with the application for discharge permit, the Division is forwarding herewith the subject NPDES 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. The Division of Water Quality received John Jarrell's comments, submitted on behalf of the City dated September 29, 2000, with regard to the draft permit. Historically, the lagoon mentioned in the letter was used to store sludge. As such, the Division considers any discharge from this treatment component to be unpermitted. Issuance of this final NPDES permit should not be construed as allowance of discharge from the lagoon. The stipulations of the NPDES permits for Kinston Peachtree and Northside WWTP must be met in addition to any requirements of the City's Judicial Order by Consent. Elimination and/or relocation of the outfall(s) to the Neuse River must take place prior to expiration of this permit and reissuance of the next permit. If any parts, measurement frequencies, or sampling requirements contained in this permit are unacceptable to you, you have the right to an adjudicatory hearing upon written request within thirty (30) days following receipt of this letter. This request must be in the form of a written petition, conforming to Chapter 150B of the North Carolina General Statutes, and filed with the office of Administrative Hearings, Mail Service Center 6714, Raleigh, North Carolina 27699-6714. Unless such a demand is made, this permit shall be final and binding. 1617 MAIL SERVICE CENTER, RALEIGH, NORTH CAROLINA 27699-1617 - TELEPHONE 919-733-5083/FAX 919-733-0719 AN EQUAL OPPORTUNITY AFFIRMATIVE ACTION EMPLOYER - 50% RECYCLED/ 10% POST -CONSUMER PAPER VISIT us ON THE WEB AT http://h2o.enr.state.nc.us/NPDES Y Mr. Henry D. McLean Page 2 4 r Please take notice that this permit is not transferable except after notice to the Division of Water Quality. The Division of Water Quality may require modification or revocation and reissuance of the permit. This permit does not affect the legal requirements to obtain other permits which may be required by the Division of Water Quality, the Division of Land Resources, the Coastal Area Management Act, or any other federal or local governmental permit. If you have any questions regarding the attached permits or you would like to discuss the above issues, please do not hesitate to contact Susan A. Wilson at telephone number (919) 733-5083, extension 510. Sincerely, Original Signed By David A. Goodrich Kerr T. Stevens w/attachments Cc: NPDES Permit File 9 Point Source Compliance and Enforcement Unit Central Files Washington Regional Office/ Water Quality Section Rob Brown, Construction, Grants & Loans EPA Region IV, Roosevelt Childress v Permit No. NC0024236 STATE OF NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES DIVISION OF WATER QUALITY PERMIT TO DISCHARGE WASTEWATER UNDER THE NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM In compliance with the provisions of North Carolina General Statute 143-215.1, other lawful standards and regulations promulgated and adopted by the North Carolina Water Quality Commission, and the Federal Water Pollution Control Act, as amended, City o, f Kinston Kinston - Northside Wastewater Treatment Plant is hereby authorized to discharge wastewater from a facility located at Kinston Northside WWTP Tower Hill Road and NC Hwy. 55 Kinston Lenoir County to receiving waters designated as an unnamed tributary to the Neuse River in the Neuse River Basin in accordance with the discharge limitations, monitoring requirements,, and other conditions set forth in Parts I, II, III, and IV hereof. This permit shall become effective February 1, 2001. This permit and the authorization to discharge shall expire at midnight on January 31, 2003. Signed this day December 28, 2000. Original Signed By David A. Goodrich Kerr T. Stevens, Director Division of Water Quality By the Authority of the Environmental Management Commission Kinston Northside WWTP NPDES No. NC0024236 Permit No. NC0024236 SUPPLEMENT TO PERMIT COVER SHEET City of Kinston Kinston Northside Wastewater Treatment PIant is hereby authorized to: 1. Continue to operate an existing 4.5 MGD wastewater treatment facility consisting of an influent pump station, fine filter screen and grit removal, 8 inch line to transfer sludge and/or wastewater from Peachtree to Northside, dual extended aeration basins, dual secondary clarifiers, chlorine disinfection, dechlorination with sulfur dioxide, cascade post aeration, aerobic digesters, sludge drying beds, caustic and alum storage/feed for chemical phosphorus removal located at Kinston Northside WWTP, Tower Hill Road & NC Hwy. 55, Kinston, Lenoir County, and 2. Discharge wastewater from said treatment works at the location specified on the attached map into an unnamed tributary to the Neuse River [see Part I, Condition A.(5.)1 which is classified C-NSW waters in Neuse River Basin. Kinston Northside NPUES No. NC0024236 1 11014 Latitude, 35°1715" 1 nngitude: 77°30'41" Quads F285E, Kinston 5tra lass: C NSW Ee�eiving_S,ream; Neuse River Permitt&LFiaw 4.5 MOD .•v City of Kinston/Northside WWTi' NCOD24236 s A. (1.) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS - FINAL During the period beginning on the effective date of the permit and lasting until expiration, the Permittee is authorized to discharge 4.5 MGD of municipal wastewater from outfall 001. Such discharges shall be limited and monitored by the Permittee as specified below: Effluent f luent Characteristics ' Limits Monitoring Requirements Monthly Average - Weekly Average Daily Maximum Measurement Frequency Sample Type Sample Locationl Flow 4.5 MGD Continuous Recording Influent or Effluent BOD, 5 day (20°C)2 [April 1- October 311 15 mg/I 22.5 mg/I Daily Composite Influent & Effluent BOD, 5 day (20°C)2 [November 1 - March 31 J 22 mg/I 33 mg/I Daily Composite Influent & Effluent Total Suspended Residue2 30.0 mg/1 45.0 mg/I Daily Composite Influent & Effluent NH3 as N [April 1- October 31] 8.0 mg/1 Daily Composite Effluent NH3 as N [November 1- March 31] 10.0 mg/I Daily Composite Effluent Dissolved Oxygen3 Daily Grab Effluent Dissolved Oxygen 3/Week Grab Upstream & Downstream Fecal Coliform (geometric mean) 200/100 ml 400/100 ml Daily Grab Effluent Fecal Coliform (geometric mean) 3/Week Grab Upstream & Downstream Total Residual Chlorine - 28 µg/I . 3/Week Grab Effluent Total Nitrogen 4 (NO2-N + NO3-N + TKN) No Effluent Limit (mg/I) • Weekly Composite Effluent No Effluent Limit (lb/month) Monthly Calculated Effluent 50,680 lb/year (Annual Mass Loading) 5 Annually Calculated Effluent Total Phosphorus 6 2.0 mg/L (Quarterly Average) Weekly Composite Effluent Temperature (°C) Daily Grab Effluent Temperature (°C) 3/Week Grab Upstream & Downstream Conductivity Daily Grab Effluent Conductivity 3/Week Grab Upstream & Downstream Chronic Toxicity? Quarterly Composite Effluent Copper Monthly Composite Effluent Zinc Monthly Composite Effluent pH8 6-9 Daily Grab Effluent (Footnotes on next page) Kinston Northside NVWTP NPDES No. NC0024236 A. (1.) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS - FINAL (Continued) Footnotes: 1. Sample locations: Upstream - least 100 ft. above outfall location on the Neuse River; Downstream - at Highway 55 bridge. Instream monitoring is provisionally waived in light of the permittee's participation in the Lower Neuse Basin Association. Instream monitoring shall be conducted as stated in this permit should the permittee end its participation in the Association. 2. The monthly average effluent BOD5 and Total Suspended Residue concentrations shall not exceed 15% of the respective influent value (85% removal). 3. The daily average dissolved oxygen effluent concentration shall not be less than 6.0 mg/1. 4. See Special Condition A. (2.), Total Nitrogen Monitoring. 5. The annual mass loading limit for total nitrogen shall become effective with the calendar year beginning on January 1, 2003 unless it is provisionally waived per Special Condition A.(3.), Annual Limits for Total Nitrogen. 6. The quarterly average for total phosphorus shall be the average of composite samples collected weekly during the calendar quarter (January -March, April -June, July -September, October - December). 7. Chronic Toxicity (Ceriodaphnia dubia) P/F at 2.4%: January, April, July, and October [see Special Condition A.(4)]. Toxicity monitoring shall coincide with any metals and cyanide monitoring, if required. 8. The pH shall not be less than 6.0 standard units nor greater than 9.0 standard units and shall be monitored daily at the effluent by grab sample. There shall be no discharge of floating solids or visible foam in other than trace amounts. Kinston Nort.hskle NV\V TP NPDES No. NC0024236 A. (2.) TOTAL NITROGEN MONITORING The Permittee shall calculate the annual mass loading of total nitrogen as the sum of monthly loadings, according to the following equations: (1) Monthly Mass Loading (lb/no) = TN x Q x 8.34 where: TN = the average total nitrogen concentration (mg/L) of the composite samples collected during the month Q = the total wastewater flow discharged during the month (MG/month) 8.34 = conversion factor, from (mg/L x MG) to pounds (2) Annual Mass Loading (lb/yr) = E (Monthly Mass Loadings) for the calendar year The Permittee shall report the total nitrogen concentration for each sample and the monthly mass loading in the appropriate self -monitoring report and the annual mass loading of total nitrogen in the December self -monitoring report for the year. A. (3.) ANNUAL LIMITS FOR TOTAL NITROGEN (a) The Neuse Nutrient Management Strategy rule for point sources (') provides that annual mass limits for total nitrogen shall be included in the permits for all dischargers with permitted flows (as defined in the Strategy) greater than or equal to 0.5 MGD and that those nitrogen limits, including the limits in this permit, shall become effective with the calendar year beginning on January 1, 2003. (b) The Neuse rule also provides that members of a group compliance association shall not be subject to individual annual mass limits for total nitrogen. At the time of permit issuance, the Permittee had expressed interest in joining such an association. Accordingly, (1) the total nitrogen limit in Condition A(1) of this permit is deemed waived provided that the following conditions are met: (i) a formal agreement between the association and Environmental Management Commission, as outlined in 15A NCAC 2B. 0234, is established and is in effect; and (ii) the Permittee is a party to said agreement; and (iii) the association and the Permittee substantially conform with the agreement. (2) So long as the total nitrogen limit in Condition A.(1.) is waived, the group nitrogen allocation established pursuant to the agreement referenced above and any subsequent amendments is hereby incorporated as an enforceable part of this permit. (c) If the Division determines, at any time during the term of this permit, that these conditions are not being met, it shall notify the Permittee in writing of this determination and of its basis. The consequence of such a determination shall be that the Permittee's annual mass limit for total nitrogen and its effective date shall be reinstated immediately. The Division shall accept and consider written responses received from the Permittee and/or the association within thirty (30) days of the original notice before making a final decision and will provide that decision in writing. Kinston Northside WWTP NPDES No. NC0024236 1 A. (3.) ANNUAL LIMITS FOR TOTAL NITROGEN (cont'd.) (d) The Permittee shall notify the Division in writing within five (5) working days if, at any time during the term of this permit, the Permittee elects not to join the association, or if it withdraws or otherwise loses its membership in the association. Notification shall be sent to: NC DENR / Division of Water Quality / NPDES Unit 1617 Mail Service Center Raleigh, NC 27699-1617 Footnote: 0) Neuse River Basin - Nutrient Sensitive Waters Management Strategy: Wastewater Discharge Requirements (15A NCAC• 2B. 0234). A (4). CHRONIC TOXICITY PERMIT LIMIT (QRTRLY) The effluent discharge shall at no time exhibit observable inhibition of reproduction or significant mortality to Ceriodaphnia dubia at an effluent concentration of 2.4%. The permit holder shall perform at a minimum, ouarterlq 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 January, April, July, and October. 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 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 Branch 1621 Mail Service Center Raleigh, North Carolina 27699-1621 Completed Aquatic Toxicity Test Forms shall be filed with the Environmental Sciences Branch 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. Kinston Norihsidc \V\VTP NI'DES No. NC0024236 A (4). CHRONIC TOXICITY PERMIT LIMIT (QRTRLY) (cont'd.) 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 Branch 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. A. (5.) RELOCATION OF DISCHARGE TO THE NEUSE RIVER The City of Kinston shall receive tertiary limits (BOD5 (5& 10 mg/1, summer/winter) NI-13-N (1&2 mg/1, summer/winter) for oxygen consuming waste, as well as more stringent limits on toxicity testing and toxicant parameters, should the facility not relocate the discharge to the Neuse River by expiration of this permit and reissuance of the next permit. The City should pursue relocation of the discharge and upgrade of the treatment facility as specified in the Judicial Order by Consent (JOC). Relocation of the discharge should be planned as one of the first steps in the construction sequence of the upgrade, if feasible. Kinston Northsicle \ \ TP NPDES No. NC:0024236 Wl Isrm NORTH CAROLINA SS LENOIR COUNTY - NORTH CAROLINA LENOIR r PUBLIC NOTICE STATE OF NORTH CAROLINA ENVIRONMENTAL MANAGEMENT COMMISSION/NPOES UNIT 1617 MAIL SERVICE CENTER RALEIGH, NC 27699-1817 NOTIFICATION OF INTENT TO ISSUE A NPDES WASTEWATER PERMIT al the basis of thorough shad review and appscS6on o/ NC Gen- eral Statute 14321, Public law 92• 600 and other lawful standards and rag la1ons, the North Caroli- na Environmental Management Commission proposes to Issue a National Pollutant Discharge Elimi- nation System (NPDES) wastewa- ter discharge permit to the person(s) listed on the attached pages e1ec ive 45 days from the pub*sh date of this notice. Written comments regarding the proposed permit will be as- cepted unt8 30 days akin the pub- lish date of this notice. All corn• roan received prior to that data ere considered in the final determi- nations regarding the proposed permit. The Director of the NC Di- vision of Water Duality may deckle 10 hold a public meeting for the proposed permit should the Divi- sion receive a significant degree of public interest. Copies of the draft porn* and \ other supporting information on file used to determine conditions pres- ent n the draft permit are available The abOV upon request and payment of the ousts of reproduction. Mail con• Z books and flies of ill tmbinn ato atnhaeorCDievsi%fnoroifnfW«antts; Publication. Duality al the above address or call Ms Christie Jackson at (919) , 733.5083, extension 538. Please Include the NPDES permit number (attached) in any communication Inlerested.persons may also visit the Division of Water Quality at 512 North Salisbury Street, Rs- )elgh, N.C, 27604-1148 between the hours of 820 a.m. and 5:00 p.m. ten/of/Iv information on file. ' NPDES Permit Number NC0024236. City of Kinston, Northside Wastewater Treatment Plant, P.O. Bok 339, Kinston, N.C. 28501 has applied ler a permit re. newel fora facility located In Le- noir County discharging treated wastewater into an unnamoditrlbu- lary to the Neuse River In the Nouse River Basin. Currently BOOS, ammonia and dissolved oxygen are water quality limited. This discharge may affect future &locations in this portwn of the re- ceiving stream. _ NPDES Permit Number NC0020541. City of Kinston, Peachtree Wastewater Treatment Plant, P.O. Box. 339, Kinston, N.C. 28501 has applied fora perm* re- newal for a facility located In Le- noir County discharging treated wastewater Into an unnamed Iribu- tary to the Neuse River in the Neuse River 8a51n. Currently 0005. Ammonia and dissolved oxygen are water quality limited. This discharge may effect future allot -aligns in tits portion of the re. solving stream. September 8,2000 (Adv.) AFFIDAVIT OF PUBLICATION �1s� Before the undersigned, a Notary Public of said County and State. duly com- missioned. qualified and uthorizcd by law to administer oaths,/personally appeared�, . /..�,../AL who being first duly sworn, deposes and says: that he (she) is t/ 15seof The Free Press engaged in the publication of a newspaper known as The Free Press published. issued, and entered as second class mail in the City of Kinston in said County and State; that he (she) is authorized to make this affidavit and sworn statement; that the notice of other legal advertisement. a true copy of which is attached hereto, was published in The Free Press on the following dates: AC0 And that the said newspaper in which such notice, paper. document of legal advcrtiscmen(was published was. al the time of each and every such publica- tion, a newspaper meeting all of the requirements and qualifications of Section 1-597 of the Gcncral Statutes of North Carolina and was a qualified newspaper within the ntciIilIi1 xof.Section 1-597 of the General Statutes of North Caro] i:ii. This / `! day of Sworn to and subscrib Reev for nac, this / -64" day of vu faLt-a4--&6°. Notary Public My commission expires: My Commission Expires May 1, 2004 State of North Carolina Department of Environment and Natural Resources Division of Water Quality James B. Hunt, Jr., Governor Bill Holman, Secretary Kerr T Stevens, Director e7A DENR Division of Water Quality NPDES Unit FAX: (919) 733-9919 � ,ZI2ZI�t� FAX TO: Roger Thorpe/ Barry Adams Re.: Kinston Plants FROM: Susan A. Wilson PHONE: 733-5083, ext. 510 1AO. OF PAGES INCLUDING THIS SHEET: 3 Roger/Barry, FAX NUMBER: WaRO Just wanted to pass along some comments from Kinston re. the draft permits (not sure you guys were copied). Could you help me with their comment #1? Not sure I understand what they still want to do. Comment #2 is no big deal and it seems just a comment on the draft letter, not the permit. Comment #3 won't affect the permit - the permit allows them 4.5 MGD (and I thought I was reasonably sure they were under moratorium before, but, whatever - the permit reflects the design flow). Susan A. Wilson. �,}cttil� i2 1t/do a•tql/b1 ):15 141(1141Cd> ? /4-71-5)'' ,n&P7/2* itt4/' 141- gip 56/1/1442.1?e4f- %115Y-4- l- l Vi $ ( .mil C'-�1� �� � r/S ,tsq dr 15 c h * 7-c. /1/F74,1 -A) i ---M77n&v! 7" G!)'11 n / 12Gf qao ee„ 6( /5 c- 4 kv e5 G'vcr��T �D b'C. 4/i41 2rdri/ TTZG( . kj,-; e 149/ ,5 eypt (06 0 1 c M./re t 17-7 1144 4 (1 1,1/va,s1u-- City of Kinston Engineering Department September 29, 2000 P.O. Box 339 Kinston, North Carolina 28502 OCT - 3 2000 - Y?ATER QUALITY SOW.1t;E BRANCH CERTIFIED MAIL RETURN RECEIPT REQUESTED NUMBER: 7099 3400 0012 0008 3725 Dave Goodrich, NPDES Branch Supervisor State Engineering Review Group North Carolina Department of Environment and Natural Resources Division of Water Quality 1617 Mail Service Center Raleigh, North Carolina 27699-1617 RE: Draft NPDES Permits Peachtree Wastewater Treatment Plant NPDES No. 0020541 Northside Wastewater Treatment Plant NPDES No. 0024336 City of Kinston Lenoir County Dear Mr. Goodrich: The City of Kinston is in receipt of the above referenced Draft National Pollutant Discharge Elimination System (NPDES) Permits. We agree with the Permit Conditions as described within the NPDES Permit. However we take issue with two items within your letter dated August 30, 2000 letter concerning these permits. 1. The lagoon at present treats only stormwater. Stormwater enters and discharges. The City no longer uses the lagoon for treatment, and if limitations are being are being placed on the lagoon, then I can assume that the lagoon is permitted. The City has repeatedly tried to make use of the lagoon only to be told that we cannot unless it is permitted. At present and since Hurricane Floyd, the lagoon has been discharging stormwater at a rate of approximately 50 gallons per minute. This fact was reported, and no comment was made. No comment was made at the last inspection of the Peachtree Wastewater Treatment Plant. In the permit application we agreed to monitor any stormwater discharge, but that is not part of the NPDES Permit. The Judicial Order of Consent (JOC) only states in Order 2,1,0) that the lagoon must be decommissioned prior to December 31, 2003, and it will be addressed in the 201 Plan. 2. Both Plants are not under a flow moratorium. The City of Kinston is under a Sewer moratorium defined in Order 6 of the JOC as, "any additional sewer system extensions". In fact Order 6 of the JOC will allow additional flows into (252) 939-3237 - Fax: (252) 939-3279 each plant under certain conditions. 3. The allowable discharge from the Northside Wastewater Treatment Plant was never reduced to 2.25 million gallons per day. According to Order 2,C,(ii) of the JOC, the Intermediate Plan of Action which was submitted on November 24, 1998, was to address this issue, and it did in Section III. Therefore allowable flow from the Northside Wastewater Treatment Plant was never reduced to 2.25 million gallons per day. This matter was also discussed with Roger Thorpe and Jim Mulligan in a meeting held in the Spring of 2000. The City therefore maintains that the permitted flow from the plant be 4.50 million gallons per day as shown on the permit conditions, and not 2.25 million gallons per day as the letter stated. We trust that you agree with each of the changes proposed above, and we trust that you will issue another letter to clarify these items. The City will continue to operate both wastewater treatment plants to comply with the conditions as outlined in the draft permits, and not according to your letter dated August 30, 2000. We would like to thank you for your review of this response to the Draft NPDES Permits for the City of Kinston. If additional information or action is required, please contact John Jarrell or Scott Stevens at (252) 939-3237. Sincerely, n A. ar ssistant Cit I, II Engineer cc: Mr. Ronald Wicker, Kinston Director of Public Utilities Mr. Vernon Rochelle, Kinston City Attorney Mr. Scott Stevens, Kinston City Engineer Mr. Chuck Cauley, Kinston Wastewater Treatment Plant Superintendent Mr. Henry McLean, City of Kinston (252) 939-3237 - Fax: (252) 939-3279 DENR/DWQ FACT SHEET FOR NPDES PERMIT DEVELOPMENT NPDES No. NC0024236, Kinston Northside WWTP Facility Information Applicant/Facility Name: City of Kinston/ Kinston Northside WWTP Applicant Address: P.O. Box 339, Kinston, NC 28501 Facility Address: North Jackson Drive Permitted Flow 4.5 MGD Type of Waste: - < 10% ind., - 90% Dom. (after 2 MGD SIU flow is dropped) Facility/Permit Status: Renewal County: Lenoir Miscellaneous Receiving Stream: Neuse River (actually "UT" to Neuse) Regional Office: WaRO Stream Classification: C NSW SI: 27-(26) Quad F28SE Kinston 303(d) Listed?: NO TMDL Permit Writer: S. Wilson Subbasin: 030405 Date: April 26, 2000 Drainage Area (mi2): 2552 "" Summer 7Q10 (cfs) 283 Winter 7Q10 (cfs): 292 Average Flow (cfs): 1514 —/� IWC (%): 2.4 Primary SIC Code: 4952 SUMMARY The City of Kinston has had well documented problems concerning residuals disposal and IR issues. Both the Kinston Peachtree and Northside Plants are under a Judicial Order by Consent (JOC) with specific intermediate and final compliance dates and stipulated penalties for not meeting those dates. The Kinston Northside plant is under a flow cap of 2.25 MGD (due to one aeration basin being down. An 8 inch line was connected between Northside and Peachtree to divert flows and/or residuals between plants, etc. This discharge is actually to a point (likely in a flood plain of the Neuse) prior to the Neuse proper. Because Kinston likely plans to shut down Peachtree and expand the Northside plant, DWQ will require a direct pipe to the Neuse at that time. Renewed permit will continue at the existing discharge point. * Addendum to Fact Sheet: Site visit 7/18/00 confirmed that this discharge enters into an unnamed tributary to the Neuse River [the tributary is subject to inflow from other sources besides the contribution from the WWTP). Kinston must eliminate the discharge into this tributary by expiration of the proposed permit and reissuance of the next permit. Long range plans for the Northside plant indicate that the effluent will be piped directly to the Neuse River. TOXICITY TESTING: Current Requirement:Chronic P/F @ 2.4% (also recommended with renewal) The City has reported toxicity "passes" since as early as 1996. COMPLIANCE SUMMARY: BASED ON THE PREVIOUS 2 YEARS Both Kinston plants have had severe compliants problems (esp. with flow and solids) which prompted the Division to recommend issuance of a JOC. [Per WaRO, JOC dates have been met]. Kinston Northside NPDES Renewal Page 1 Oct. 1999 - TSS = 37 mg/1 (limit = 30 mg/1 monthly avg.); Mar. 1998 - TSS = 34 mg/1; Feb. 1998 - TSS = 38 mg/1. (Kinston - Northside appears to be compliant with other limits, per computer retrieval) INSTREAM MONITORING: Kinston is part of the Lower Neuse Basin Association (LNBA) and is not required to perform the instream monitoring required in this permit. PROPOSED CHANGES: Kinston proposes to become a member of the Neuse nutrient compliance group. If Kinston joins the compliance association, the annual load limit for total nitrogen will not have to be met. The total phosphorus limit of 2 mg/1 was instituted in the previous permit. Cadmium and mercury limits have been eliminated from the permit due to lack of reasonable potential to exceed the water quality standard. Copper and zinc monitoring have been included in the permit due to the presence in long term monitoring data and it's exceedance of the 1/2 Final acute value. Kinston Northside has lost its major industry during this latest permit cycle (- 2 MGD permitted ind. flow). This will likely reduce average monthly flows significantly and allow some flow from the Peachtree plant to be diverted. PROPOSED SCHEDULE FOR PERMIT ISSUANCE: Draft Permit to Public Notice: May 17, 2000 (est.) Permit Scheduled to Issue: July 1, 2000 (est.) STATE CONTACT: If you have any questions on any of the above information or on the attached permit, please contact Susan Wilson at (919) 733-5038 ext. 510. REGIONAL OFFICE COMMENT: QQ, I 't il. h4G 1 Pe'L fPFICAtitL 5/5/00 ( vie Ti-l" i-1 ViSc ti;5, re. 'V& 73tsu-1 /24 o .,A` " u.T " .r-IGA/ w&J'r 6/3 £ T V1ScT 16 Pe'RGin 2-ee-. f}DDeN 7c.t,v To F'Ac.r` lF1SITE NAME: DATE: Kinston Northside NPDES Renewal Page CHRONOLOGY 4/26/00 1990, December - Authorization to Construct permit (CG&Ls) issued for chemical phosphorus removal, anaerobic sludge digestion, dechlorination. 1994, April - previous permit issued. Included a requirement for an EAA to meet limits of 5/2 (due by 1997). Due to the severe compliance concerns at the Kinston plants, the City has been forced to address treatment plant improvements via the JOC. 1995, October - Authorization to Construct permit (CG&Ls) issued for mechanical screening and grit removal. 1998, August - Kinston submitted permit renewal. JOC was issued August 18. 1999, June - NPDES Unit issued ATC for physical modifications at both plants (aerators, mixers, etc.) to assist operations. 1999, July - Kinston requests speculative limits for 201 Facility Plan (to receive CG&L funding) 1999, August - Kinston consultants narrow request for speculative limits using possible flow scenarios (subject to change). Alternatives: a) continue discharge at Peachtree and Northside, b) eliminate Peachtree & continue Northside (if reuse) appx. 12 or 15 MGD. If continue both - 5 MGD Peachtree & 6 MGD Northside. 1999, September - DWQ gave speculative limits to Kinston - 5/1 (BOD/NH3-N), TP = 1, mass TN annual limit. 2000, January - Project 11.5 - 12 MGD for combined flows from both plants (possibly use Peachtree for equalization only, then divert all flow to Northside). 2000, February - Kinston's consultants submitted letter expressing concern about meeting a concentration based limit of 3.5 mg/1 TN; DG clarified and stated annual load limit would be required. 1998, June through 2000, March - DWQ has to revise nitrogen allocation, submit TMDL for EPA approval, and revise Neuse rules. In February 2000, EPA approved NCDWQs TMDL and the EMC approved revised temporary Neuse rules. 2000, July 18 - NPDES staff went on site visit to both Kinston plants to look at effluent conveyances. In actuality, neither effluent conveyance qualified as an "effluent channel" by current definition. However, since both plants are under a JOC and the 201 plan intends to phase out the Peachtree plant and transfer flow to the Northside plant, this permit will reflect a compliance schedule until expiration. Kinston Northside NPDES Renewal Page Date: c/3 Time: TELEPHONE RECORD Project: /-i r.19-re, ski 1I 2 f FT . Tor-7- 0 Return Mr./ Mrs. Po S 7 aRP� ❑ CaII to Address t,, I Call from W iA-ac) Telephone: Representing: FAX: Subject: NOTES/ SUMMARY R.T. Leer Votc- AkPri 1, I2- AZ: (c . N 5To1S FAT S,-irr$ ..L I(A17 eAgP<L) ' l) ) DG •DAr�s f44\f -4-1 Mei- 2) F0 i ►i ?Li ,' r 5 f) - (- I.IIJDG(z- Mo -kTs f2.. i Q u4l 3) ol)-,Ai c 1464 oon) PT iPerC.1.4- - E (-714kt TI.I£j W Air6-> k 5VO ouXrALL r (2J� IdcL.1,1:2p; a /nihc<<Je" c4400AJ i in) b SC.IZ oN - . flu.i 5A76 f,-/ry Nu s� ?�(7..a24.-1 c L-c 6 71E, - spl,ep 0,7- ( '`"`,`�. &A PL4t [1Lt9.701- 46-9 i"oPX oP) 1nIDsc r T4 ( W1 w Jeib- PLotJ $ To t ban( S( DE - c(�v5&• 4cµ•T(L�Ci 4r�D e-XPMb iP ( 2 9 172,6 (1) � 't' I,L, "'N I Ile DI RGG-r PI PI N.)c l b N S e TAB . (-e' 6 ri 4 0/ 1*cl 12 1, +i NEEDED FOLLOW-UP ACTION(S) 1. - 1.42(c,i- Lilo Par fri SPPc *L BY WHOM/WHEN .1. 2. Cv ^-I c (o N -11(4) “,3 P2o? 1Z.- 2. 3. (L.056 ©UT- 3. 4. 4. 5. 5. cc: Signed Facility Name = NPDES # = Ow (MGD) = 7Q 10s (cfs)= !WC (%) = Kinston - Northside NC0024236 4.5 283.1 2.40 FINAL RESULTS Cadmium Max. Pred Cw Allowable Cw 2.08 83.2 72. FA4 = 15&oN-I2) 140 ( �T Parameter = Standard = Cadmium 2 pg/I n BDL=1/2DL Actual Data 1 0.50 <1 2 0.50 <1 3 0.50 <1 4 0.50 <1 5 0.50 <1 6 0.50 <1 Mult Factor = 7 0.50 <1 Max. Value 8 0.50 <1 Max. Pred Cw 9 0.50 <1 Allowable Cw 10 0.50 <1 11 0.50 <1 12 0.50 <1 13 0.50 <1 14 0.50 <1 15 0.50 <1 16 0.50 <1 17 0.50 <1 18 0.50 <1 19 0.50 <1 20 0.50 <1 21 0.50 <1 22 0.50 <1 23 0.50 <1 24 0.50 <1 25 0.50 <1 26 0.50 <1 27 0.50 <1 28 0.50 <1 29 0.50 <1 30 0.50 <1 31 0.50 <1 32 0.50 <1 33 0.50 <1 34 0.50 <1 35 0.50 <1 36 0.50 -<1 37 0.50 <1 38 0.50 <1 39 0.50 <1 40 0.50 <1 41 0.50 <1 42 0.50 <1 43 0.50 <1 44 0.50 <1 45 0.50 <1 46 0.50 <1 47 0.50 <1 48 0.50 <1 RESULTS Std Dev. 0.2231595 Mean 0.4287037 C.V. 0.5205449 1.3 1.6 ug/l 2.08 pg/I 83.2 'IV t r 49 0.50 <1 50 0.50 <1 51 0.50 <1 52 0.50 <1 53 0.50 <1 54 0.50 <1 55 0.50 <1 56 0.50 <1 57 0.50 <1 58 0.50 <1 59 0.50 <1 60 0.50 <1 61 0.50 <1 62 0.50 <1 63 0.50 <1 64 0.50 <1 65 0.50 <1 66 0.50 <1 67 0.50 <1 68 0.50 <1 69 0.50 <1 70 0.50 <1 71 0.50 <1 72 0.50 <1 73 0.50 <1 74 0.50 <1 75 0.65 0.65 76 1.6 1.6 77 0.37 0.37 78 0.27 0.27 79 0.95 0.95 80 0.93 0.93 81 0.12 0.12 82 0.31 0.31 83 0.27 0.27 84 0.42 0.42 85 0.5 0.5 86 0.39 0.39 87 0.65 0.65 88 0.27 0.27 89 0.05 0.05 90 0.44 0.44 91 0.3 0.3 92 0.02 <.04 93 0.02 <.04 94 0.4 0.4 95 0.08 0.08 96 0.05 0.05 97 0.02 <.04 98 0.02 <.04 99 0.02 <.04 100 0.02 <.04 c 101 0.02 <.04 102 0.02 <.04 103 0.02 <.04 104 0.02 <.04 105 0.02 <.04 106 0.02 <.04 107 0.02 <.04 108 0.02 <.04 109 110 LONG TERM MONITORING PLAN REQUEST FORM (A • rNd • J C� i 3 o — < c ,� hN 0 FACILITY: i-� (In. 5 D►\ f, O r S t O.e NPDESNO.: riGaa EXPIRATION DATE: REGION:() P&E REQUESTOR: PRETREATMENT CONTACT: --I-e.wk_ pD v`Gt rc DATE OF REQUEST: 3) / 10 INDICATE THE STATUS OF PRETREATMENT PROGRAM: 1) THE FACILITY HAS NO SIU'S AND SHOULD NOT HAVE PRETREATMENT LANGUAGE (2) THE FACILITY HAS A PREATREATMENT PROGRAM. PERMITTED FLOW: INDUSTRIAL % DOMESTIC 3) ADDITIONAL CONDITIONS REGARDING THE PRETREATMENT PROGRAM ATTACHED. c,k,rrevv+ S j l (A- P Now c s - . 3S m 60) cu-L.QQ Pretreatment Unit Staff (Region) 2,00 skta- 41,41:4- S(C pots butt se ri- 'r7'Y u PnG(5 s, rxrP-f\rrj`o VI) ofit` Vo''.g)00 -7Da.v,� �-�cd,a,c.., ph, cca,cio, d-r8ipuiat 6 a-D , 7-ss n 1-4 7 1 " Tc+a 1 P . 3 D f o �!' Q 'LAC [ S ' J i G A- I l (�Cr-- rT J` l ✓C)e (C `��r J � fi �11 he �o,•,•�l� �� a.(! a-t' ? ovv kite_ --� $� cG.G�� � s j h (IOW ip a p�-G.�� 01;,` I vtGe cJ h C'� k n • 06±4\ ctj,x4pij:.---- Gan a fi �-s 1 l.glciS) a�not g-) Ba ssz:ti w 0.1 1k4,- SAA at-v-ur'1 0Y) e k:c��u►� a 5 a- - 9 3 9- 3 306 64.n. b MAR- 7-00 TUE SAMPLE LOCATION t. Mani& 8ffl l DATA SOURCE " Icor R,00rds lc( 1 COY OF 101413110e1 LONG VERMMONIIMING DATA SSIM1g, D� flour (1) ( ) pg M' BOO � INS \� MIN � Temp. 0 P (10110 l �1s r (' .'i! Ord '.•1) Cu Cr '.A! .) P b (1?.D 1& 111 Se ( ) Al 2 I OW* l� M `� TEN f (WM Talot Nitrogen "VP ttbueved t mago ' / owlty /� ��/� ' ) (Rt$/ ( _ Iut 97 1J0 71 12 <3 23. , ' <5 <3 <10i <10r _ 21.0 13 012 Aps-97 308' 7.40 10.0 2001 <li 19 1.10 CS.O <1 25.1 <1.0 <5 <2 10.0 <10 <5.0- SSA <10 3.08, 7.2 0. 0.007 111-97 1 154 7.40 3.9 6.0 <1 25 /2.4 <5..0_ "<1! 13.1 <1.0 • 5 "<.2 <10 <101 <s.0 260 <10 "4.4 "14.73` 7, 0.48 0.011 0e119'i 1.49 1.00 4.9\ 39.0 0.5O. 21 2.40 <3 03 231 5.0 1.0 _ <2 40 7.9 .53 , 30.0 3.4 43 769 7.6 0. F6 -91 3.2i 7.30 41 380 2.714 13 1.10 <5 <04 20. t - <7 1.8 <2 4.a ati 31.0 42. 5. 8 4 1 1.91 COOS May94 1.18 7.30. SD 160 <5 23 2.91 <3 .51 Li 4.4 0.8, <2 10.0 .23 32.0 18 u 62623 7.2_ 1.44 <005 , 237, ?.S 3.0 1?0 U 26 0.7>1 <5 _ d7 90 15 b 3.2 <.2 11.0 32 213.0 47 1.6 - 1132 6.49 1.6 0.006 IAng9i 98 2.711 7.5 7.6 4.2 0.25 20 0q <5.0 <1.0 4.0 < .0 <5.0 <.2 17.0 <10 <S_' 10.0 15 ^""27.12 "^"21.16 :i 26 0.006 .Nov i<7cb'99 233 6. 3.0, _ 2S.D 0.54 17� •.43 <SI wecl 26. <S.0 <i "<.2 <10 <l0! <5 0 31.0 [1 *1.83 '11.611 1 2.42 20061 'Ap.99 2.66 T <2.0 12.0 0.75 18.A "*.3S <3.0!'R••<1 11., <5.0- <50 """'<.2 42.0i <11k <5.0 33.0 15 "13.1 "115.5 8 2.1 <.005 ' Ang-99 1.6375 6: 22 1 <.01 26.5 p•31 <5.0 "<1 <1 ' <5. <5.0 1.<. <10 <10 1.0 "'1.19 "'4 9 4 6.4 LTA <005 Oct-09 _ 10012 6.70 6.0 37. 0.13 17 "1'1".83 <S 0 '""<1 20. + <5.0k <5.0 ^ '<2 <10 <10 4. ' i 0 31 i 8.2 1.41 COOS Norw99 1.9142 611 22 28. 16.M»me <5.0 "*s**<l 16 ' <10 <10 ^..++rs <l4 <101 <3, 53.0 12 ''"°"444 Aj4.i'6.66 8.4, 1.67 <005 Deo-99 1.774 6.85 <2 27. 0.19 14 041i 67 <5.0 9P<S, 170' 4A\ <10 fi'<.2 <10 <IO <5. Ir,'IA) L2 rl.33 So10.91 1114 3.73 <905] lan-00 L5141 7.18 <2.0 21<.04 122 0.39 <5.0 <1.0 <10 <5.0 <3.0 <.2 <10 <14 <5.0 50.0 1 0.9 6.75 8 0.SLT O. 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V kl.0 ES 5 rnlce 1/97 No Re-qmr) 3/71130 Re: kinston northside Subject: Re: kinston northside Date: Mon, 24 Apr 2000 09:15:33 -0400 From: Dana Folley <Dana.Folley@ncmail.net> To: Susan Wilson <susan.a.wilson@ncmail.net> sounds good to me. -Dana Susan Wilson wrote: > hey, looks like for this one from what you gave them i'll end up > dropping Cd, Hg then adding Cu and Zn monitoring due to action level > concerns. 1 of 1 4/24/00 10:52 AM Memorandum To: Susan Wilson From: Christie Jackson Date: 03/24/00 Re: Kinston - Northside (NC0024236) I did not enter RPA Data for Mercury as the DMR's reported only < values. The self -monitoring summary report indicated that this facility has passed all toxicity test since 1996. 1 P.O. Box 33396 Raleigh, North Carolina 27636 USA Tel: (919) 462-7501 Fax: (919) 462-8356 C((a ulP-e,Poyvi, HBO �' � r BLACK Illy& VEATCHvi:/��, � fig/ , &7/a41;11.* Veatch International Company dj )4P 15 _ F E B 1 1 2000 DENR - WATER QUALITY POINT SOURCE BRANCH Mr. David A. Goodrich Supervisor, NPDES Unit Division of Water Quality North Carolina Department of Environment & Natural Resources 1617 Mail Service Center Raleigh, North Carolina 27699-1617 Re: City of Kinston Total Nitrogen Limits 201 Facilities Planning Update Dear Mr. Goodrich: February 8, 2000 On February 2, 2000 representatives of the City of Kinston and Black & Veatch met with representatives of Construction Grants and Loans of the Division of Water Quality to discuss issues and progress on the preparation of the 201 Facilities Plan Update. One of the issues discussed was the planning limits for total nitrogen. Representatives of Construction Grants and Loans expressed concern that the total nitrogen limit may not be finalized as a yearly mass loading. Opinions were expressed by DENR personnel that the total nitrogen limit could be finalized in the permit as a daily limit of 3.5 mg/1 based on a monthly average. These comments were especially of concern to us and the City of Kinston because of some recent analysis and additional sampling that was performed to assist in modeling and developing design parameters for proposed facilities. There was some indication from sporadic sampling performed by the City on influent concentrations in previous years that high levels of refractory organic TKN were present in the influent. If this condition existed, it would make it difficult for Kinston to comply with the proposed limits as no technology currently exists to treat wastewater with high concentrations of refractory organic TKN down to the limits proposed. Therefore, additional sampling was conducted on the influent and the effluent of both the Peachtree and the Northside plants for both nitrogen and phosphorus. Samples were taken the week of December 13, 1999, and a summary of the analysis of these samples is attached to this correspondence for your information. the imagine . build companyTM Page 2 Mr. David A Goodrich February 8, 2000 One of the conclusions from this additional sampling is that the refractory organic TKN is low enough that the annual mass loading limit for total nitrogen is achievable with current technology; however, to meet 3.5 mg/1 consistently on a daily basis may not be possible. On behalf of the City of Kinston, we are requesting you to reconfirm that the total nitrogen limit will be an annual mass loading. The parameters of the proposed facility will be designed on meeting a 3.5 mg/1 on a daily basis, but the current available technology will not allow us to guarantee that said concentration can be consistently achieved on a daily basis using the data from the attached summary. Thank you for your assistance. Should you have any questions, please do not hesitate to call me at 462-7509, or our process engineer for this project, Chris deBarbadillo, at 704- 548-8461. Very truly yours, BLACK & VEATCH International Company Randall L. Foulke, PE, DEE Project Manager enclosure c: Mr. Scott Stevens, City of Kinston Engineering Mr. John Jarrell, City of Kinston Engineering Mr. Harold Herring, City of Kinston Utilities Mr. Vernon Rochelle, the City of Kinston Mr. Henry McLean, City of Kinston Utilities Mr. Jim Mulligan, NCDENR Mr. John Blowe, NCDENR = less that detection limit Peachtree Collected specifically for this project Date Collected 12/13/99 12/14/99 12/15/99 12/16/99 12/17/99 Influent Mixed Liquor RAS Effluent Influent Effluent Influent Effluent Influent Effluent Influent COD, mg/I 273 20 503 21 594 20 567 20 Filtered COD, mg/I 130 15 175 16 168 15 198 16 BOD, mg/I 140 23 160 11 170 24 200 24 Filtered BOD, mg/I 92 16 160 2.1 110 7.2 130 11 TSS, mg/I 74 5800 9250 2.8 115 3 92 2.8 141 2.5 VSS, mg 66 3800 3850 Cancelled 104 88 134 NH3-N, mg/I 10.32 0.05 2.9 0.13 12.6 0.09 11.04 0.08 TKN, mg/I 35.3 5.99 22.74 0.69 21.66 0.76 19.3 2.67 Filtered TKN, mg/I 1.16 0.82 16 0.7 14.8 0.78 15.6 1.01 NO3-N04, mg/I 0.54 0.1 0.1 0.84 TP, mg/I 0.2 0.19 5.04 0.21 4.4 0.26 4.1 0.2 Ortho-P, mg/I 1 0.04 1.59 0.05 1.49 0.16 1.51 0.05 Alkalinity, mg/I 127 105 124 109 127 121 184 126 Northside Date Collected 12/13/99 12/14/99 12/15/99 12/16/99 12/17/99 Influent Mixed Liquor RAS Effluent Influent Effluent Influent Effluent Influent Effluent Influent COD, mg/I 114 32 350 28 98 31 578 29 Filtered COD, mg/I 38 17 47 17 45 18 62 16 BOD, mg/I 13 4.7 40 3 40 24 62 20 Filtered BOD, mg/I 13 4.3 13 2.6 13 7.7 19 23 TSS, mg/I 49 22 86 17 18 20 82 23 VSS, mg 38 3900 5455 36 45 340 NH3-N, mg/I 7.6 2350 2819 0.16 7.32 0.19 7.88 0.24 7.32 0.012 TKN, mg/I 29.6 8.13 12.4 1.4 8.42 1.3 14.2 3.09 Filtered TKN, mg/I 7.6 1.26 3.95 0.65 5.54 0.66 5.69 0.69 NO3-N04, mg/I 5.1 5.33 5.99 5.5 TP, mg/I 2.14 0.96 5.28 0.8 2.1 0.89 6.92 0.92 Ortho-P, mg/I 0.89 0.14 1.59 0.53 0.61 0.23 2.04 0.43 Alkalinity, mg/I 89 29 101 29 98 47 108 67 To: Permits and Engineering Unit Water Quality Section SOC Priority Project: Yes No X If "Yes", SOC No. Attn: Steve Pellei Date: August 31, 1998 NPDES STAFF REPORT AND RECOMMENDATION Permit No. NC0024236 PART I - GENERAL INFORMATION 1. Facility and Address: City of Kinston, Northside WWTP P.O. Box 339 Kinston, NC 28501 2. Date of Investigation: August 24, 1998 3. Report Prepared by: Brad Shaver RECCjV WATER QUALITY SECTION TON SPP '2 1998 Non -Discharge Permitting 4. Person(s) Contacted and Telephone Number(s): Mr. Chuck Cauley, ORC 939-3375 2Sz 5. Directions to Site: Take hwy 11 south out of Ryden. Take a left onto Hwy.55 traveling east. Travel approximately 3/4 of a mile and take a right turn onto Tower Hill Road. Travel another 1/2 mile on Tower Hill Road and take a left onto Becton Farm Road, the Treatment Plant is at the terminus of this road. 6. Discharge Point(s); List for all discharge points: Latitude:35°17"15' Longitude:77°30"41' Attach USGS map extract and indicate treatment facility site and discharge point on map. USGS Quad No. USGS Quad Name: Kinston 7. Site size and expansion area consistent with application? Yes _X_ No If "No", explain: 8. Topography (relationship to flood plain included): The treatment plant sits approximately 10 feet above mean sea level. 9. Location of nearest dwelling: The nearest dwelling is 1/4 mile down Becton Farm Road toward Tower Hill Road. 10. Receiving streams or affected surface waters: Neuse River a. Classification: C-NSW i b. River Basin and Sub -basin No. Neuse River Basin c. Describe receiving stream features and pertinent downstream uses: Fish Propagation, fishing, boating PART II - DESCRIPTION OF DISCHARGE AND TREATMENT WORKS 1. a. Volume of Wastewater to be Permitted: 4.5 MGD b. Current Permitted Capacity: 4.5 MGD c. Actual Treatment Capacity: 4.5 MGD d. Date(s) and construction allowed by Authorizations to Construct issued past two years: N/A e. Description of existing or substantially constructed wastewater treatment facilities: 4.5 MGD activated sludge wastewater treatment facility consisting of fine filter screen and grit removal, 8 inch line to transfer sludge and/or wastewater from Peachtree to Northside, dual aeration basins, dual secondary clarifiers, chlorine contact basins, aerobic sludge digesters, sludge drying beds, cascade type post aeration, one 13,150 gallon caustic storage tank, one 13,150 gallon alum storage tank for chemical phosphorous removal facility and sulfur dioxide dechlorination facility. f. Description of proposed wastewater treatment facilities: No construction proposed. g Possible toxic impacts to surface waters: Northside's flow is 90% industrial from its on-line users. There may be possible toxic impacts from these users. h. Pretreatment Program (POTWs only): In development Approved X Should be required Not needed 2. Residuals Handling and Utilization Disposal Scheme a. If residuals are being land applied, specify DEM permit number: Residuals Contractor: Advanced Waste Management Services, Inc. Telephone Number: b. Residuals Stabilization: PSRP PFRP Other c. Landfill: d. Other disposal/utilization scheme (specify): 3. Treatment Plant Classification (attach completed rating sheet): IV 4. SIC Code(s): 4952 Wastewater Code(s): 01 & 02 Main Treatment Unit Code: 054 3 PART III - OTHER PERTINENT INFORMATION 1. Is this facility being constructed with Construction Grant Funds or are any public monies involved (municipals only)? Yes. 2. Special monitoring or limitations (including toxicity) requests: Chronic Acute Toxicity Testing Quarterly. 3. Important SOC, JOC, or Compliance Schedule dates (indicate): A JOC is being arranged at present. Activity Date Submission of Plans and Specifications Begin Construction Complete Construction 4. Alternatives Analysis Evaluation: Has the facility evaluated all of the non -discharge options available? Provide Regional perspective for each option evaluated. N/A Spray Irrigation: Connection to Regional Sewer System: Subsurface Disposal: Other Disposal Options: 5. Other Special Items: PART IV - EVALUATION AND RECOMMENDATIONS Presently aeration basin #1 is out of service and is full of treated sludge which is ready to be removed from site. The new grit removal system is used sparingly as to not lose treatment before the wastewater enters the plant aeration basins. During the site visit the #5 aerator associated with the #2 aeration basin was out of service and was altering their treatment capability to remove nitrogen and phosphorous. The site has the dechlorination system in place but is not using because the active permit does not specify a total residual chlorine limit. The City has decided to use residual haulers to manage the sludge disposal as opposed to the drying beds. The beds remain in place but have been grown over with weeds and other volunteer vegetation. The bold highlighted components in the description of the existing wastewater treatment facility need to be added to the permit language. Kinston recently has entered into a JOC, which limits their flow at Northside to half capacity as long as only half the aeration basins are working. This office recommends renewal of this permit for 4.5 MGD given that the treatment plant will be operated at full capacity. Signature of report preparer .4,,Wa er Q Quality egional Supervisor Date NPDES Permit Staff Report Version 10/92 City .af Iftineten Pjrartmextt of public i tilities Post Office Box 339 2517 Richlands Road Kinston, North Carolina 28502 Administration Operations (919) 559-4253 (919) 559-4252 Fax: (919) 559-4271 July 30, 1998 Charles H. Weaver, Jr. NPDES Unit P.O. Box 29535 Raleigh, NC 27626-0535 Dear Mr. Weaver, �oz7l‘a �50. OD le% VD, eio) faz-ct Subject: Renewal of NPDES Permit No. NC0024236 Northside WWTP Lenoir County This is the letter requesting renewal of the NPDES permit for the Northside WWTP (NC0024236). Since the last permit was issued, the City of Kinston has had the following changes: 1. A 8 inch line was added to transfer sludge and/or raw wastewater from the Peachtree WWTP to the Northside WWTP. 2. A U.S. Filter FILTER SCREEN Unit was added to screen material larger than 0.25 in diameter from the influent waste stream. 3. A Walker ROLLING GRIT UNIT WITH GW200 GRITWASHER was added to remove grit and other inorganics from the influent waste stream. This packet contains the original and two copies of the cover letter, completed application form, $300 renewal fee and a description of the sludge management plan. If you have any questions or comments, please contact me at (252) 939-3307 or Fax (252) 939-3741. Sincerely, ELECTRIC, WATER, AND WASTEWATER SERVICES FOR THE BENEFIT AND PROSPERITY OF OUR COMMUNITY Henry evon McLean Assistant Utilities Director/WWT cc. David Walker -City Manager Ron Wicker -Utilities Director Subject: Outline For Sludge Management Program Here is the outline for the sludge management program that will be followed at both the Northside and Peachtree plants. This program was developed based on the Agreement for Biosolids Management Treatment & Disposal Services between the City of Kinston and Advanced Waste Management Services, Inc. Aerobic Sludge Digestion/Storage Facilities At Northside There are 2 above ground circular digestors that hold 737,200 gallons each. There is 1 in ground rectangular digestor that holds 1,496,000 gallons. TOTAL NORTHSIDE SLUDGE STORAGE CAPACITY IS 2,970,400 GALLONS Aerobic Sludge Digestion/Storage Facilities At Peachtree There are 2 above ground circular digestors that hold 888,000 gallons each. TOTAL PEACHTREE SLUDGE STORAGE CAPACITY IS 1,776,000 GALLONS A MINIMUM OF 1,000,000 GALLONS OF SLUDGE MUST BE HAULED BY SLUDGE HAULER FOR EACH LAND APPLICATION EVENT. Sludge Management At Peachtree At the Peachtree WWTP there are 2 above ground digestors that hold 888,000 gallons each. Digestor A will be used for aeration and mixing. It will be considered the primary digestor. No waste sludge will be sent to Digestor B until Digestor A is full. Once Digestor A has been stabilized and decanted as much as possible to meet 503 regulations, the majority of it will be sent to Digestor D at Northside by forcemain for storage and removal to land apply. Once the sludge haulers have enough space in Digestor D the additional amount of sludge shall be sent from Digestor A at Peachtree. Once Digestor A is full, it will be taken off line and Digestor B will be used to stabilize sludge. We will alternate between using Digestor A and Digestor B, with one of the digestor possibly always staying empty. Sludge Management At Northside Digestor A will be the primary digestor for aeration and mixing, with Digestor B being used for some mixing and gravity thickening. The majority of the stabilized sludge will then be sent to Digestor C for ultimate sludge disposal by land applying. Once the sludge haulers have remove enough sludge form Digestor C, the remain sludge in Digestor B will be sent to Digestor C to dispose. Scheduling Of Sludge Hauling Witit Contractor Because the stablized sludge from Peachtree is sent to Digestor D at Northside, Once Digestors C and D at Northside are as full, stablized and dewatered as possible, it is time to make sure all pre -land application testing gets done and a call is made to the sludge hauler to land apply. An initial call should be made to the sludge hauler three weeks before you are ready for them to haul to make sure all scheduling is right. After that call is made all pre -land application test should be done immediately. Keep in touch with the sludge hauler to ensure him your sludge meets 503 regulations and that he gives you a date of arrive. The total volume of Digestor C and D is 1,474,400 gallons which is over the minimum 1,000,000 gallons required per sludge event. For both the Peachtree and Northside WWTPs sludge more than likely will be hauled every 30-45 days. This will call for 8-12 land application events per year. FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2 Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b 404a 404b 405 Farval Lubrication Systems P003 Pipe #1 • -. 2501 Airport Road Kinston Lenoir North Carolina 28501 3569 Lubrication Sy& ms 251 J Intermittent(int) ® Yes 403d Quantity thousand gallons per day ® Continuous (con) No 403e 403f Units(See Table Illl Parameter Name Flow BOD TSS pH Cd Cr Cu Parameter Number 50050 00310 00530 00040 01027 .05 '• 01034 1.32 01049 1.62 Value . 025MGD 025 MG/1 300 mel 6-9 Parameter Ca Pb Ni Ag Zn P TTO Parameter Number 00720 01051 01067 01077 01092 00665 - Value 0.51mg/10.33mg/11.91 mgLi 0.20 mgll 1.25mg/1 - 1.02 FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the Industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2 Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b o" 404a 404b 405 West Company N002 Pipe #1 3910 Rouse Road Kinston Lenoir North Carolina 28503 3069 Molded Rubbe 403c Rubber I4O3d Quantity 120) thousand gallons per day Intermittent(int) Eg Continuous (con) [l Yes Ei No 403e 403f Units(See Table III) Parameter Flow BOD TSS pH Cu Zn 0&G Parameter Number 50050 00310 00530 00040 01042 01092 0055h Value .120 700mg/1 200mg/1 6-9 0.07mg/'1 0.70mg/L 95mg/1 Parameter Name Cl P Parameter Number 50060 00665 Value 0.5mg/1 FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facilityinto the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2 Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b 404a 404b 405 Cedar Fresh N003 Pipe#1 2400 Airport Road Kinston Lenoir North Carolina 2499 Wood Product 403c Wood Cedar 40Qd Intermittent(int) ® Yes Quantity thousand gallons per day r2 Continuous (con) E No 403e 403f Units(See Table III) Parameter Name Flow BOD TSS pH Parameter Number 50050 00310 00530 00040 Value 0.025M 3 104mg/I 834mg/L 6-9 Parameter Name Parameter Number Value FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2. Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b Kinston Neuse CorpnrM-inn N004 Pipe 1 2000 Dobbs Farm Road Kinston Lenoir North Carolina 28501 3537 Fork Lifts 403c 403d Quantity 404a ✓ thousand gallons per day 404b Interm✓✓✓rmittent(int) ja Continuous (con) 405 Yes [] No 403e 4031 Units(See Table 1111 Parameter Name Flow BOD TSS pH Cd Cr Cu Parameter Number 50050 00310 00530 00040 01027 01034 01042 Value 0.008mgd200mg/1 200 mg/1 6 - 9 0.11mgt12.77mg/11.50mg/1 Parameter Name Cn Pb Ni Ag Zn TTO P Parameter Number 00720 01051 01067 01077 01092 - 00665 - Value 1. 20mg/10.15mg/1). 60mg/1 0. 43mg/11. 50mg71,2.13mg/1_ FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2. Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 4011 402 403a 403b 404a 404b 405 Kinston Neuse Corporation N004 Pipe 2 2000 Dobbs Farm Road Kinston Lenoir North Carolina 28501 3537 Fork lifts 403c 403d Quantity '0. 50) thousand gallons per day Intermittent(int) Continuous (con) a Yes El No 403e 403f Units(See Table III) Parameter Name Flow BOD TSS pH Cd Cr Cu Parameter Number 50050 00310 00530 00040 01027 01034 01042 value ).0005mgd200mg/1 200mg/1 6 - 10 0.11mg/'12.77mg/1 1.5mg/1 Parameter Name Cn Pb Ni Ag Zn TTO Parameter Number 00720 01051 01067 01077 01092 - value 1.20mg/10.15mg/1 0.60mg/10.43mR/11.50mg/1 2.13mg/1. FOR AGENCY USE :ti• ti STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2. Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b 404a 404b 405 Bassett Walker N006 Pipe 1 2500 Airport Road Kinston Lenoir North Carolina 28501-2300 2200 & 2300 Tee Shirts & Sweat Suits 403c 403d Quantify 2, 250 thousand gallons per day 0 Intermittent(int) El Continuous (con) XI] Yes 0No 403e 403f Units(See Table 1111 Parameter Name Flow BOD TSS pH As Cl- Cr Parameter Number 50050 00310 00530 00040 01002 00940 01034 Value 2.25mgd 4170 1bs4170 lbs 6 - 9 0.831bs - 0.83 lbs Parameter Name Cu Cn Ni Zn P Parameter Number 01040 00720 01067 01092 00665 Value 5.00 lbs0.66 lbs2.50 lbs 3.33 lbs - A _ FOR AGENCY USE STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2 Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 4011 402 403a 403b • 404a Lenox China N005 Pipe 1 1800 Dobbs Farm Road Kinston Lenoir North Carolina 28501 3262 Fine China 403c 403d Quantiv /40) thousand gallons per day 404b Intermittent(int)E Continuous (con) 405 Yes Ei No 403e 4031 Units(See Table III1 Parameter Name STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2 Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 4011 402 403a 403b • 404a Lenox China N005 Pipe 1 1800 Dobbs Farm Road Kinston Lenoir North Carolina 28501 3262 Fine China 403c 403d Quantiv /40) thousand gallons per day 404b Intermittent(int)E Continuous (con) 405 Yes Ei No 403e 4031 Units(See Table III1 Parameter Name Flow BOD TSS pH Pb Zn P ' Parameter Number 50050 00310 00530 00040 01051 0.161bs 01092 0.07 lbs 00665 - Value 0.04mgd 66 mg/1 100 mg/I, 6 - 11 Parameter Name Parameter Number Value FOR AGENCY USE i... -: .. : 1 ?:.:- [t4 ....4 . ::.- ,... r M. E.4-%.. :::. t f 1.1 STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system, using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry, the major product or raw material, the flow (in thousand gallons per day), and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code 2. Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 401f 402 403a 403b 404a 404b 405 403c 403d Quantity thousand gallons per day Intermittent(*) 0 Continuous (con) Yes No 403e 4031 Units(See Table 111) 04 '• • Parameter Name , isi: .,• • Parameter Number Value FO1-i AGENCYUS-t ' j:$ji.. STANDARD FORM A - MUNICIPAL SECTION IV. INDUSTRIAL WASTE CONTRIBUTION TO MUNICIPAL SYSTEM Submit a description of each major industrial facility discharging to the municipal system. using a separate Section IV for each facility description. Indicate the 4 digit Standard Industrial Classification (SIC) Code for the industry. the major product or raw material. the flow (in thousand gallons per day). and the characteristics of the wastewater discharged from the industrial facility into the municipal system. Consult Table III for standard measures of products or raw materials. (see instructions) 1. Major Contributing Facility (see instructions) Name Number & Street City County State Zip Code v 2. Primary Standard Industrial Classification Code(see Instructions) 3. Primary Product or Raw Material (see instructions) Product Raw Material 4. Flow Indicate the volume of water discharged into the municipal sys- tem in thousand gallons per day and whether this discharge is intermittent or continuous. 5. Pretreatment Provided Indicate if pretreatment is provided prior to entering the municipal system 6. Characteristics of Wastewater (see instructions) 401a 401b 401c 401d 401e 4011 402 403a 403b 4b4a 404b 405 Intermittent(int) 0 Yes 403c 403d Ouanti y thousand gallons per day 0 Continuous (con) El No 403e 4031 Units(See Table III) r , 4•••::': > :.;.�; Parameter `ti , ig§ ;4 Name Parameter I 406a , .;: A,. :.�*� Number Value ' f 446b �4�. SLUDGE L OAOINC STATION V.B. IC SLUDGE DI SCUN STA CAUSTIC FEED • TION WASTE NIP ATIO AWN FEED POLYMERFEED SYSTEM EXHIBIT 1-1 SCHEMATIC 'FLOW *DIAGRAM • PEACHTREE 'WASTEWATER `TREATMENT PLANT CHLORINE CONTACT cITANKS IiTiIiI POST AERATION *a ui iflrr FEED SYSTQI ,�,.r NOSE RIVER • 5/41o6E15 WASTED To 7t/5 Di ibit MIFo t PRlf2y AE T/DAv'1N1 Xi G, ai slog 6 : WED Fqq 410749NN. Mlxw& AND ere4W7)f A v11- r 1 POLYMER FEED SYSTEM 1 1 1 ALUM FEED SYS CAUSTIC FEED SYS PARSHALL FLUME LINFLUENT D281AIBUTION SOX 6 A 74$600 STABILIZED SLIME TO APPLICATION DIGESTED SLOE A 748.00 IF/ER CHLORINE FEED SYSTEM NOTE THETERED SLUDGE FRoil__ThE SLUDGE DRUM MILL osaR AT WO APPLICATION BITE SLUM BAYING-~ BEDS POST AERATIONI I111'11I EFFLUENT' RECEIVING ST FEW: SSYSTEM : skud�e ; ' d .R ,5 Ram ies4 used foR,Ackghowy /4 EXHIBIT I�-1 D: 3 e'•c�- +►9. ^�9 R Jqpp4S,w eof ti►�� tOta SCHEMATIC FLOW DIAGRAM �;`t°��d�.FoRje� �oR s�. NORTHSIDE WASTEWATER TREATMENT PLANT 6E OF 1 a, ob ApPLKATin,� - Pzafeot Costa and Term VIA. Coss, We genre proposed on.the basis of 8 "turn Key' program. Ow costs Include ati permitting, a, monitoring, reporthg, loading, hauNng, and spreading. 1.) Land applying biosolids dire& from Peachtree Plant minimum 50O,00O gallon per sentice. . . Per Gamin 2.) Land applying biosolids direct from Nark Plant rr nuP a t'5Q0,00O gallon per service. Per Griffon litLIZAL a) !w8pert blosolids f:om Peachtree Plant to Northslde Plant. Per Gaon ,DM 4.) Land apply bioeofds p by either plant from Nordside pint Storage Tank. Mbiknum1,,OQ9 gallons per service. Per (;ems '• 5.) Ume Stabilize NOM ode utlizig existing minimum 500,000 gaion Per batch at 1-4% solids.. Per Gallon, .. Not0: C,P.t.• :' • AWMS earnsto funtith all if the ec limn and labor necessary and to perform all of the work and servicesdesaThed in this 'ifor the above project costs. The amourita,sistlirth shell be waisted at the beginning of the second year and each atiisequest year of the term according to the pement of change in the Consurner'Prce Index *Wished by the Bureau of Labor Statistics, Unitedd States Department oftabor: •: VLQ. • The term of this cones wl-be for a five year period with renewal ohs -for a period of five -years each as muksally agreed upon. III. kayo Planning and Organization III.A. Proposed Biosolids Management AWMS has developed a Management and Disposal plan for City Biosolids that is specifically designed to achieve the goals of the City, which we see as providlng an "Environmentally Safe and Cost Effective Land Application Program." The program must be sensitive and flexable so as to handle the biosolids production and meet the City's demands over the future years. We view the City of IGnston's program as a two phase program: Phase One - Before Force Main Installation Phase Two - After Force Main Installation During Phase One AWMS would toad and haul Biosolids from each plant independently of one another. The biosolids would be loaded direct from the existing aerobic digesters at each plant. After the Force Main completion Phase Two would begin, all biosoldids would be hauled from the existing 1,496,000 gal. basin at the Northside Plant, in addition any time stabilization needed would be performed in that same tank, however during phase one the stabilization process could be performed in the individual aerobic digesters if neccessary. AWMS will if requested provide personnel to show the City different ways to decant the aerobic digesters inorder to increase solids concentrations. Alternatively if the City desired or it became a necessity AWMS could haul excess biosolids from the Peachtree Plant to Northside for storage until permits are received. (See Project Cost Section). 111.B. Land Requirergeg#s Based on our experience and calculations using the information provided the City's Biosolids production will produce from 82.5 lbs. of PAN to 137.5 lbs. of PAN a day or 30,112 to 50,187 lbs. of PAN annually. Assuming an average application rate of 200 lbs. of PAN per acre per year the program would require 250 Acres be used per year. Recognizing crop cycles, weather conditions, and needs the plant may have we recommend and propose the program contain a minimum of 500 A. and ultimately increase that to 1000 A. over a period of time. During the first year we would propose that over the first 90 days of the contract we acquire the permits on the 300 acres the City presently has land owner agreements on and then during the remainder of the first year add an additional 200- 500 Acres to the permit ultimately reaching 1000 Acres by the end of the third year. AWMS can assure the City by following this plan, they would always have adequate land available to handle their biosolids re -use needs. t11.C. Manpower and Equipment AWMS will provide the following manpower and equipment to provide our services to the City: 1. Project Manager - 2. Project Superintendent 3. Agronomist/Soil Scientist - 4. Field Operator 5. Field Laborer 8. Truck Drivers 7. Terra-Gator Model 2505 8. Tractor -Trailer Tankers (7,000 gal.) 9. Superintendent Pick-up 10. Emergency Response Trailer 11. Miscellaneous pumps etc. J. Gary Steele William Taman Rob Wilcox 4 ea. 1ea 4 ea. 1 ea. 1ea. (as needed) Proposctd Method of plopolids Disposal We are very proud of the success of the Agronomic Land Application Programs we manage for clients throughout the southeast and propose the same type program for the City of Kinston. AWMS is pleased to provide the City with our team of highly qualified professionals. The following describes our method of biosolids disposal or more appropriately put recycling program. Following loading at the WWTP, biosolids will be transported to the application sites using the most direct primary and secondary state highways. The drivers will be instructed to avoid residential areas where possible. Prior to intiating field operations. the farm operator will be contacted relative to available fields, specific field conditions, anticipated cropping schedule, and whether fields have been Limed to required Ph levels. Field conditions will only be deemed acceptable when both the farm operator and the project superintendent concur. Trucks will be unloaded in the field at designated staging areas. To minimize field compaction by application and truck traffic, staging areas will be selected in regard to buffer restrictions, topography, access, farm management concerns, and soil conditions. Although several staging areas wiU be required for the typical field, all efforts will be made to minimize the effects of staging areas. Liquid biosolids will be recycled using one or more AgChem Terra-Gators depending on the volume to be applied. The biosolids wil be removed from the tankers using the vacuum pump on the Terra-Gator. The Terra-Gator will be equipped to allow surface or subsurface application of the liquid biosolids. All field equipment wcft be equipped with high floatation tires to minimize soil compaction. Prior to leaving the application site, the transport trucks will be scraped along the wheels, mud flaps, tailgate, etc. to minimize trucking mud onto public roads. Drivers wM be instructed on the importance of preventing mud from being tracked onto roads relative to the public perceptions of site activities and safety considerations. Once the area of the farm has received the designated application rate, the biosolids applications operation will relocate and phase out the staging area Each site will be inspected by the project superintendent prior to application, during, and after phase out to insure proper operations. The AWMS team continually monitors, supervises, and inspects ail operations to insure a safe and smooth operation. In the unlikely event an accident occurs or some other spill or emergency arises we have developed Spill Prevention and Emergency Spill Controls, Containment, and Clean-up Plans. 111.E. Spill Prevention Plan The spill prevention plan requires that all equipment used to transport Biosolids be subject to periodic safety inspections. fires, brakes, fights, and turn signals will be inspected for proper working order. Each truck will be equipped with safety flares and appropriate signs to be used in the event of a breakdown. Any deficiencies observed during the safety inspections will result in the vehicle being removed from service. Routes leading from the plant to the disposal sites will be inspected for road hazards. The road hazards will be documented and drivers will be informed of the hazards. Alternate routes will be investigated and routes which minimize road hazards will be selected. Hazardous situations resulting from rush-hour traffic will be avoided during the hauling of residual solids. Drivers and management personnel associated with the hauling of biosolids will be instructed in the spill prevention plan and will be required to attend training sessions. Drivers will be trained in defensive driving techniques in order to minimize road hazards. A driver who observes a road hazard will be required to report the hazard to the dispatcher who, in turn, will wam other drivers who will be hauling residual solids. As part of the spill prevention plan, drivers will be required to inspect the safety equipment on their vehicles on a daily basis. Any deficiency in safety equipment will be noted for corrective action. Drivers will be trained in the procedures to be taken in the event of a spill that occurs during the hauling of residual soUds. These procedures are discussed in the spill control, containment, and cleanup plan. tt1.F. SpW Contpt. Containment. and Cleanup Flan Spills that occur during loading or unloading blosolids will occur at the generation point and the disposal point, respectively. These spills will not involve an environmental hazard or an over -the -road hazard and, therefore, will be handled using the equipment that will be available at either site. Spills that occur over -the -road will be subject to the contingencies contained in the spill control containment and cleanup Plan. All personnel associated with the hauling of biosolids will be trained in the procedures to be taken in the event of a spill. The equipment used in the spill control containment and cleanup consists of the following: 1. An emergency response vehicle. This vehicle is maintained on a 24-hour state of readiness. The emergency response vehicle is a pick-up truck and trailer. Loaded within the pick-up are absorbents, spin containment equipment, barricades, sand bags, tools, and flares for the rerouting of traffic. 2. Vacuum pump and Tanker Truck. The vacuum pump and tanker truck wiU be used to cleanup liquid residual solids spills. 3. Front End Loader. Low Elpy. and Dump Truck. This group of equipment will be used to cleanup any necessary soils. 4. Byoom T1#or. Used to sweep roadway. 5. Truck and High Pressure Pump. The tanker truck and a high pressure pump will be used to wash the surface of the pavement after the residual solids have been removed. The following personnel will be involved in spill control, containment, and cleanup. 1. Project Superintendent. The field superintendent is on notice 24 hours a day. The field superintendent will respond by driving the emergency response vehicle to the spill site with an assistant and make an assessment of the spill and determing the containment procedures to be initiated and the equipment to be used to clean up the spill. 2. Cleanup Team Memberr. The cleanup team wiU consist of the Project Superintendent, equipment operators and laborers. The Project Superintendent WU be responsible for the direction of the cleanup team. Each member of the cleanup team will be trained in cleanup actions. Spill Contrail. Containment. Arid Clete Procedures In the event of a spill, the driver of the truck, if he has not sustained a debilitating injury, will call the project superintendent and report the spill. The project superintendent will notify the appropriate authorities and will also mobilize the clean-up team. The driver will set safety flares and signs to wam motorists of the hazard. The Project Superintendent will mobilize the necessary equipment and personnel to the site, and he and his assistant will initiate containment procedures. When the cleanup team arrives at the site, the site will be deaned up in accordance with the contingency plan. Blosoffds cleaned up from the site will be transported to the disposal area where it will be disposed of in accordance with the operational plan. On each anraversary date of the contract, the spill control, containment, and cleanup plan will be reviewed and appropriated changes will be made if necessary. AN personnel associated with the transportation and application of residual solids will be required to become familiar with the spill control, containment, and cleanup plan. M.G. Lime Stabilization AWMS proposes to lime stabilize biosolids on an as needed basis. We will furnish all labor, euipment, and materials needed except we plan to use the existing aerator in the various tanks to assist in mixing. The city would be responsible for furnishing the electricity for operation and to keep them in good working order. The ideal facility to be used for the stabilization process would be the 1,496,000 gal tank at the Northside Plant, however, if an emergency was to arise the individual digesters could be used. After the completion of the force main (Phase Two), AWMS proposes to use only the Northside Facility for the Stabilization Process. Kinston WWTP Fs o&m Page (5 ) I. SYSTEM DESCRIPTION: The following system description is intended to convey the intended equipment supplied for the Two (2) U.S. Filter FILTER SCREEN unit(s) supplied to Kinston, NC. Although multiple systems may be supplied under this order, the system description is written in reference to a single operating system. Refer to installation drawing attached. A. EQUIPMENT: The equipment to be furnished will be a self-cleaning bar/filter screen. The equipment will be of the latest design and will be fabricated of materials and in a fashion which will perform the functions described below. The equipment shall be installed in the flow channel by others as shown on the drawings. The filter screens are a Model FS304-41-168 with i( inch openings for the Peachtree Plant and a Model FS304-41-150 with W inch openings for the Northside Plant manufactured by U.S. Filter. The unit will be furnished and installed with stainless steel foundations and supports; mechanical equipment required for proper operation, including drive units as indicated by these submittal drawings. B. SCREENING EQUIPMENT (OPERATION): The heavy-duty, mechanical self-cleaning bar/filter screen will be suitable for installation and operation in a flow channel measuring 48 inches wide x 60 inches deep at the Peachtree Plant and a 42 inch wide x 60 inch deep channel at the Northside Plant, as measured from the base of the screen to the level at which it is supported. The angle of inclination shall be 75° from horizontal. The screen will provide continuous filtration of materials and minimize head loss through the screen. The screen will remove materials larger than .25 in diameter. The screen will continuously present a clean filtration surface .to the oncoming liquid stream. In addition to the fine materials, materials up to 3.31 in size will be transported by the screens for deposit into the Screw Compactors. The screen will be semi -self-cleaning by mechanical means without requiring brushes to remove the captured materials from Kinston WWTP Fs o8m Page [6 } the screen surface. A combination drive/unloading sprocket which both powers the screen assembly and discharges the screened materials from the screen will be provided. The sprocket segments will enter the screen openings from the inside and push the trash off the elements. The screen will have no rake mechanisms in close proximity to the screen. It shall be designed to prevent jamming or binding by eliminating rake mechanisms. The screen will require no mounting or fastening to the side walls or bottom of the channel. It will be possible to pivot or remove the screen from the channel for inspection or service without DEWATERING the channel. The screen will be provided with a water spray wash system designed to assist in the removal/discharging of debris from the screen. A solenoid valve will be provided with the screen, allowing the water flow to occur while the screen is operating and for an extended wash duration set by a timer in the control panel. C. SCREEN CONSTRUCTION: All moving wetted parts or all wetted parts on which the moving parts ride which include the pivot shafts, screen elements, guide rails and stationary frame will be corrosion - resistant and will be made of SS304 except as noted. No plastic filter elements will be used. The side seals will be made of neoprene rubber with SS304 supports. All nuts and bolts will be SS304. The guide links and element spacers will be high -impact UHMWPE. Stainless steel and/or other metal rollers and spacers will not be used in order to eliminate metal -to -metal contact. Other appurtenances including drive components, etc. will be US Filters standard corrosion -resistant materials. The UHMWPE guide links will ride on SS304 rails. A curved stainless steel shoe will be provided at the foot of the screen, eliminating the need for a sump. Units which require sumps, ramps or other channel floor alterations will not be acceptable. No submerged bearings, sprockets or chains shall be used. The screen will be factory assembled and tested prior to delivery and shall be delivered to the jobsite assembled. It will be capable of being set in place and field erected by the Installing Contractor with minimal additional field assembly. The drive unit is a SEW Eurodrive model K87R62 with a 613:1 reduction stage equipped with anti -friction bearings and designed in accordance with AGMA recommendations for 24 hours, Class II service. Input power will be by a 3/4 HP, 480 VOLTS/ a 0 s j i *`4 T OaWOO Is Mu Wager and Wasilastaite taikaary OPERATION Paso ION-6211-1 2 of 2 ISSUED APR. ' 74 PRoDucT ROLLING CRT UNIT =TWfl OFH$w= The frequency and duration of GritLift operation is dependent upon conditions which exist at your plant at a given time. This schedule can be determined only after observation of the flow patterns which develop. For instance, the quantity of grit entering your plant may not warrant continuous operation of the GritLift. On the other hand, if your plant is served by combined sewers, it is recommended, and maybe necessary, to operate the OritLift continuously during periods when storm flows are being received. In addition, certain seasons of the year may dictate varyingschedules of GritLift operation. Your plant may be equipped with a mechanical grit pump rather than a GritLift. In these cases, the sequence of operation is the same as described above for the GritLift j however, normal maintenance procedures for mechanical pumps must be allowed. Refer to the manu- facturer's instructions. HUDSON H TcOMPZECE The Hudson Retractable Footpiece is an exclusive feature available on a walker Process GritLift used in a rolling grit basin, and is used to restore pumping after an unusual grit load has been admitted to the basin. Figure 1 shows a normal -operating system in which grit is removed as it enters the hopper area. In times of heavy grit load, as in storm flaws with combined sewers, the grit deposited in the hopper may inundate the entry to the GritLift, stopping the pumping action (Figure 2) . The Hudson Retractable Footpiece, operable from above, can be raised such that pumping is again restored (Figure 3) and lowered gradually to pump away the deposit (Figure 4) to return to normal operation. 1 0161% fullasseeleam Wiitsvwawwe.wsMw Indu•rr air . OPERATION & MAINTENANCE I0IM-6211-5 PaDo 1 of 2 FEB.'86 PRODUCT ROLLING GRIT UNIT - ROLL AND GRITLIFT The Rolling Grit Unit consists of a "RollAer" eductor tube, a "GritLift" lift tube, a surface baffle, and a support bridge from which the above components are suspended. Roth lift tubes have their own internal air lines with diffusers. Absolutely no moving parts make up this assembly and, therefore, it is quite simple to operate and maintain. To start the RollAer Lift Tube in operation, all that is necessary is to open the main air valve and adjust this valve to the desired level. To assure proper and most efficient operation, the surface baffle is positioned at the operating liquid surface of the basin in which it is installed. The surface baffle is quite meant in the operation of the unit and, therefore, this is a consideration which must be strictly adhered to. Any deviation in the surface baffle from the liquid surface will reduce the surface velocities radiating from the basin centerline below optimum, and reduce the overall tank turnover.. Tank turnover and/or oxygenation level can also be adjusted by changing the guentity of airibeingg diffused into the eductor tube. • • IghlaniaraWa The only possible maintenance problem which should be encountered with the unit is fouling or clogging of the air diffuser. while the design of the walker Process diffuser bead, with its bottomless blow -off feature, precludes this occurrence to the maximum extent possible, rags and other stringy or fibrous material may, in time, cause a clogging of the blow -off and/or orifices. The preferred method of unclogging the orifices is to dewater the basin to gain direct access to the diffuser head. If this is not possible,then all air and grit lines must be disconnected at the bridge, the. . surface baffle removed, and the rolling grit unit lifted in a . vertical direction until the diffuser head and orifices are access- ible for cleaning. GEMTLITTOPERATION All that is required to start the GritLift is to open the air valve which feeds the internal air diffusion pipe. The air is to be adjusted to such a point that the pumping rate produced is at the desired level. Since the airlift principle dictates that the greater the quantity of air diffused into the lift tube, the greater the velocity of liquid within the tube, •the rate of pumping is more or less linear with respect to the quantity.of air diffused. 4' a.lbe«.e»gnaw WellUmalle �. a wr•..lONO a mamba OPERATIONT ION-6214-2 Pans 1 of 2 issuEo PRODUCT GRIT WASHER StiPEIRsEOEs MAR. 081 There are several es to the Walker'Process Grit Walther: 1) it is used as the race ving vessel for the grit and water being removed from the grit basin; 2) thru the mechanical action .of the screw, the Walker Process Grit Washer is used to transport the grit (inorganic) material to the discharge point; 3) the organic aaterals are returned to the plant flow by the overflow weir system. The Grit Washer must be placed into operation Marl any �ttis pumped to the receiving portion of the unit. Similarly, he duration of the grit pumping has been terminated, the een grit washer should be left in operation until the grit completely. Supplemental wash water is not required when a ritLift or aechsnical pump is used to feed the Walker Process Grit Supplemental wash water is required when a dry grit isb the transportedto a Grit Washer. These situations grit is being removed from the grit basin by a bucket elevator, or other mechanical elevating device. In these cases, a. non -potable water supply is fed at the upper end of the Grit Washer screw to provide the •necessary volume to remove the organics from the grit c) material and return then to the plant flow. Other instructions given above for the Grit usher appurtenances and accessories should be followed. Form KE8