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HomeMy WebLinkAboutWQ0005763_Application_20100715McGifl A S S O C I A T E S July 15, 2010 Mr. Jon Risgaard North Carolina Department of Environment And Natural Resources Division of Water Quality 2728 Capital Boulevard Raleigh, North Carolina 27604 Dear Mr. Risgaard: r"ECEw ® i' JG 13 2610 Asheville regional Office Re: Distribution of Residual Solids Tuckaseigee Water and Sewer Authority Wastewater Treatment Plant No. 1 Jackson County, North Carolina On behalf of the Tuckaseigee Water and Sewer Authority (TWSA), please find attached application for major modification to the Distribution of Residual Solids Permit No. WQ005763. TWSA is expanding WWTP No. 1 from 1.5 mgd to 3.5 mgd and will utilize a sludge dryer to produce a. ' Class A residual. Application package includes "Distribution of Residuals Solids Application"; "Residuals Source Certification Attachment(RSCA) for WWTP No. 1 and RSCA for Whittier, application fee, three (3) sets of detailed plans and specifications, Engineering Calculations, and Residuals .Management Plan. Note that the Whittier Facility has not produced any residuals to date and sampling data in RSCA is from WWTP No. 1. An Authorization to Construct has been previously issued by Construction, Grants and Loans for the proposed project. Information required by Item 5 in the application is included in the Residuals Management Plan. If you have any questions or need additional information please don't hesitate to give me a call at 828-252-0575 or email at davidh e,mcgillengineers.com. Thank you for your assistance. Sincerely, McGILL ASSOCIATES, P.A. DAVID L. HONEYCUTT, PE Project Engineer Enclosures cc: Joe Cline, Tuckaseigee Water and Sewer Authority RECEIVED / DENR / DWQ Harry Buckner, PE, McGill Associates, P.A. Aquifer Protection Section P:\2005\05734\Letters\jrI3julyIO.doc JUL 19 2010 E n g i n e e r i n g 0 P l a n n i n g F i n a n c e McGill Associates, P.A. • P.O. Box 2259, Asheville, NC 28802 • 55 Broad Street, Asheville, NC 28801 828-252-0575 • Fox.828-252-2518 AQUIFER PROTECTION SECTION APPLICATION REVIEW REQUEST FORM Date: To: ® Landon Davidson, ARO-APS ❑ David May, WaRO-APS ❑ Art Barnhardt, FRO-APS ❑ Charlie Stehman, WiRO-APS ❑ Andrew Pitner, MRO-APS ❑ Sherri Knight, WSRO-APS ❑ Jay Zimmerman, RRO-APS From: Alice M. Wessner ®LAU E-Mail: alice.wessner@ncdenr.gov Telephone: (919) 715-5208 A. Permit Number: WQ005763 C. Facility/Operation: ❑ Proposed ® Existing D. Application: MG 13 2610 Asheville Regional Office Fax:(919) 715-0588 Aquifer Protection B. Owner: Tuckaseigee WASA ❑ Facility ❑ Operation I. Permit Type: ❑ Animal ❑ Surface Irrigation ❑ Reclaimed ❑ H-R Infiltration ❑ Recycle ❑ I/E Lagoon ❑ GW Remediation (ND) ❑ UIC - (5A7) open loop geothermal ❑ Single Family Residence ® Residuals 2. Project Type: ❑ New ® Major Mod. ❑ Minor Mod. ❑ Renewal ❑ Renewal w/ Mod. E. Comments/Other Information: ❑ I would like to accompany you on a site visit. Attached, you will find all information submitted in support of the above -referenced application for your review, comment, and/or action. Within 30 calendar days, please take the following actions: ® Return a Completed APSARR Form. ❑ BIMS indicates monitoring wells locations are not complete. Please update monitoring well locations not currently in BIMS. ® BIMS indicates ongoing ❑ NDMR ❑NDAR ❑ GW monitoring violations. Please investigate reoccurring compliance issues and summarize results in staff report. NOV for Monitoring ❑ Attach Well Construction Data Sheet. ❑ Process Attachment B for Certification by the Land Application Unit (LAU). ❑ Issue an Attachment B Certification from the RO.* *coordinating site visits and reviews, as well as additional information requests with other RO-APS representatives in order to prepare a complete Attachment B for certification. Refer to the RPP SOP for additional detail. Please indicate the name and date assigned in the spaces below, make a copy of this sheet, and return it to the appropriate Central Office -Aquifer Protection Section contact person listed above. RO-APS Reviewer: --,7, C '-) -'_� Date: FORM: APSARR 03/10 Page 1 of 1 Price, Bev From: Wessner, Alice Sent: Friday, October 08, 2010 11:31 AM To: Price, Bev Subject: FW: Tuckaseigee-Whittier RSCA Attachments: Whittier RSCA.pdf For your records. Alice M. Wessner Environmental Engineer Land Application Unit Aquifer Protection Section Division of Water Quality 1636 Mail Service Center Raleigh, NC 27699-1636 919-715-5208 919-715-0588 (fax) http://h2o.enr.state.nc.us/aps/lau.htm From: David Honeycutt[mailto:david.honeycutt@mcgillengineers.com] Sent: Friday, October 08, 2010 8:10 AM To: Wessner, Alice Subject: Tuckaseigee-Whittier RSCA Alice, Please find attached RSCA for Whittier. Per our discussion as they have not hauled any solids from the Whittier facility (at the time of application) there is no sample data available for solids produced at that facility. It is a 100% domestic facility and sample data in the RSCA is for the Tuckaseigee Water and Sewer Authority Plant No. 1 which is expected to be similar. Please let me know if you are missing any other supporting documentation listed on the last page of this PDF. Thanks for your assistance on this permit modification. Please don't hesitate to give me a call or email if you have any questions. Thanks, David L. Honeycutt, PE Project Engineer McGill Associates, P.A. Phone 828-252-0575 Fax 828-252-2518 State of North Carolina Department of Environment and Natural Resources Division of Water Quality RECEIVED / DENR /D WQ DISTRIBUTION OE RESIDUAL SOLIDS Protection Section JUL(FORM: DRS 070807) 19 2010 The Division of Water Quality will not accept this application unless all the instructions are followed. Plans and specifications must be prepared in accordance with 15A NCAC 2T .1100, and good engineering practices. Failure to submit all required items will lead to additional processing and review time. For more information, visit our web site at: http://h2o.e ar.state.n.c.iis/laufinain.html A. Application Form (All Application Packages): ✓ Submit one original and two copies of the completed application package. Any changes made to this form will result in the application being returned. The Division of Water Quality will only accept application packages that have been fully completed and all applicable items are addressed. ✓ The project name should be consistent on the plans, specifications, etc. ✓ The signing official must meet the criteria stipulated in 15A NCAC 2T .0106(b). An alternate person may be designated as the signing official, provided that a delegation letter from a person who meets the referenced criteria is submitted. The delegation letter does not have to be resubmitted if the signing official has not changed since the last permitting action associated with this residuals land application program. ✓ If this project involves a modification of an existing permit, submit one copy of the existing permit. ✓ Please submit this application form at least 180 days prior to the expiration date on the existing permit, or 90 days prior to operation of proposed facility(ies) for application packages involving new or changes to treatment and storage units. B. Application Fee (New and Major Modification Application Packages): ✓ For new permits submit a check in the amount of $1,310 if over or equal 3,000 dry tons per year are generated for disposal or $810 if less 3,000 dry tons per year are generated for disposal, made payable to: North Carolina Department of Environment and Natural Resources (NCDENR). Major modification fee are $395 and $245, respectively. C. Cover Letter (All Application Packages): ✓ Submit a cover letter, which lists all item and attachments included in the application package as well as a brief project description. ✓ If necessary for clarity, include attachments to the application form. Such attachments will be considered part of the application package and should be numbered to correspond to the section to which they refer. D. Retailed Plans and Specifications (Application Packages Involving New or Changes to Treatment and Storage Units): ✓ Submit three sets of detailed plans and specifications signed, sealed, and dated by a NC Professional Engineer per 15A NCAC 2T .1104(a). Specifications for standard equipment may only be omitted for municipalities with approved standard specifications, but use of the standard specifications must be noted on each sheet of the plans. ✓ Plans must include the following minimum items: a general location map, a topographic map, plan and profile view of the residuals treatment and storage units as well as the proximity of the residuals treatment and storage units to other utilities and natural features within 500 feet of all treatment and storage facilities, and detail drawings of all items pertinent to the residuals treatment and storage units. Depict minimum separations required in 15A NCAC 2T .1108 (a) on the plans. ✓ Specifications must include, at a minimum, the following for all items pertinent to residuals treatment and storage units: description of materials to be used, methods of construction, quality of construction testing procedures to ensure the integrity of the final product in accordance with 15A NCAC 2T .1104(a)(2)(B), including leakage and pressure testing as appropriate. Plans and specifications must not be labeled with preliminary phrases (e.g., FOR REVIEW ONLY, NOT FOR CONSTRUCTION, etc.) that indicate that they are anything other than final plans and specifications. However, the plans and specifications may be labeled with the phrase: FINAL DESIGN — NOT RELEASED FOR CONSTRUCTION. E. Engineering Calculations (Application Packages Involving New or Changes to Treatment and Storage Units): ✓ Submit three copies of all design calculations signed, sealed, and dated by a NC Professional Engineer per 15A NCAC 2T .1104(a). ***INSTRUCTIONS CONTINUE ON NEXT PAGE (, r V E D FORM: DRS 070807 Page 1 of 6 A,'��a 1� 24�tachinenU Order 1 .Anhovill' Regional Office r F. Environmental Assessments (Maybe Required— See 15A NCAC 1C .0300): ✓ Submit one copy of the Findings of No Significant Impact (FONSI) or Environmental Impact Statement (EIS). Also, include information on any mitigating factor(s) from the Environmental Assessment (EA) that impact the construction of the residuals treatment and storage facilities. An EA may also be required for private systems if any public funds and/or lands are used for the construction of the subject facilities. G. Residuals Source Information (All Application Packages): ✓ Attach FORM: RSCA (Residuals Source Certification Attachment) and all associated documentation. ✓ FORM: RSCA can be downloaded at http://h2o.enr.state.nc.us/lau/gl2lications.litml 2610 Asheville Regional Office --A-g�aifer Protection FORM: DRS 070807 Page 2 of 6 Attachment Order 1 State of North Carolina Department of Environment and Natural Resources Division of Water Quality DISTRIBUTION OF RESIDUAL SOLIDS (FORM: DRS 070807) (THIS FORMMAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL) Application Number: (to-b"o»apteted-by L)-W- I. OWNERSHIP INFORMATION: RECEIVED 1. Specify whether the process facility is owned by: `A.Ijb Zb ot� ❑ County; ❑ Federal; N Municipal; ❑ State; ❑ Non -Government. g Asheville Regional Office I /= ouifer Protection 2. Owner's name (please specify the name of the municipality, corporation, individual, etc.): TUCKASEIGEE WATER AND SEWER AUTHORITY Mailing address: 1246 West Main Street City: Sylva State: North Carolina Zip: 28779 Physical address: 1246 West Main Street City: Sylva State: North Carolina Zip: 28779 Telephone number: ( 828 ) 586-5189 Facsimile number: ( ) E-mail address: jcline@twsanc.org 3. Signing official's name and title: (See Instruction A) Robert J. Cline. Executive Director Mailing address: 1246 West Main Street City: Sylva State: North Carolina Zip: 28779 Physical address: Same as above City: State: Telephone number: ( 828 ) 586-5189 Facsimile number: ( E-mail address: icline@twsalic.org H. PERMIT INFORMATION: Zip: 1. Application is for: ❑ new; ® modified; ❑ renewed permit (check all that apply). 2. Fee Submitted: $ 245 (See Instruction P) 3. If this application is being submitted to renew or modify an existing permit, provide the following: Permit number: WQ0005763 (please attach a copy of the existing permit). Most recent issuance date: August 26, 2005 , and the expiration date: July 31, 2010 RECEIVED IDENRIDWQ Aquifer Protection Section FORM: jDRS 070807 Page 3 of 6 JUL 19 2010 Attachment Order 1 M. FACILITY INFORMATION: 1. Name of facility where residuals are processed: TWSA WWTP Plant No. 1 Physical address: 1871 North River Road City: Sylva State: North Carolina Zip: 28779 Telephone number: ( 828 ) 586-9318 Facsimile number: ( County where facility is located: Jackson County Latitude: 350 21' 02" Longitude: 830 14' 15" of residual process facility. 2. Facility contact (person familiar with residuals preparation): Stan Bryson Mailing address: 1246 West Main Street City: Sylva State: North Carolina Zip: 28779 Physical address: 1871 North River Road City: Sylva State: North Carolina Zip: 28779 Telephone number: ( 828 ) 586-9318 Facsimile number: ( ) E-mail address: 3. Program contact person and/or consulting firm who prepared application (If different from the above): Harry B. Buckner P E McGill Associates P.A. Mailing address: Post Office Box 2259 City: Asheville State: North Carolina Zip: 28802 Physical address: 55 Broad Street City: Asheville State: North Carolina Zip: 28801 Telephone number: ( 828 ) 252-0575 Facsimile number: ( 828 ) 252-2518 E-mail address: hbbuckner(@mc ig llenaineers com 4. Is the residual process facility also the generator? ® Yes; ❑ No 5. If the residual process facility is not the same as the generator, please specify delivery frequency and quantity of residual to be processed: n/a 6. Length of residuals storage at facility: 30 (liquid) days (the Division requires a are separate from treatment system, i.e. not in clarifiers, aeration basins, etc.). IV. RESIDUALS QUALITY INFORMATION: 1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or U��C OVED jA'JG 10 2G ►G jCIjevill114.0"c�FBJ(PRT4P;7ff ice AaLlifer Protect_ iOn FORM: DRS 070807 Page 4 of 6 Attachment Order 1 up 2. Specify how these residuals will be distributed: ❑ sold or given away in bags or other containers; ® lawn (bulk); ® home garden (bulk); ❑ other; 3. Complete the following if residuals are to be mixed with other materials: Type of Materials I Amounts to be added per 1.0 dry ton of residuals (dry ton) 4. Approximate amounts of the final product to be distributed 659 dry tons per year. 5. Provide a description of the onsite storage management plan for the treated residuals (including estimated average and maximum storage times prior to distribution): Solids from the diver will be discharged to an 86 cubic foot storage hopper. Solids from the storage hopper will be conveyed by a blower system to a 94 cubic yard storage silo. Dried sludge will be conveyed from the storage silo to the end -users The storage silo will provide 35.2 days of storage at the permitted design flow for the facility. The anticipated average storage time is 14 days. ADDITIONAL REQUIRED INFORMATION: 1. Provide a narrative explaining the following: a. How will the materials be handled and transported from where the residuals were produced to where it will be treated? b. How will the residuals be processed/treated (attach process flow diagram). c. How will leachate collection be handled? d. Where will the residuals be stored until processed? e. How will the final product be distributed (packaging)? 2. Attach a marketability statement detailing destinations and approximate amounts of the final product to be distributed. 3. Provide either a label that shall be affixed to the bagged processed residual or an information sheet that shall be provided to the person who receives the processed residual. The label or information sheet shall contain, at a minimum, the following information: a. The name and address of the person who prepared the residual that is sold or given away in a bag or other container for application to the land. b. A statement that application of the residual to the land is prohibited except in accordance with the instructions on the label or information sheet. c. A statement that the residuals shall not be applied to any site that is flooded, frozen or snow-covered. d. A statement that adequate procedures shall be provided to prevent surface runoff from carrying any disposed or stored residuals into any surface waters. e. Information on all applicable setbacks in accordance with 15A NCAC 02T .1108(b). f. A statement that the residuals shall be applied at agronomic rates and recommended rates for intended uses. dA°JG 1 ^ 2G I0 FORM: DRS 070807 Page 5 of 6 P Asheville regional Off&ttacl" ent Order 1 Atmil`or Protection Professional Engineer's Certification: (Application Packages Involving New or Changes to Treatment and Storage Units) I, Harry B. Buckner, P.E. , attest that this application for Tuckaseigee Water and Sewer Authority Wastewater Treatment Plant No. 1 has been reviewed by me and is accurate and complete to the best of my knowledge. I further attest that to the best of my knowledge the proposed design has been prepared in accordance with the applicable regulations. Although certain portions of this submittal package may have been developed by other professionals, inclusion of these materials under my signature and seal signifies that I have reviewed this material and have judged it to be consistent with the proposed design. North Carolina Professional Engineer's Seal, Signature, and Date: ,`�� till !0 •• �s • v 'L 0 a g SEAL • 0 22541 a a Applicants Certification: ordReaaittd The applicant or any affiliate has not been convicted of an environmental crime, has not abandoned a wastewater facility without proper closure, does not have an outstanding civil penalty where all appeals have been exhausted or abandoned, are compliant with any active compliance schedule, and do not have any overdue annual fees under Rule 2T .0105. ® Yes ❑ No, Explain; I, Robert J. Cline , attest that this application for Tuckaseigee Water and Sewer Authority has been reviewed by me and is accurate and complete to the best of my knowledge. I understand that if all required parts of this application are not completed and that if all required supporting information and attachments are not included, this application package will be returned "e as incpnplete. Signature Date ?r � r /d THE COMPLETED APPLICATION PACKAGE, INCLUDING ALL SUPPORTING INFORMATION AND MATERIALS, SHOULD BE SENT TO THE FOLLOWING ADDRESS: NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES DIVISION OF WATER QUALITY AQUIFER PROTECTION SECTION LAND APPLICATION UNIT By U.S. Postal Service: 1636 MAIL SERVICE CENTER RALEIGH, NORTH CAROLINA 27699-1636 By Courier/Special Delivery: 2728 CAPITAL BOULEVARD RALEIGH, NORTH CAROLINA 27604 TELEPHONE NUMBER: (919) 733-3221 FORM: DRS 070807 Page 6 of 6 Attachment Order 1 State of North Carolina Department of Environment and Natural Resources Division of Water. Quality RESIDUALS SOURCE CERTIFICATION ATTACHMENT (FORM: RSCA 070807) (THIS FORMMAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL) The Division of Water Quality (Division) will not accept this attachment unless all the instructions are followed, Failure to submit all required items will lead to additional processing and review time. For more information, visit our web site at: h1tp•//It2o erv:state.itc.irsllatilntaln.htnil .INSTRUCTIONS TO THE APPLICANT: _ A. Attachment Form: ✓ Do not submit this attachment form for review without a corresponding residuals program application form (FORM: NDRLAP, FORM: DRS, or FORM: SDRS). ✓ Any changes to this attachment form will result hi the application package being returned. ✓ For new residuals programs or renewe residuals programs, submit a separate attaclunent form for each residuals source -generating facility to be certified for this residuals program. ✓ For modified residuals programs in which any modification to the certified residuals -source generating facilities is proposed, submit a separate attachment form for oil those residuals source -generating facilities that are affected by the proposed modification. ✓ The attachment should be organized prior to submission in the following order (i.e., by facility): ♦ Attachment Order 2: Residuals;Source Certification Attachment (FORM: RSCA). ➢ Attachment Order 2-a: Vicinity map. ➢ Attachment Order 2-b: Process flow diagram and/or narrative. ➢ Attachment Order 2-c: Quantitative justification for residuals production rate. ➢ Attachment Order 2-d: Sampling plan. ➢ Attaclunent Order 2-e: Laboratory analytical reports'and operational data.' B. Residuals. Source -Generating Facility hiformatlon: ✓ Attach a vicinity map that shows the location of the facility and meets all of the criteria in time latest version of the document entitled "Guidance for the Preparation of Vicinity/Buffer Maps for North Carolina Residuals Permitting Programs." . - ✓ Attach a detailed narrative and/or process flow diagram that describes how the residuals are to be generated, treated, processed, and stored at the facility. ✓ Attach a quantitative justification for the value provided in Item I. 8. Ensure that the amount of residuals listed is the maximum amount expected to be generated by the facility for the life of time permit. In addition, ensure that this amount is equivalent to that which is actually to be land applied, distributed, and/or disposed, including any chemicals, amendments, or other additives that are added to the residuals during processing. C. Residuals Quality Information: . • . . • . • • 1. ✓ Attach a detailed sampling plan for the residuals source -generating facility. Ensure that the plan identifies sampling points, sampling. frequency, sample type, as,well as-the•Division-certified laboratory to be used. In addition, ensure that the plan details how the facility. and/or the residuals are monitored for any applicable pathogen reduction and vector attraction reduction requirements. Note that all sampling and monitoring must be completed on the residuals as they are to be land applied, distributed, and/or disposed. ✓ Attach reports for all laboratory analyses used to complete this attachment form. Attach documentation that time facility complies and/or the residuals comply with any applicable pathogen reduction and vector attraction reduction requirements. ✓ Item II. 3. does not have to be completed for facilities that are less than 0.5 MGD in design flow that treat I 00°/anon-inunicipali• domestic wastewater. only. FORM: RSCA 070807 Page 1 of 8 Attachment Order 2 State of North Carolina Department of Environment and Natural Resources Division of Water Quality RESIDUALS SOURCE CERTIFICATION ATTACHMENT (FORM: RSCA 070807) (THIS FORMMAYBE PHOTOCOPIED FOR USE ASAN ORIGINAL) Applicant's name: Tuckaseigee Water and Server Authority Check all that apply: ❑ NEW RESIDUALS PROGRAM ❑ RENEWED RESIDUALS PROGRAM ® INCREASE ❑ DECREASE the maximum permitted annual dry tonnage for this residuals source - generating facility certified for this residuals program. Current: 250 Dry Tons/yr. and proposed: 659 Dry Tons/yr. ® ADD ❑ DELETE this residuals source -generating facility to/from those certified for this residuals program. I. ❑ OTHER Explain: RESIDUALS SOURCE -GENERATING FACILITY INFORMATION (See Instruction B.): 1. Name of facility: TWSA Whittier Sanitary District W WTP 2. Facility permit holder: Tuckaseiaee Water and Sewer Authority Facility permit holder is (check one): ❑ federal, ❑ state, ® local government, or ❑ private. Facility permit number: NPDES No. NCO087602 Facility permit issued by (check one): ® Div. of Water Quality, ❑ Div. of Environmental Health, or ❑ other (explain: )• 3. if the facility permit is not issued by the Div. of Water Quality, complete the following: a. Facility contact person and title: Facility complete mailing address: City: State: Zip: Telephone number: ( ) Facsimile number: ( } E-nail address: b. Facility complete location address: City: State: Zip: Latitude: and longitude: 4. County where facility is located: Jackson County 5. Purpose of the facility (check one): ® treatment of municipal wastewater, ❑ treatment of 100% domestic wastewater, ❑ treatment of potable water, ❑ treatment of 100% industrial wastewater, ❑ treatment of industrial wastewater mixed with domestic wastewater, or (approximate percentages: % industrial and % domestic) ❑ other (explain: FORM: RSCA 070807 Page 2 of 8 Attachment Order 2 6. Does the facility have an approved pretreatment program: ❑ yes ® no 7. Facility.permitted/dQsign flow: 0.1 MGD and facility average daily flow: <0.005 MGD. B. Average amount of residuals being generated at this facility �_ dry tons per year. 9. Specify the following regarding- lreatnieut and storage,volumes available at the facility: Type and volume of residuals treatment:. See Page 3 of the attached Residuals Management Plan. Type and volume of residuals storage (i.e,, outside of residuals treatment units): Dried Solids will be stored in a 94 CY storage silo which providesa roxim el 36.1 days of storage at the permitted design flow for the facility. II. REsIDUALs QUALITY INTORMATION (See Instruction C.): 1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or ❑ 40 CFR Part 257. 2. Specify if residuals are intended for (check one): ® Land Application/Distribution (Class A or Equivalent). Complete all items EXCEPT Items II.4b., 7b., and 7c. ❑ Land Application (Class B or Equivalent). Complete all items EXCEPT items II.4b., 7a., and 7c. ❑ Surface Disposal. Complete all items EXCEPT Items H. 4a., 5., 7a., 7b., and 8. FORM: RSCA 070807 Page 3 of 8 Attachment Order 2 3. Hazardous Waste Determination: Complete the following to demonstrate that the residuals are non- hazardous under RCRA: a. Are the residuals are listed in 40 CFR §261.31-§261.33: ❑ yes ® no. If yes, list the number(s): b. Specify whether or not the residuals exhibit any of the characteristics defined by 40 CFR §261.21- §261.24: ❑ yes ® no. Fill in the following tables with the results of the latest toxicity characteristic leaching procedure (TCLP) analysis as well as those for corrosivity, ignitability, and reactivity: laboratory: Pace Analytical, Asheville and date of analysis: 8/25/2009 (3/11/lQ) Passed corrosivity test: ® yes ❑ no. pH: 11.16 (lime stab) 6.54 dewatered s.u. (2 < pH < 12.5). Passed ignitability test: ® yes ❑ no. Flashpoint: >140 °F (> 140°F). Passed reactivity test: Z. yes ❑ no. HCN: ND mg/kg (<250) & HzS: ND mg/kg (<500). TCLP Parameter Limit OWL) Result NgQ TCLP Parameter Limit NA) Result (i)tg/L) Arsenic ' 5.0 ND Hexachlorobenzene 0.13 ND Barium 100.0 0.039 Hexacliloro-1,3-Butadiene 0.5 ND Benzene 0.5 ND Hexachloroethane 3.0 ND Cadmium I.0 ND Lead 5.0 ND Carbon Tetrachloride 0.5 ND Lindane 0.4 ND Chlordane 0.03 ND Mercury 0.2 ND Chlorobenzene 100.0 ND Methoxychlor 10.0 ND Chlorofonn 6.0 ND Methyl Ethyl Ketone 200.0 0,319 Chromium 5.0 ND Nitrobenzene 2.0 ND m-Cresol 200.0 Pentachlorophenol 100.0 ND o-Cresol 200.0 ND Pyridine 5.0 ND p-Cresol 200.0 Selenium 1.0 ND Cresol 200.0 0.218 Silver 5.0 ND 2,4-D 10.0 ND Tetrachloroethylene 0.7 ND 1,4-Dichlorobenzene 7.5 ND Toxaphene 0.5 ND 1,2-Dicltloroetliane 0.5 ND Trichloroethylene 0.5 ND 1,1-Dichloroethylene 0.7 ND 2,4,5-Trick loropliettol 400.0 ND 2,4-Dinitrotoluene 0.13 ND 2,4,6-Trichlorophenol 2.0 ND Endrin 0.02 ND 2,4,5-TP (Silvex) 1.0 ND Heptachlor and its Hydroxide 0.008 ND Vinyl Chloride 0.2 ND FORM: RSCA 070807 Page 4 of 8 Attachment Order 2 4. Metals Determination:. Complete one of the following tables (i.e., as applicable) to demonstrate that the residuals do not violate the ceiling concentrations for metals regulated under 15A NCAC 02T .1105. a. For Class A or Class B: Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the following metal parameters: Laboratory: Pace Analytical Asheville/Huntersville, NC and date of analysis: 8/24/2009 Parameter Ceiling Concentration 'Limits "(ClnssA &ClassB (nrg1kg) Monthly Average Concentration Limits (For Class A Only) (rng/kg) :. Result Ongft) Arsenic 75 41 6.6 Cadmium 85 39 0.6. Copper 4,300 1,500 104 Lead 840 300 6.0 Mercury 57 17 0.50 Molybdenum 75 n/a 1.0 Nickel 420 420 4.6 Selenium 100 100 5.8 Zinc 7,500, 2,800 324 b. For Stu;%Cce Disposal: Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the.following metal parameters: Laboratory: and date of analysis: Closest Distance to. Property Lines (neters) Arsenic (tng/k) Chromium (ing/kg) Nickel (rng/kg) > 0 but < 25 30 200 210 ? 25 but < 50 .. ' , 34 220 240 > 50 but < 75 39 260 270 >_ 75 but < 100 46 300 320 >_ 100 but < 125 53 360 390 > 125 but < 150 62 450 420 >_ 150 73 600 420 FORM: RSCA 070807 Page 5 of 8 Attachment Order 2 5. Nutrient/1llicronutrient Determination: Complete the following: a. Total solids: 57.2 %. b. Fill hi the following table with the results of the latest analyses (i.e., on a dry weight basis) for the following nutrient and micronutrient parameters: Iaboratory: Pace Analvtical Asheville/Huntersville, NC and date of analysis: „ 8/24/2009 , Parameter Result (niglkg, dq height) Aluminum 9,460 Ammonia -Nitrogen 286 Calcium 331,000 Magnesium • , ;.'-2,920.•... . Nitrate -Nitrite Nitrogen ND pH (Standard Unit) 12.4 Phosphorus 155 Potassium 3,690 - Sodium ND Total Kjeldalil Nitrogen 11,900 ..; c. Using the results listed in Item II.Sb, above, calculate the sodium adsorption ration (SAR): 0 . d. Specify the mineralization rate to be used in calculating the plant available nitrogen (PAN) of the residuals: 30 %. This rate is a ® default value or ❑ actually established. If the residuals are not generated from the treatment of municipal or domestic wastewater, explain or provide technical justification as to why the selected default value is appropriate to be applied to these residuals: Calculate the PAN for the residuals (i.e., on a dry weight basis) and list the results in the following table: Application Method First Year Five -Year PAN Maximum Adjusted PAN 0119/W (mgft) Surface 3,630 5,625 Injection/Incorporation 3,770 5,765 c. Are the residuals a registered fertilizer with the NC Department of Agriculture and Consumer Services: ❑ yes ® no. If yes, provide date of registration approval: the current registration number: and the fertilizer equivalent: %, %, and %. FORM: RSCA 070807 Page 6 of 8 Attachment Order 2 6. Other Pollutants Determination: Specify whether or not.there are any other pollutants of concern in the residuals and list the results of the latest analyses: No other pollutants of concern. 7. Pathogen Reduction Determination: Specify which alternative(s) will be used to meet the pathogen reduction requirements: a. For C1assA orEquivalent: ® A fecal coliforn density that is demonstrated to be less than 1,000 MPN per gram of total dry solids. OR ❑ A salmonella sp. density.that is demonstration to be less than 3 MPN per 4 grains of total dry solids. AND one of the following (except for residuals regulated under 40 CFR Part 257 that are to be distributed): ❑ Alternative 1 [40 CFR §503.32 (a)(3)] - Time/Temperature Compliance. ❑ Alternative 2 [40 CFR §503.32 (a)(4)] - Alkaline Treatment. ❑ Alternative 3 [40 CFR §503.32 (a)(5)] - Prior Testing for Enteric Virus/Viable Hehninth Ova, ❑ Alternative 4 [40 CFR §503.32 (a)(6)] - No Prior Testing for Enteric Virus/Viable Helmuith Ova. ® Alternative 5 [40 CFR §503.32 (a)(7)] - Process to Further Reduce Pathogens (PFRP). Specify one: ❑ composting, ® heat drying, . ❑ .heat treatment, ❑ pasteurization, ❑ thernnophilic aerobic digestion, ❑ beta ray irradiation, or ❑ gamma ray irradiation. ❑ Alternative 6 [40 CFR §503.32 (a)(8)] - PFRP-Equivalent Process. Explain: b. For Class B or Equivalent: ❑ Alternative 1 [40 CFR §503.32 (b)(2)] - Fecal Colifor . Density Demonstration. ❑ Alternative 2 [40 CFR §503.32 (b)(3)] - Process to Significantly Reduce Pathogens (PFRP). Specify one: ❑ aerobic digestion, ' ❑ air drying, "❑ anaerobic digestion, ❑ 'composting, or ❑ lime stabilization. ❑ Alternative 3 [40 CFR §503.32 (b)(4)] - PSRP-Equivalent Process. Explain: ❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution. c. For Surface Dis osal: ❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/OtherMaterial Cover. ❑ Select One of the Class'A'oir Equivalent Pathogeii Reduction Alternatives in Item E. 7a, above. ❑ Select One of the Class B or Equivalent Pathogen Reduction Alternatives in Item Il. 7b. above. ❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution. FORM RSCA 070807 ' :�'' Page 7 of 8 Attachment Order 2 8. Vector Attraction Reduction Determination: Specify ,which alterhative(s).will be used to meet the vector attraction reduction requirements: ❑ Alternative 1 [40 CFR §503.33 (b)(1)] - 38% Volatile Solids Reduction (Aerobic/Anaerobic Digestion). ❑ Alternative 2 140 CFR §503.33 (b)(2)] - 40-Day Bench Scale Test (Anaerobic Digestion). ❑ Alternative 3 [40 CFR §503.33 (b)(3)] - 30-Day Bench Scale Test (Aerobic Digestion). ❑ Alternative 4 [40 CFR §503.33 (b)(4)] - Specific Oxygen Uptake Rate Test (Aerobic Digestion). ❑ Alternative 5 [40 CFR §503.33 (b)(5)] -14-Day Aerobic Processes. ❑ Alternative 6 [40 CFR §503.33 (b)(6)] - Alkaline Stabilization.. i. ❑ Alternative 7 [40 CFR §503.33 (b)(7)] - Drying of Stabilized Residuals. ® Alternative 8 [40 CFR §503.33 (b)(8)] - Drying of Unstabilized Residuals. ❑ Alternative 9 [40 CFR §503.33 (b)(9)] - Injection. ❑ Alternative 10 [40 CFR §503.33 (b)(10)] - Incorporation. ❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(I1)] - Soil/Other Material Cover. ❑ Alternatives for Animal Processing Residuals Only: , Specify one: ❑ injection, ❑ incorporation, or ❑lime addition to raise pH to 10. ❑ Not Applicable - Non -Biological Residuals with NO Domestic Wastewater Contribution. FORM: RSCA 070807 Page 8 of 8 Attachment Order 2 Whittier Sanitary District WWTP Residuals -Source Certification Attachment..Order 2:, Attachment Order.2 a. Viclr ity, Map..See Whittier_. plan sheet C3 .. Attachment Order 2-b: Process Flow Narrative. See Residuals Management Plan Page 3. Attachment Order 2-c :Quantitative Justification for residuals production rate. See Design Calculations Page 1. Attachment Order 2-d:+Sampling Plan: Attached Attachment Order 2-inIaboratory Analytical "reports and Operational Data: Attached. State of North Carolina Department of Environment and Natural Resourees Division of Water Quality RESIDUALS SOURCE CERTIFICATION ATTACHMENT (FORM: RSCA 070807) (THIS FORM MAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL) The Division of Water Quality (Division) will not accept this attachment unless all the instructions are followed. Failure to submit all required items will lead to additional processing and review time. For snore info nation, visit our web site at: http://h2o.e7ir.state.nc.usllauhnain.htrnl INSTRUCTIONS TO THE APPLICANT: A. Attachment Form: ✓ Do not submit this attachment form for review without a corresponding residuals program application form (FORM: NDRLAP, FORM: DRS, or FORM: SDRS). ✓ Any changes to this attachment form will result in the application package being returned. ✓ For new residuals programs or renewed residuals programs, submit a separate attachment form for each residuals source -generating facility to be certified for this residuals program. ✓ For modified residuals programs in which any modification to the certified residuals -source generating facilities is proposed, submit a separate attachment form for o& those residuals source -generating facilities that are affected by the proposed modification. ✓ The attachment should be organized prior to submission in the following order (i.e., by facility): ♦ Attachment Order 2: Residuals Source Certification Attachment (FORM: RSCA). ➢ Attachment Order 2-a: Vicinity map. ➢ Attachment Order 2-b: Process flow diagram and/or narrative. ➢ Attachment Order 2-c: Quantitative justification for residuals production rate. ➢ Attachment Order 2-d: Sampling plan. ➢ Attachment Order 2-e: Laboratory analytical reports and operational data. B. Residuals Source -Generating Facility Information: ✓ Attach a vicinity map that shows the location of the facility and meets all of the criteria in the latest version of the document entitled "Guidance for the Preparation of Vicinity/Buffer Maps for North Carolina Residuals Permitting Programs." ✓ Attach a detailed narrative and/or process flow diagram that describes how the residuals are to be generated, treated, processed, and stored at the facility. ✓ Attach a quantitative justification for the value provided in Item I. 8. Ensure that the amount of residuals listed is the maximum amount expected to be generated by the facility for the life of the permit. In addition, ensure that this amount is equivalent to that which is actually to be land applied, distributed, and/or disposed, including any chemicals, amendments, or other additives that are added to the residuals during processing. C. Residuals Quality Information: ✓ Attach a detailed sampling plan for the residuals source -generating facility. Ensure that the plan identifies sampling points, sampling frequency, sample type, as well as the Division -certified laboratory to be used. In addition, ensure that the plan details how the facility and/or the residuals are monitored for any applicable pathogen reduction and vector attraction reduction requirements. Note that all sampling and monitoring must be completed on the residuals as they are to be land applied, distributed, and/or disposed. ✓ Attach reports for all laboratory analyses used to complete this attachment form. Attach documentation that the facility complies and/or the residuals comply with any applicable pathogen reduction and vector attraction reduction requirements. ✓ Item II. 3. does not have to be completed for facilities that are less than 0.5 MGD in design flow that treat 100% non -municipal, domestic wastewater only. RECEIVED / DENR / DWQ Aquifer Protection Section FORM: RSCA 070807 Page 1 of 8 JUL 19 2010 Attachment Order 2 State of North Carolina Department of Environment and Natural Resources Division of Water Quality RESIDUALS SOURCE CERTIFICATION ATTACHMENT (FORM: RSCA 070807) (THIS FORM MAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL) Applicant's name: Tuckaseigee Water and Sewer Authority Check all that apply: ❑ NEW RESIDUALS PROGRAM ❑ RENEWED RESIDUALS PROGRAM ® INCREASE ❑ DECREASE the maximum permitted annual dry tonnage for this residuals source - generating facility certified for this residuals program. Current: 250 Dry Tons/yr. and proposed: 659 Dry Tons/yr. ADD ❑ DELETE this residuals source -generating facility to/from those certified for this residuals program. ❑ OTHER Explain: I. RESIDUALS SOURCE -GENERATING FACILITY INFORMATION (See Instruction B): 1. Name of facility: TWSA Wastewater Treatment Plant No. 1 2. Facility permit holder: Tuckaseigee Water and Sewer Authority Facility permit holder is (check one): ❑ federal, ❑ state, E local government, or ❑ private. Facility permit number: NPDES No. NCO039578 Facility permit issued by (check one): ® Div. of Water Quality, ❑ Div. of Environmental Health, or ❑ other (explain: 3. If the facility permit is not issued by the Div. of Water Quality, complete the following: a. Facility contact person and title: Facility complete mailing address: City: Telephone number: ( ) E-mail address: b. Facility complete location address: _ City: Latitude: 4. County where facility is located: Jackson County State: Zip: Facsimile number: ( ) State: and longitude: Zip: 5. Purpose of the facility (check one): ® treatment of municipal wastewater, ❑ treatment of 100% domestic wastewater, ❑ treatment of potable water, ❑ treatment of 100% industrial wastewater, ❑ treatment of industrial wastewater mixed with domestic wastewater, or (approximate percentages: % industrial and % domestic) ❑ other (explain: FORM: RSCA 070807 Page 2 of 8 Attachment Order 2 6. Does the facility have an approved pretreatment program: ❑ yes ® no 7. Facility permitted/design flow: _3.5 MGD and facility average daily flow: _0_9 MGD. 8. Average amount of residuals being generated at this facility _158.77 dry tons per year. 9. Specify the following regarding treatment and storage volumes available at the facility: Type and volume of residuals treatment: See Page 3 of the attached Residuals Management Plan. Type and volume of residuals storage (i.e., outside of residuals treatment units): Dried Solids will be stored in a 94 CY storage silo which provides approximately 36 1 days of storage at the permitted design flow for the facility. H. RESIDUALS QUALITY INFORMMATION (See Instruction C.): 1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or ❑ 40 CFR Part 257. 2. Specify if residuals are intended for (check one): ® Land Application/Distribution (Class A or Equivalent). Complete all items EXCEPT Items II.4b., 7b., and 7c. ❑ Land Application (Class B or Equivalent). Complete all items EXCEPT Items II. 4b., 7a., and 7c. ❑ Surface Disposal. Complete all items EXCEPT Items II. 4a., 5., 7a., 7b., and 8. ***FORM: RSCA CONTINUES ON NEXT PAGE*** FORM: RSCA 070807 Page 3 of 8 Attachment Order 2 3. Hazardous Waste Determination: Complete the following to demonstrate that the residuals are non- hazardous under RCRA: a. Are the residuals are listed in 40 CFR §261.31-§261.33: ❑ yes ® no. If yes, list the number(s): b. Specify whether or not the residuals exhibit any of the characteristics defined by 40 CFR §261.21- §261.24: ❑ yes ® no. Fill in the following tables with the results of the latest toxicity characteristic leaching procedure (TCLP) analysis as well as those for corrosivity, ignitability, and reactivity: laboratory: Pace Analytical, Asheville and date of analysis: 8/25/2009 (3/11/10) Passed corrosivity test: ® yes ❑ no. pH: 11 16 (line stab) 6.54 dewatered s.u. (2 < pH < 12.5). Passed ignitability test: ® yes ❑ no. Flashpoint: _>140_ OF (> 1400F). Passed reactivity test: ® yes ❑ no. HCN: ND_ mg/kg (<250) & HzS: ND_ mg/kg (<500). TCLP Parameter LimitTRes/ul)t (mg/L)MgL TCLP Parameter Limit (nig/L) Result (nzg/L) Arsenic 5.0 ND Hexachlorobenzene 0.13 ND Barium 100.0 0.039 Hexachloro-1,3-Butadiene 0.5 ND Benzene 0.5 ND Hexachloroethane 3.0 ND Cadmium 1.0 ND Lead 5.0 ND Carbon Tetrachloride 0.5 ND Lindane 0.4 ND Chlordane 0.03 ND Mercury 0.2 ND Chlorobenzene 100.0 ND Methoxychlor 10.0 ND Chloroform 6.0 ND Methyl Ethyl Ketone 200.0 0.319 Chromium 5.0 ND Nitrobenzene 2.0 ND m-Cresol 200.0 Pentachlorophenol 100.0 ND o-Cresol 200.0 ND Pyridine 5.0 ND p-Cresol 200.0 Selenium 1.0 ND Cresol 200.0 0.218 Silver 5.0 ND 2,4-D 10.0 ND Tetrachloroethylene 0.7 ND 1,4-Dichlorobenzene 7.5 ND Toxaphene 0.5 ND 1,2-Dichloroethane 0.5 ND Trichloroethylene 0.5 ND 1, 1 -Dichloroethylene 0.7 ND 2,4,5-Trichlorophenol 400.0 ND 2,4-Dinitrotoluene 0.13 ND 2,4,6-Trichlorophenol 2.0 ND Endrin 0.02 ND 2,4,5-TP (Silvex) 1.0 ND Heptachlor and its Hydroxide 0.008 ND Vin�Chlo�ride 0.2 ND FORM: RSCA 070807 Page 4 of 8 Attachment Order 2 4. Metals Determination: Complete one of the following tables (i.e., as applicable) to demonstrate that the residuals do not violate the ceiling concentrations for metals regulated under 15A NCAC 02T .1105. a. For Class A or Class B: Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the following metal parameters: Laboratory: Pace Analytical Asheville/Huntersville. NC and date of analysis: _8/24/2009 Parameter Ceiling Concentration Limits (ClassA & ClassB) (mg/kg) Monthly Average Concentration Limits (For Class A Only) (mg/kg) Result (nig/kg) Arsenic 75 41 6.6 Cadmium 85 39 0.6. Copper 4,300 1,500 104 Lead 840 300 6.0 Mercury 57 17 0.50 Molybdenum 75 n/a 1.0 Nickel 420 420 4.6 Selenium 100 100 5.8 Zinc 7,500 2,800 324 b. For Surface Disposal: Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the following metal parameters: Laboratory: N/A and date of analysis: Closest Distance to Property Lines (meters) Arsenic Onglkg) Chromium (mg/Icg) Nickel (nig/kg) > 0 but < 25 30 200 210 > 25 but < 50 34 220 240 > 50 but < 75 39 260 270 > 75 but < 100 46 300 320 > 100 but < 125 53 360 390 > 125 but < 150 62 450 420 > 150 73 600 420 FORM: RSCA 070807 Page 5 of 8 Attachment Order 2 5. Nutrient/Micronutrient Determination: Complete the following: a. Total solids: 57.2 %. b. Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the following nutrient and micronutrient parameters: laboratory: Pace Analytical Asheville/Huntersville. NC and date of analysis: 8/24/2009 Parameter Result (mg/kg, dry weight) Aluminum 9,460 Ammonia -Nitrogen 286 Calcium 331,000 Magnesium 2,920 Nitrate -Nitrite Nitrogen ND pH (Standard Unit) 12.4 Phosphorus 155 Potassium 3,690 Sodium ND Total Kjeldahl Nitrogen 11,900 c. Using the results listed in Item II. 5b. above, calculate the sodium adsorption ration (SAR): _0_ . d. Specify the mineralization rate to be used in calculating the plant available nitrogen (PAN) of the residuals: 30 %. This rate is a JZJ default value or L_J actually establisnecl. If the residuals are not generated from the treatment of municipal or domestic wastewater, explain or provide technical justification as to why the selected default value is appropriate to be applied to these residuals: Calculate the PAN for the residuals (i.e., on a dry weight basis) and list the results in the following table: Application Method First Year Five -Year PAN Maximum Adjusted PAN (ing/kg) (mg/kg) Surface 3,630 5,625 Injection/Incorporation 3,770 5,765 e. Are the residuals a registered fertilizer with the NC Department of Agriculture and Consumer Services: ❑ yes ® no. If yes, provide date of registration approval: the current registration number: and the fertilizer equivalent: %, %, and %. FORM: RSCA 070807 Page 6 of 8 Attachment Order 2 6. Other Pollutants Determination: Specify whether or not there are any other pollutants of concern in the residuals and list the results of the latest analyses: No other pollutants of concern. 7. Pathogen Reduction Determination: Specify which alternative(s) will be used to meet the pathogen reduction requirements: a. For Class A or Equivalent: ® A fecal coliform density that is demonstrated to be less than 1,000 MPN per gram of total dry solids. OR ❑ A salmonella sp. density that is demonstration to be less than 3 MPN per 4 grams of total dry solids. AND one of the following (except for residuals regulated under 40 CFR Part 257 that are to be distributed): ❑ Alternative 1 [40 CFR §503.32 (a)(3)] - Time/Temperature Compliance. ❑ Alternative 2 [40 CFR §503.32 (a)(4)] - Alkaline Treatment. ❑ Alternative 3 [40 CFR §503.32 (a)(5)] - Prior Testing for Enteric Virus/Viable Helminth Ova. ❑ Alternative 4 [40 CFR §503.32 (a)(6)] - No Prior Testing for Enteric VirasNiable Helminth Ova. ® Alternative 5 [40 CFR §503.32 (a)(7)] - Process to Further Reduce Pathogens (PFRP). Specify one: ❑ composting, ® heat drying, ❑ heat treatment, ❑ pasteurization, ❑ thermophilic aerobic digestion, ❑ beta ray irradiation, or ❑ gamma ray irradiation. ❑ Alternative 6 [40 CFR §503.32 (a)(8)] - PFRP-Equivalent Process. Explain: b. For Class B or Equivalent: ❑ Alternative 1 [40 CFR §503.32 (b)(2)] - Fecal Coliform Density Demonstration. ❑ Alternative 2 [40 CFR §503.32 (b)(3)] - Process to Significantly Reduce Pathogens (PFRP). Specify one: ❑ aerobic digestion, ❑ air drying, ❑ anaerobic digestion, ❑ composting, or ❑ lime stabilization. ❑ Alternative 3 [40 CFR §503.32 (b)(4)] - PSRP-Equivalent Process. Explain: ❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution. c. For Surface Disposal: ❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/Other Material Cover. ❑ Select One of the Class A or Equivalent Pathogen Reduction Alternatives in Item II. 7a. above. ❑ Select One of the Class B or Equivalent Pathogen Reduction Alternatives in Item II. 7b. above. ❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution. FORM: RSCA 070807 Page 7 of 8 Attachment Order 2 8. Vector Attraction Reduction Determination: Specify which alternative(s) will be used to meet the vector attraction reduction requirements: ❑ Alternative 1 [40 CFR §503.33 (b)(1)] - 38% Volatile Solids Reduction (Aerobic/Anaerobic Digestion). ❑ Alternative 2 [40 CFR §503.33 (b)(2)] - 40-Day Bench Scale Test (Anaerobic Digestion). ❑ Alternative 3 [40 CFR §503.33 (b)(3)] - 30-Day Bench Scale Test (Aerobic Digestion). ❑ Alternative 4 [40 CFR §503.33 (b)(4)] - Specific Oxygen Uptake Rate Test (Aerobic Digestion). ❑ Alternative 5 [40 CFR §503.33 (b)(5)] - 14-Day Aerobic Processes. ❑ Alternative 6 [40 CFR §503.33 (b)(6)] - Alkaline Stabilization. ❑ Alternative 7 [40 CFR §503.33 (b)(7)] - Drying of Stabilized Residuals. ® Alternative 8 [40 CFR §503.33 (b)(8)] - Drying of Unstabilized Residuals. ❑ Alternative 9 [40 CFR §503.33 (b)(9)] - Injection. ❑ Alternative 10 [40 CFR §503.33 (b)(10)] - Incorporation. ❑ Altemative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/Other Material Cover. ❑ Alternatives for Animal Processing Residuals Only: Specify one: ❑ injection, ❑ incorporation, or ❑ lime addition to raise pH to 10. ❑ Not Applicable - Non -Biological Residuals with NO Domestic Wastewater Contribution. FORM: RSCA 070807 Page 8 of 8 Attachment Order 2 TWSA Plant No. 1 Residuals Source Certification Attachment Order 2: Attachment Order 2-a: Vicinity Map. See plan sheet C3 Attachment Order 2-b: Process Flow Narrative. See Residuals Management Plan Page 3. Attachment Order 2-c: Quantitative Justification for residuals production rate. See Design Calculations Page 1. Attachment Order 2-d: Sampling Plan: Attached Attachment Order 2-e: Laboratory Analytical reports and Operational Data: Attached. Tuckaseigee Water and Sewer Authority Residuals Distribution Permit- Sampling Plan Residuals will be sampled after the dryer process has completed at the pneumatic conveyor or storage silo. Toxicity Characteristics Leaching Procedure Analysis shall be performed annually. For Product distribution up to 319 Dry. Tons per year residuals will be tested once per year for aluminum, magnesium, phosphorus, ammonia -Nitrogen, Mercury, Potassium, Arsenic, Molybdenum, Selenium, Cadmium, Nickel, Sodium, Calcium, Nitrate -Nitrate Nitrogen, Total Kjeldahl Nitrogen, Copper, pH, Total Solids, Lead, Plant Available Nitrogen and Zinc. For product distribution from 319 dry tons per year to 659 dry tons the above shall be sampled quarterly. Pathogen Reduction shall be verified by Total Solids > 90% dry solids or maintenance of 158 degrees F for at least 30 minutes. Vector Attraction shall be verified by total solids > 90% dry solids. All samples will be completed by Tuckaseigee Water and Sewer Authority Certification No. 160 or Pace Analytical Services Inc. - Asheville Certification No. 40 DESIGN CALCULATIONS WASTEWATER TREATMENT PLANT NO. 1 IMPROVEMENTS SLUDGE MANAGEMENT TUCKASEIGEE WATER AND SEWER AUTHORITY JACKSON COUNTY, NORTH CAROLINA PREPARED BY: DAVID L. HONEYCUTT, P.E. REVIEWED BY: HARRY B. BUCKNER, P.E. McGfll A S S O C I A T E S Engineering • Planning • Finance Post Office Box 2259 Asheville, North Carolina 28802 JULY 2010 05734 i SEAL 2254; `fAEetetet►d`�` -7 ,01 ,1oI a TABLE OF CONTENTS I. SLUDGE HOLDING.....................................................................................1 II. SLUDGE HANDLING SYSTEM FEED PUMP .......................................... 4 III. SOLIDS HANDLING FACILITY................................................................. 5 IV. PLANT AVAILABLE NITROGEN.............................................................. 7 i Io SLUDGE HOLDING Determine sludge wasting rate Q = V/ SRT (Ref. Wastewater Engineering, Metcalf and Eddy 4t' edition, pg 693) V = 2,235,000 gal. Per WWTP No. 1 Design Calculations SRT =13.1 days Per WWTP No. 1 Design Calculations Q = 2,235,000 gal. / 13.1 days=170,611 GPD at 4,500 mg/l Lbs solids wasted = 0.170611 mgd * 4,500 mg/l * 8.34 = 6403 lbs/day Assuming 75% volatile solids and 75% reduction of volatile solids digestion Solids to disposal = 6403 — 6403*0.75 *0.75 = 2801 lbs/day 2801 lbs/day at 3.5 mgd = 0.80 lbs/day Based on historic data the plant has produced 0.95 lbs/1000 gallons. In addition the plant receives solids from the Cashiers WWTP with a permitted flow of 0.2 mgd and the Whittier WWTP with a permitted flow of 0.1 ingd. At 0.95 lbs/1000 gallons *3.8 ingd = 3,610 lbs/day 3,610 * 365 days/year = 659 dry tons per year Size Sludge Holding for sludge production at Plant No. 1. At 0.95 lbs/1000 gallons *3.5 mgd = 3,325 lbs/day 30 days of solids storage required per 15A NCAC 02H. Assume 2 %. solids concentration (ref. Metcalf and Eddy, Wastewater Engineering 3rd Edition, pg 774) 3,325 lbs solids / day * 1/ (62.4 lbs / cubic foot water * 1.015 (SG of 2% sludge) x 0.02 (solids content) = 2,625 cubic feet per day=19,634 GPD 19,634 GPD * 30 days = 589,025 gal sludge produced in 30 days Existing Sludge Holding tank basin is 50' - 6" 0 x 19' W.L. Volume = 50.52 * pi/4 * 19' * 7.48 gallons/CF = 284,660 gallons Page 1 Existing Flow Equalization Basin is 53' - 4" x 20'-6" W.L. Volume = 53.332 * pi/4*20.5*7.48 gallons/CF = 342,522 gallons Total Sludge Storage Volume = 627,182 gallons Greater than 589,025 gal therefore, 30 days storage requirement met. Proposed Sludge Holding Tank Air Requirements Calculate the air required for mixing and to prevent anaerobic conditions in the proposed sludge holding tank. Per Metcalf and Eddy Wastewater En ineering 3'd edition, pg 837 air requirements for sludge holding is 20-40 SCFM per 1000 CF of sludge holding volume. Therefore use 30 SCFM per 1000 CF. Air required for Proposed Sludge Holding Tank (existing Flow Equalization): 342,522 gallons / 7.48 gallons/CF *30 SCFM/1000 CF =1374 CFM, Use 1375 CFM Determine discharge pressure required. Discharge pressure = head of water above diffusers + piping friction head + silencer/filter losses + diffuser headloss Water above diffusers = 20.5 ft Silencer/Filter Head = 2.25 ft Diffuser Headloss = 1 ft Air header is a total of 100' long. Per Duct Resistance Chart 0.35" of headloss per 100 ft for 1375 SCFM in 12" piping. Air header friction loss = 0.35 in (0.03 ft) Discharge Pressure = 20.5' + 2.25' + 0.25' + 0.03' = 23.03' (9.97 psi) Specify duplex blowers, each 1375 SCFM cr 10.5 psi Use 24" coarse bubble diffusers loaded at 16 SCFM each requires 86 diffusers. Air required for Existing Sludge Holding Tank 284,660 gallons / 7.48 gallons/CF *30 SCFM/1000 CF=1141.7 CFM, Use 1145 CFM Determine discharge pressure required. Discharge pressure = head of water above diffusers + piping friction head + silencer/filter losses + diffuser headloss Page 2 Water above diffusers = 19.5 ft Silencer/Filter Head = 2.25 ft Diffuser Headloss =1 ft Air header is a total of 100' long. Per Duct Resistance Chart 0.2" of headloss per 100 ft for 1145 SCFM in 12" piping. Air header friction loss = 0.2 in (0.016 ft) Discharge Pressure =19.5' + 2.25' + 0.25' + 0.016' = 22.02' (9.53 psi) Specify duplex blowers, each 1145 SCFM tt 10 psi Use 24" coarse bubble diffusers loaded at 16 SCFM each requires 72 diffusers. Both basins are existing structures and therefore buoyancy calculations are not necessary. Page 3 U. SLUDGE HANDLING SYSTEM FEED PUMP Size progressive cavity pump to feed belt press at 50-100 gpm. High Point at ceiling in sludge handling facility = 2061.6 Assume pumping from bottom EL. of Proposed Sludge Holding Tank = 2000.0 Static Head = 2061.6-2000.0 = 61.6' The friction loss in the 4-inch force main can be represented as: Head iri,.tion = 10.57 Q1.85 L C1.85 D4.87 For L in feet, Q in GPM, and D in inches For 100 GPM, Head f;,,t,on = 10.57 * 1001.85 550 1201.85 44.87 Head fii�tton = 4.85 ft Total Dynamic Head = 61.6 + 4.85 = 66.5' Size pump for 100 gpm at 67' TDH. Page 4 III. S®LIDS HANDLING FACILITY Belt Press Belt press is proposed to be relocated from existing solids handling process Existing Press has a 1 meter effective width. Verify capacity is adequate for 3.5 mgd design flow with flow from Cashiers and Whittier. Note that sludge from TWSA Plant No. 2 is also hauled to this facility. The 3.5 mgd design flow for Plant No. 1 includes all flow from Plant No. 2 to be pumped to Plant No. 1 in the future. Per sludge calculations 3,610 dry lbs/day of sludge at 26/o solids will be produced. Belt Press Hydraulic capacity is 60-70 gpm assume 65 gpm. 65 gpm *8.34 lbs/gallon * 0.02 lbs solids*60 min/hr = 650.5 lbs/hr 3610 lbs/day/ 6501bs/hr = 5.55 hrs/day To press only 5 days a week would require the press to run 7.77 hrs/day. Therefore Belt Filter Press capacity is adequate at the design flow. Solids Dryer Proposed utilize indirectly heated dryer to produce Class A biosolids. Estimate volume from belt press for dewatered sludge at 16% solids. Assume a density of dewatered sludge of 62.4 lbs/CF * 1.07 = 67 lbs/CF (1.07 is Specific gravity per Metcalf and Eddy) 65 gpm * 0,02% solids * 8.34 lbs/gallon * 60 min. = 650.5 lbs dry solids/hr 650.5 lbs dry solids/hr/0.16 = 4,065.75 lbs wet 16 % solids/hr Water weight = 4065.75-650.5=3,415.25 lbs water/hr Volume = 4,065.75/67 lbs/CF = 60.68 CF/hr Proposed storage hopper between belt press and solids dryer is 50 CY 50 CY / (60.68 CF/27) = 22.25 hrs belt press run time to fill hopper. Page 5 Dryer Capacity is 9.5 CY per batch EPA 40 CFR 503 regulations require pathogen reduction and vector attraction reduction for class A biosolids. 1. Pathogen Reduction 176° F and 90% solids Or 158°F for 30 minutes (Pasteurization) Proposed dryer will produce of 90% solids and provide over 158° F for greater than 30 minutes. 2. Vector Attraction Reduction Dry un-stabilized solids to 90% solids. Determine therms natural gas required for drying. Calculate per wet ton at 16% solids 20001bs * 0.16% = 3201bs dry solids/wet ton 320 lbs dry solids at 90% solids = 365 lbs (451bs water remaining) 2000 lbs wet sludge — 365 lbs =1644 lbs water evaporated per wet ton. 16441bs water evaporated/wet ton * 1600 BTUs/lb = 2,630,400 btu/wet ton 2,630,400 btu/wet ton / 1,000,000 btu/ MCF Natural Gas = 2.63 MCF/wet ton Natural Gas required at design flow 3610 dry lbs/day / 0.16 = 22,562.5 wet lbs/day =11.28 wet tons/day 11.28 wet tons/day * 2.63 MCF/wet ton = 29.67 MCF/day at 3.8 imgd Check Proposed Silo Storage Volume Silo Inside Diameter =12 ft noire. Silo Height = 21 ft Silo Cone Height = 3.5 ft Silo Cone Lower Inside Diameter = 4 ft Volume Silo = pi/4* 12 f 2 (21 ft) = 2,375 CF Volume Silo Cone = pi/4 (1/2(12+4))2(3.25) = 163 CF Total Volume Silo = 25538 CF Unit Weight Sludge = 40 to 50 lb/CF use 50 lb/CF Total Dry Sludge Capacity = 2,538 CF * 50 lb/CF = 63.45 tons 63.45 tons/ 3610 lbs/day = 35.2 days storage at Design Flow. Page 6 IV. PLANT AVAILABLE NITROGEN Determine PAN for TWSA Biosolids (first year and 5-year max.) First Year PAN = AN(Kvol) + NN + ONo(Ko) Ref. EPA Design Manual 625/R-95/001 September 1995 pg 77. Assume no denitrification losses AN = Aininonia-nitrogen (lb/ton) = 286 mg/kg(sainple data)*0.002 lb/ton / mg/kg = 0.5721b/ton NN = Nitrate -nitrogen (lb/ton) = 0 mg/kg * 0.002 lb/ton / mg/kg = 0 lb/ton ONo = Organic Nitrogen during year of application (lb/ton) = TKN — AN — NN = 11,900-286-0= 11,614 mg/kg * 0.002 lb/ton / mg/kg = 23.23 lb/ton Ko = mineralization rate of ON during year of application rate = 0.30 per Table 7-7 EPA Design Manual 625/K-95/001 September 1995 Kv01 = Volatilization losses of AN Typically 0.5 for surface application per Table 7-8 EPA Design Manual 625/R-95/001 September 1995 Kv01= Volatilization losses of AN Typically 1.0 for incorporation per Table 7-8 EPA Design Manual 625/R-95/001 September 1995 Surface First Year PAN = 0.572 * 0.5 + 0 + 23.23 * 0.30 = 7.26 lb/ton 7.26 lb/ton / 0.0021bs/ton / mg/kg = 3630 mg/kg Incorporated First Year PAN = 0.572 * 1 + 0 + 23.23 * 0.30 = 7.54 lb/ton 7.54 lb/ton / 0.0021bs/ton / mg/kg = 3770 mg/kg Determine 5 year max PAN 5 year max. PAN = First Year PAN + PAN fiom previous applications Per Table 7-7 EPA Design Manual 625/R-95/001 September 1995 the following mineralization rates will be used Years After Application Kmin for Aerobically Digested Sludge 1-2 0.15 2-3 0.08 3-4 0.04 5 Year Max. PAN = First Year PAN + ON12 (0.15) + ON23(0.08) + ON34(0.04) Page 7 5 Year Max. PAN= Year 1 PAN + Year 2 PAN + Year 3 PAN + Year 4 PAN Year 1 Pan = 7.26 lb/ton Year 2 PAN = [(23.23-Year 1 PAN)*0.15) = 2.40 lb/ton Year 3 PAN = [23.23-Year 1 PAN — Year 2 PAN] *(0.08) =1.09 lb/ton Year 4 PAN = [23.23 — Year 1 PAN — Year 2 PAN — Year 3 PAN] * (0.04)=0.50 lb/ton 5 Year Max. PAN=11.251b/ton 11.25 lb/ton / 0.002 lbs/ton / mg/kg = 5625 mg/kg Page 8 TUCKASEIGEE WATER AND SEWER AUTHORITY RESIDUALS MANAGEMENT PLAN FEBRUARY 2009 The Tuckaseigee Water and Sewer Authority is proposing to construct facilities for heat drying of municipal wastewater sludge from their wastewater treatment plant. The EPA 503 regulations allow for pathogen reduction by subjecting the material to high temperatures for a certain length of time. After the liquid sludge is dewatered to approximately 16% solids by a belt filter press, the dewatered sludge will be conveyed to a gas -fired dryer for final heat and drying treatment. One of the following two (2) methods of compliance with EPA regulations for pathogen reduction will be performed to achieve a Class A biosolids product. PATHOGEN REDUCTION METHODS 1. Heat Drying The dewatered sludge will be dried by indirect contact with hot gases to reduce the moisture content to 10% or lower (i.e., at least 90% dry solids). The temperature of the sludge will be raised to at least 80 degrees C (176 degrees F) during this process. 2. Pasteurization The temperature of the dewatered sludge in the dryer will be maintained at 70 degrees C (158 degrees F) or higher for at least thirty minutes to achieve pasteurization of pathogens. EPA regulations also stipulate that vector attraction reduction methods be utilized to achieve a Class A biosolids. The vector attraction reduction requirements will be met by one of the following two methods. VECTOR ATTRACTION REDUCTION METHODS 1. Thermal drying of unstabilized biosolids to at least 90% dry solids. Page 1 2. Thermal drying of stabilized biosolids to at least 75% dry solids. After the heat drying process is completed, the final Class A biosolids product will be conveyed to either a truck or silo storage. The product will be sold or given away to local farmers, nurserymen and landowners for use as a soil amendment. Page 2 B. BIOSOLIDS PROCESSING FACILITIE Waste activated sludge will be pumped at 400 gpm from the sequencing batch reactor basins to one of two (2) aerated sludge holding tanks. The total sludge holding tank volume is 627,182 gallons which provides 30 days storage at the design flow at 2% solids. The thickened sludge will then be pumped at 50-100 gpm to a belt filter press to be dewatered to approximately 16% dry solids. Per design calculations the belt press will be required to run an average of 5.3 hrs per day at 65 gpm feed rate at the plant design flow of 3.5 mgd. Dewatered sludge from the belt filter press will be discharged to a 50 cubic yard storage hopper. The dewatered sludge will be conveyed from the storage hopper to a gas -fired dryer for final heat and drying treatment. The dryer has a capacity of 9.5 cubic yards per load and therefore the storage hopper can store up to 5 loads. The dryer will utilize either liquid petroleum or natural gas to heat oil, and will heat and dry the sludge by through indirect contact. Sludge will be dried to 90% solids and then conveyed to an 86 cubic foot storage hopper. A blower system will be used to blow the dried sludge from the storage hopper through a 4 inch ductile iron pipe to the sludge storage silo. The sludge storage silo provides 94 cubic yards of storage capacity or 36.1 days at design flow. The dried sludge will be distributed from the silo to the final users. It is expected that the final product will be distributed in bulk. Page 3 C. Heat dried biosolids from the Tuckaseigee Water and Sewer Authority Solids Handling Facility will be attractive to several markets including fanning businesses and the private sector. It is anticipated that both commercial and private fanners, landscape professionals, golf courses and private landowners in Jackson County will be interested in obtaining the Class A biosolids material for utilization as a soil amendment. Page 4 Page 5 USE OF HEAT DRYED WASTEWATER DI®SOLIDS AS A S®II, AMENDMENT A Guide for the Consumer Heat Dryed Biosolids Tuckaseigee Water and Sewer Authority Jackson County, North Carolina For fiwther technical guidance contact your County Agricultural Extension Service Agent. The Tuckaseigee Water and Sewer Authority may be contacted at the address below: Tuckaseigee Water and Sewer Authority 1246 West Main Street Sylva, North Carolina 28779 Page 6 THE HEAT DRYING PROCESS The EPA 503 regulations allow for pathogen reduction by subjecting the material to high temperatures for a certain length of time. After the liquid sludge is dewatered to approximately 16% solids by a belt filter press, the dewatered sludge will be conveyed to a gas -fired dryer for final heat and drying treatment. One of the following two (2) methods of compliance with EPA regulations for pathogen reduction will be performed to achieve a Class A biosolids product. PATHOGEN REDUCTION METHODS 1. Heat Dryin The dewatered sludge will be dried by indirect contact with hot gases to reduce the moisture content to 10% or lower (i.e., at least 90% dry solids). The temperature of the sludge will be raised to at least 80 degrees C (176 degrees F) during this process. 2. Pasteurization The temperature of the dewatered sludge in the dryer will be maintained at 70 degrees C (158 degrees F) or higher for at least thirty minutes to achieve pasteurization of pathogens. EPA regulations also stipulate that vector attraction reduction methods be utilized to achieve a Class A biosolids. The vector attraction reduction requirements will be met by one of the following two methods. VECTOR ATTRACTION REDUCTION METHODS 1. Thermal drying of unstabilized biosolids to at least 90% dry solids. 2. Thermal drying of stabilized biosolids to at least 75% dry solids. After the heat drying process is completed, the final Class A biosolids product will be conveyed to either a truck or a covered storage area. The product will be sold or given away to local farmers, nurserymen and landowners for use as a soil amendment. Page 7 The heat drying method of producing biosolids is approved by the EPA as an effective method of sludge stabilization and pathogen reduction and results in an environmentally safe product with multiple beneficial uses. GENERAL, USES, PROPERTIES, AND PRECAUTIONS Heat dryed biosolids can be utilized advantageously by the local, large scale fanner as a soil amendment or to supplement fill material. It can also be used by individuals wishing to enhance their lawns and gardens or any other area that may need a soil amendment. Heat dryed biosolids should improve the physical properties of soil in the following ways: • hnproved Permeability - Helps snake clay or other heavy soils more friable and loose, reducing compaction. Improved aeration - Looser soil encourages root growth. • Supplement other fill material Heat dryed wastewater biosolids are a product of municipal sewage. Heat dryed biosolids should be free of dangerous pathogens and toxic substances, but it should be treated with respect. Contact with children and pets should be minimized and direct ingestion of heat dryed biosolids should be avoided. Also as a precaution, prolonged contact with the heat dryed biosolids should be avoided. Heat dryed biosolids should not be applied to any site that is flooded, frozen or snow covered and adequate procedures shall be provided to prevent surface runoff from carrying any disposed or stored residuals into any surface waters. Residuals also cannot be placed any closer than ten (10) feet from any public or private water supply source (including wells) and any stream, lake, river, or natural drainage way. Application of these residuals is prohibited except as in accordance with the instructions on this information sheet. Page 8 January 26, 2010 DENR/DWQ/Water Quality Section Non -Discharge Compliance Unit 1617 Mail Service Center Raleigh NC 27699-1617 Attn: Non -Discharge Compliance Unit, Enclosed is the Annual Residuals Report for the Tuckaseigee Water and Sewer Lime Stabilization facility (permit 4WQ0005763) for the period of January 1, 2009 - December 31, 2009. Should you have any questions or if I can provide you any additional information, please don't hesitate to contact me. Sincerely, Stan Bryson Wastewater Plant Operations Superintendent Tuckaseigee Water & Sewer Authority Enc. TABLE OF CONTENTS (1) REPORTING REQUIREMENTS/PERTINENT INFORMATION (2) CERTIFICATION (a) 2009 distribution and marketing summary PartA & B (b) Annual Residuals Sampling Summary Form (c) 2009 Residuals Analysis. Lab Sheets (d) TCLP analysis (e) Annual Pathogen and Vector Attraction Reduction Forms (fl Pathogen & Vector Attraction Reduction Lab Sheets/Records (g) 2009 sludge production data ANNUAL SEWAGE SLUDGE REPORT OF �l 'I'iTCKASEIGEE WATER AND SEWER AUTHORITY PLANT # fl-NPHiES # NC0039578 (WQ0005763) for the period of 1 00) January 1, 2009-December 31, 2009 as required by 40 CFR, PART 503 STANDARDS FOR THE USE OR DISPOSAL OF SEWAGE SLUDGE a L L 1 1 1 . )1 1l'►MKy Facilities responsible for reporting annually are described in the regulations as: 1. Publicly Owned Treatment Works (POTW) with an average design influent flow rate equal to or greater than 1.0 MGD. 2. POTW's serving a population of 10,000 or more. 3. Class I (facilities with an approved pretreatment program) sludge management facilities The Tuckaseigee Water and Sewer Authority Wastewater Treatment Plant is a 1.5 MGD design facility. The facility also treats the sludge from two additional plants owned by the authority. Pertinent information includes: facility name: Tuckaseigee Water & Sewer Authority Plant # 1 NPDES # NC0039578 correspondence address: 1246 West Main St Sylva NC 28779 physical address: 1871 North River Rd Sylva NC 28779 facility operator: Stan Bryson Wastewater Plant Operations Superintendent ph. 828-586-9318 e-mail: sbrysontwsa@verizon.net I - - CERTIFICATION REQUIREMENTS PART I - POLLUTANT CONCENTRATIONS Ceiling Concentrations mg/kg Parameter Sample. Analysis value Maximum Permitted value Arsenic 6.7 75 Cadmium 0.42 85 Chromium, 8.8 300 Copper 86 4,300 Lead 5.0 840 Mercury 0.313 57 Molybdenum 0.5 75 Nickel 2.6 420 Selenium 6.2 100 Zinc 268 7,500 PART II - PATHOGEN REDUCTION (40 CFR 503.32) X Class A - Class B PART III - VECTOR ATTRACTION (40 CFR 503.33) option Option 2 Option 3 Option 5 X Option 6 Option 7 Option 4 Option 8 -CERTIFICATION " I certify under penalty of law, that the Class A pathogen requirements in 40 CFR, Part 503. 32 have been met and the vector attraction reduction requirement in 40 CFR, Part _ [50133(b)(6}] has been met. I am aware that there are significant penalties for false certification including fine and imprisonment." i Signeo this 5th day of . _ February, 2009 Stan Bryson, Wastewater Superintendent.. Nil t Appendix (a) 2009 a . Distribution and Marketing Summary (Part A) MM '% ANNUAL DISTRIBUTION AND .MARI STING/ SURFAd DISPOSAL CERTIFICATION AND SUMMARY;FORM PERMIT #: L!0_ DD T_rl(a 3 FACILITY NAME: PHONE: gam_ eJ g& _ ?.318 COUNTY: ��c�C�i o F-1 . OPERATOR: FACILITY TYPE lease check one): e ❑ Surface Disposal`(coniplete;Part A- (Source(s) and •"Resi ual In" Volume only) and Part C) II Distribution and Marketing (complete Parts A, B, and C) Was the facility in operation during the past calendar. year?.. No.If No skip parts A, B, C and certify form below Part A*;, Part B*: Sources(s) (include NPDES # if .:Volume (dry, tons) Month Amendment/ applicable). Residual In `Product Out : Name(s).. Bulking Agent unary — bruarp irch IV t October November December Totals: olume (dry tons)I - Intended use(s) nuuuflg 4geni s) useo: * If more space than given is required, please -atta& additional infoniiatioi sheet s () Check box if additional sheets) are. attached Part C: Facility was compliant during calendar, year. a 661. with* 41f-con, dit ons .of the ermif includin but npt limited to items 1-3-below) issued by the P•.. ( Division:of'Water Quality.. .3 Yes 0 No- If No, please provide_ a. written. descri description'. .the facility p y ty.vvas not compliant. 1. All monitoring was done in accordance with the pci7nit and reported:for the year as required and tliree:(3) copies of certified laboratory results are attached. 2. All operation and maintenance requirements were compiled with or, in'the case of a deviation, prior authorization was received from the Division of Water Quality. .3. No contravention of Ground Water Quality Standards occurred at a monitoring. well, "I certify, under penalty of law; that the above information'is' to the best of.iny knowledge and -belief, true, accurate and complete. I am aware tha ere are si nificant penalties for submitting. false information, including the possibility of fines and imprisonment for knowing violations." Signature of Permitt a Date Signature of Preparer**-. Dater '(if different:from P.ermittee).**Preparer is defined in 40 .QFRPart.503.9(r) . i - �.„.::` .• In;=A1D GnDKA MhfiQMEZ 14 4 /nnnr_ Part A Residual Sources and Volume Sludge A Volume Sludge Volume SludgeClass Volume Month Source Produced (dry tons Dewatered Residual Volume Treated Lime Added Produced July TWSA (dry tons) (dry tons) (dry tons) (dry tons) Plant # 1 (NC0039578) 19.11 TWSA Plant # 2 (NC0020214) 2.73 TWSA Plant # 3 (NC0063321) 0.00 Septage Received 2.85 Monthly Totall 24.69 13.72 0 0.00 August TWSA Plant # 1 (NC0039578) 23.51 TWSA Plant # 2 (NC0020214) 1.13 ® TWSA Plant -# 3. (NC0063321) 0.00 Septage Received 2.69 otal 27.33 15.95 0 ® 0 II September TWSA Plant # 1 (NC0039578) 22.84 TWSA Plant # 2 (NC0020214) 3.00 TWSA Plant # 3 (NC0063321) 2.11 Septage Received 1.80 Month!y Total 29.75 15.21 0 0 0 �(- October TWSA Plant # 1 (NC0039578) 25.27 1 TWSA Plant # 2 (NC0020214) 0.00 TWSA Plant # 3 (NC0063321) 0.00 Septage Received 2.89 IxIIrM!y Total 28.16 18.03 p 0 0 November TWSA Plant # 1 (NC0039578) 22.28 TWSA Plant # 2 (NC0020214) 1.49 TWSA Plant # 3 (NC0063321) 0.00 Septage Received 1.62 Month Total 25.39 20.63 ' December TWSA Plant # 1 (NC0039578) 17.12 TWSA Plant # 2 (NC0020214) 0.00 TWSA Plant # 3 (NC0063321) 0.00 Septage Received 2.87 - Month) Total 19.99 11.83 T �� Total Sludge produced by all sources for 2009= 305.36 dry tons Total "sludge" dewatered by belt press in 2009= 203.96 dry tons Total "sludge" treated in pastuerization process in 2009= 45.90 dry tons Total lime added in pastuerization process in 2009= 112.87 dry tons �Total "residual" produced for distribution in 2009=158.77 DRY TONS I 0 Appendix A TWSA PLANT ANNUAL DISTRIBUTION AND MARKETING SUMMARY 2009 Part A Residual Sources and Volume Sludge Volume Sludge Volume Sludge Volume Class A Month Source Produced Dewatered Treated Lime Added (d tons) Residual Volume Produced January TWSA Plant * I (NC003957 (dry tons) d Ions) (dry tons) 13.47 (d tons TWSA Pla4f2 (NC0020214) 0.00 TWSA Plant * 3 (NC0063321) 0.00 Septage Received 1.29 Monthly Total 14.78 13.14 0.00 0.00 0.00 February, TWSA Plant# I (NC0039578) 18.91 TWSA Plant # 2 (NC0020214) 2.74 TWSA Plant # 3 (NC0063321) 0.00 Septage Received 3.14 Month) Total 24.79 20.78 0.00 0.00 March TWSA Plant * 1 (NC0039578) 20.51 0.00 TWSA Plant # 2 (NC0020214) 2.27 TWSA Plant # 3 (NC0063321) 0 Septage Received 1.53 Month) Total 24.31 14.80 0.00 0.00 0.00 April TWSA Plant# 1 (NC00P9578) 23.34 TWSA Plant # 2 (NC0020214) 5.20 TWSA Plant # 3 (NC0063321) 0 Septage Received 2.29 13.9 1 27 IR N Appendix (a) 2009 Distribution and Marketing, Summary (Part B) 1. i q TWSA PLANT # 1 ANNUAL DISTRIBUTION AND MARKETING SUMMARY 2009 A I Part B Recipient Information Est. Volume Month Name Address wet tons Intended Use _ Janyary. _ _ _. Monthly Total 0 7uary Month IV Total 0 March Chester Sorrells 274 Davis Cove Rd. 26 Commercial Hauler Waynesville NC 28786 Jim Rhineheart PO Box 303 182 Pasture/Hayfields Webster NC 28788 ph: 828-399-1878 Phil Woody 376 Mack -town Gap Rd. 0.5 Garden Sylva NC 28779 ph: 828-631-4607 Harold Cole 128 Holstein Drive 20 Hayfield Sylva. NC 28779 ph: 828-586-6770 Lloyd Green 60 Zion Hill Church Rd. 1 Pasture Sylva NC 28779 ph: 828-586-6383 Monthly Total 229.5 April Lloyd Green 60 Zion Hill Church Rd. Sylva NC 28779 4 Pasture h: 828-586-6383 Monthly Total 4 May Chester Sorrells 274 Davis Cove Rd. 26 Commercial Hauler Waynesville NC 28786 Monthiv Total 26 June Monthly Total 0 4 I - Jul Arnold Frady 270 Christmas Tree Lane 2 Pasture/Hayfields Sylva NC 28779 h: 828-631-3858 Monthly Total 2 August Tony Collins 40 Pasture/Hayfields Franklin NC 828-421-0140 Monthly Total 40 September Chester Sorrells 274 Davis Cove Rd. 36 Waynesville NC 28786 Tony Collins 20 Franklin NC 828-421-0140 Monthly Totall 56 October Chester Sorrells 274 Davis Cove Rd. Waynesville NC 28786 14 Pasture/Hayfields Monthly Total 14 November Monthly Total0 December Monthl Total Annual Total 371.5 wet tons (est.) Annual vet tons x 55.4 (avg % solids) = 205.8 dry tons distributes!. h Appendix (b) 2009, Annual Residual Sampling Summary Form f . 2009 Annual Residampling Summary Form Attach this form to the corresponding Annual Report Please note that your permit may contain additional parameters to be analyzed than those required to be summarized on this form. Permit Number:WQ 0005763 Facility Name: Tuckasei9ee Water and Sewer Auth. NPDES # NC 0039578 WQ # : WQ 0005763 WWTP Name: TWSA Plant # 1 ='lai E Sample Date 2/17 5/5 7/14 8/11 8/18 8/24 Avg. i ` li.. Percent Solids 54.3 49.6 . 55.5 58.3 57.2 57.4 55.4 Aluminum 8,720 7,910 8,590 9,460 8,670 P Arsenic 7.7 1 6.7 5.7 6.6 6.68 A Cadmium 0.36 0.44 0.25 0.63 0.42 R Calcium 295,000 319,000. 339 000 331,000 321,000 A Chromium 7.6 7.0 8.6 11.9 8.8 M Copper 84.2 62.6 93.1 104 86 E Lead 4.6 3.5 5.9 6.0 5.0 T Magnesium* 2,850 2,570 2,820 2,920 2,790 E Mercury 0.053 0.41 0.29 0.5 0.313 R Molybdenum < 0.62 < 0.55 1 1.1 1.0 0.5 S Nickel 1.3 1.3 3.3 4.6 2.6 h 12.3 12.0 11.9 12.4 Potassium 2,960 3,730 3,320 3,690 3,425 Selenium 7.8 6.6 4.5 5.8 6.2 Sodium 647 555 < 795 < 870 301 Zinc 256 208 284 324 268 TKN 1,520 15,500 11,700 11,900 10,155 mg/ Ammonia -Nitrogen 241 134 208 286 217 kg Nitrate -Nitrite < 16.7 < 18.1 < 14.3 < 18.1 0.0 Plant Available N 504 4,680 2,070 3,630 2,721 Total Phosphorous 235 3640 206 155 1,059 Fecal Coliform < 200 < 4 < 4 . < 20 < 20 <. 3 I certify, under penalty of law, that this document was prepared under my direction or supervision in accordance with a system designed to assure that qualified personnel properly gathered and evaluated the information submitted. I am aware that there are significanWenalties for submitting false information, including the possibility of fines and imprisonment for knowing violations." Of ��Tl Date Appendix (c) Residual Analysis Pace Analytical Services, Inc. 2225 Riverside Dr. ` r SIC Asheville, NC 28804 (828)254-7176 _ March 03, 2009 Pace Analytical Services, Inc. 9800•KinceyAve. Suite100 Huntersville, NC 28078 (704)875-9092 Mr. Stan Bryson Tuckaseigee. Water & Sewer Co. 1246 West Main Street Sylvia, NC 28779 RE: Project: Lime Residual '2/17/09 Pace Project No.: 9238154 r rY Dear Mr. Bryson: Enclosed are the analytical results for sample(s) receivetl- by the laboratory on February 17, 2009. The -results relate only to the samples included in this report. Results reported herein conform to the most current NELAC standards, where applicable, unless otherwise narrated in the -body of the.. report: Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and Organic testing.was performed at,our Pace Huntersville laboratory unless otherwise footnoted. All Microbiological analyses were performed at the laboratory where the samples were received. If you: have any questions concerning this report, please feel free to contact.me. erely, m Williams 'tom.williams@pacelabs.com '"���`''�:` _ Project Manager - .Enclosures 4 REPORT'OF LABORATORY ANALYSIS This report shall not be reproduced, except in full, -without the written consent of Pace Analytical Services, Inc.. Page 1 of 14 4~ ,,,,II S` R PrI�II6IlG�CI! a{' Pace Analytical Services, Inc. Pace Analytical Se ' " Yt rvices, Inc. d ," '`" wwwp"'acetabs c°rrr 2225 Riverside Dr. Asheville, NC 28804 9800 Kince Ave y. Suite 100 HuntersyiIle, NC 28078 (828)2547176 (704)875_9092 ANALYTICAL -RESULTS _P_[oject; Lime. -Residual, 2/17/09 'Pace Project No.: 9238154 . :.-.Sampler TWSA Lime Residual Lab ID: 9238154001 Collected: 02/17.109 10:00 Received: 02/17/09 12:16 _ Results -reported on. a `dry-weight".basis MatriSolid x: - Parameters Results Units Report Limit DF Prepared Analyzed CAS No. 6010 MET ICP Analytical Method: EPA 6010 Preparation Method: EPA 3050 Qual' Aluminum Arsenia - 8720 mg/kg 12.4 1 7.7 m /k -' g g 02/1.8109 15:30 02/20/09 13:01 7429-90-5 0. 1 __.._.._ _07.7 m /k 9 02/18/ob 15:30 02/20/09 13:01 7440-38-2 Calcium -2 12 1 g 295000 mg/kg 1240. 100 02118/0915:30 02/20/09 13:01 7440-43-9 C- .pper m 7.6 mg/kg 02/18/09 15:30 02/20/09 15:51 7440-70-2 Copper ; tE 6� 1 84.2 mg/kg C : s �' : 02/18/09 15:30 02/20/09 13:01 7440-47-3 :. Leadz.3 1 4.6 m /k g g 02/18/09 15:30 02/20/09 13:01 1 7440-50-8 4 Magnesium. 2850 mg/kg ` 02/18/09 15:30 02/20/09 13:01 7439-92-1 Molybdenum , 72 4 1 ND mg/kg 02/1810915:30 02/20/09 13:01 7439-95 4 Nicker 0.62 1 1.3 mg/kg g g 02/18/09 15:30 02/20/09 13.01 7439=98-7 : P8 Potassium 0.62 1 2960 mg/kg 02/18/0915:30 02/20/0913:01. 7440=02-0 Selenium 622 1 7 8'mg/kg 02/18/09 16.30.. 02/20/09 13:01 '7440-09-7 'Sodium 1.2 1 647 mg/kg 02/18/09 15:30 02120/0913:01 • 7782-49-2 Zinc 622 1 256 mg/kg 02/18/09 15:30 02120/0913:01 7440-23-5 7471 Mercury 1.2 1 02/18/09 15:30 02/20/09 13:01 7440-66-6 Analytical Method: EPA 7471 Preparation Method: EPA 7471 erctry scent Moisture 0.053 m /k g g 0.0067' 1 02/1910916:20 02/20/0911:11 7439-97-6 r Analytical Method: ASTM D2974-87 Percent Moisture :. ' . 42.6 % ' 9045 pH Soil 0.10 1 03/03/09 13:39 .; Analytical Method: EPA 9045 pH at25.Degrees G 12.3 Std. Units 0.10 1 Plant Available Nitrogen Analytical Method: 40CFR PART 503 02/19/09-18:45 . Plant Available Nitrogen 504 mg/kg. Total. Nitrogen Calculation 01GQ 1 Analytical. Method: 40CFR PART 503 UM12r 7. 03/03/09 14.08 �. ,Nitrogen i2� 350.1 Ammonia 1520 mg/kg , A.T._ 1 03/0310914:09 7727-37-9 Analytical Method: EPA:350.1 Nitrogen Ammonia ' 351.2 Total Kjeldahl Nitrogen 241 mg/kg -1b':1 1 02/24/09 10:04 776441 -7 Analytical Method: EPA 351.2 - Nitrogen, Kjeldahl, Total 1520 mg/kg 353.2 Nitrogen NO2IN0 3 . 87.1 1 Analytical Method: EPA 353.2 03/021091.4:35 7727-37-9 Mo ' Nitrogen, NO2 plus NO3 ND mg/kg 365.1 Phosphorus, Total 16.7 1 Analytical Method: EPA 365.1 02/23/09 15:30 - Phosphorus 235 mg/kg 17.4 5 02/19/0917:37 7723-14-0 R1 Ai Vie: 03/03/2009 04:26 PM REPORT OF LABORATORY AN S Page 4 of 14 This report shall not be reproduced, except in full, without the written consent of Pace Analytical Services, Inc.. A Analytical Results ®�=any . IL-- - Pacii�E1a"Wical Mhe.-V@0'e For: 9238154 2225 Riverside Drive Asheville PVC 28804 Entered 2/18/2009 Reported:_:._-.2/19/2009 _..::'.. . Sample Remark **RAN OUT OF HOLD per clients request... Pace Analytical Services, Inc. Pace Analytical Services, Inc. 2225 Riverside Dr. 9800 Kincey Ave. Suite 100 Asheville, NC 28804 Huntersville; NC 28078 (828)254-7176 (704)875-9092 ANALYTICAL RESULTS sdival 5/5/09 race rro)ect No.: 9243444, 1 ... . vv.jn 1-111je 1Ce51Qual Lab lu: 9243444001 Collected: 05/05/09 10:15 Received: 05/05/09 14:00 Matrix Solid. Results reported on a "dry -weight" basis Parameters Results Units Report Limit DF Prepared Analyzed CAS No. Qua[ . 6010 MET ICP Analytical Method: EPA 6010 Preparation Method: EPA 3050 Aluminum : 7916 mg/kg 10.9 1 05/11/09 16:19 05/14/09 00:28 7429-90-5 MO Arsenic --Cadmium 6.7 mg/kg 0.55 1 05/11/09 16:1.9 05/14/09 00:28 7440-38-2 ___._ __ _ _ 0'.44 n g/kg 0.11 1 05/11/09 16:19 05/14/09 00:28 7440-43-9 Calcium 319000 mg/kg 1090 100 05/1170916:19 05/14/09 10:31 7440-70-2 MO Chromium 7.0 mg/kg 0.55 1 05/11/09 16:19 05/14/09 00:28 7440-47-3 Copper Lead 62.6 mg/kg 0.55 1 05/11/09 16:19 05/14/09 00,28 7440-50-8 Magnesium 3.5 mg/kg 0.55 1 05/11/09 16:19 05/14/09 00:28 7439-92-1 Molybdenum 2570 mg/kg 10.9 1 05/11/09 1.6:19 05/14/09 00:28 7439-95-4 ND mg/kg 0.55 1 05/11/b9 16:19 05/14/09 00:28 7439-98-7 Nickel 1.3 mg/kg 0.55 1 05/11/09 16:19 05/14/09 00:28 7440-02-0 Potassium 3730. mg/kg 546 1 05/11/09 16:19 05/14/09 00:28 7440-094 MO Selenium . 6.6 mg/kg 1.1 1 05/11/0916:19 05/14/09 00:28 7782-49-2 Sodium 555 mg/kg 546 1 05/11/09 16:19 05/14/69 00:28 7440-23-5 MO Zinc 208 mg/kg 1.1 1 05/11/09 16:19 05/14/09 00:28 7440-66-6 .7471 Mercury Analytical Method: EPA 7471 Pre aration Method: EPA p . 7471 Mercury 0.41 mg/kg 0.041 5 05/15/0911:30 05117/0913:36 7439-97-6 entWisture Analytical Method: ASTM D2974-87 Percent Moisture 46.8 % 0.10 1 05/07/0913:40 9045 pH Soil Analytical. Method: EPA 9045 .- pHat25D egrees C . .12.0 Std. Units 0.10 1 05/12/0911:25 H1 Plant Available Nitrogen Analytical Method: 40CFR PART 503 Plant Available Nitrogen 4680 mg/kg 1.0 1 06/05/09 09:20 .. -Total Nitrogen Calculation. Analytical* Method: 40CFR PART 503 Nitrogen 15500 mg/kg 40.0 1 06/0410910:39 7727-37-9 350.1 Ammonia Analytical Method: EPA 350.1 Nitrogen, Ammonia 134 mg/kg 16.8 1 05/12/09 11:05 7764-41-7 353.2 Nitrogen; NO2/NO3 Analytical Method: EPA 353.2 Nitrogen, Nitrate Nitrogen, Nitrite ND mg/kg ND mg/kg 18.1- 18.1 1 1 05/15/09 09:08. Nitrogen, NO2 plus NO3 ND mg/kg 18.1 1 05/15/09 09:08 05/15/09 09:08 365.1 Phosphorus, Total Analytical Method: EPA 365.1 phosphorus 3640 mg/kg 9.0 1 05/14/09 21:07 7723-14-0 oi'�. 6/05/2009 09:20 AM REPORT OF LABORATORY ANALYSIS Page 4 of 13 This report shall not b d e repro ueed, except in full, without the written consent of Pace Analytical Services, Inc.. Analytical Results Pace Analytical Asheville For: 9243444 2225 Riverside Drive Asheville. NC 28804 Entered 5/6/2009 P.O. Box 228 • -Statesville, North Carolina 28687. 704/872/4697 Analytical X I-sults Pace Analy-tical Ashevilie For: 9248499 2225 Riverside Drive Asheville NC 28804 Entered 7/16/2009 Repgited: 7/20/2009 P.O. Box 228 • Statesville, North Carolina 28687 ,, 704/872/4697 c Pace Analytical Services, Inc. ® 2225 Riverside Dr. " n�irtJcaf. wwwpacelabs_com; Asheville, NC 28804 }. (828)254-7176 Pace Analytical Services, Inc. 9800 Kincey Ave. Suite 100 Huntersville, NC 28078 (704)875-9092 ANALYTICAL RESULTS Project: Lime Residual 8/11/0*9 Pace Project No.: 9250568= Sample:. TWSA Lime Residual. Lab ID: 9250568001 Collected: 08/10/09 00:00 Received: 08/1110915:52 Matrix: Solid Results reported on a "dry -weight' basis Parameters Results Units Report Limit DF Prepared Analyzed CAS No �6010 MET ICP Analytical Method: EPA 6010 Preparation Method: EPA 3050 . Aluminum. Arsenic 8590 mg/kg 15.9 1 08/14/00 08:25 08/14/09 19:22 7429-90-5 Cadmium - - 5.7 mg/kg - _.. - . - -. 0.79 1 08/14/09 08:25 08/14/09 19:22 7440-38-2. - ---- - Calcium 0.25 mg/kg 0.16 1 08/14/09 08:25 08/14/09 19:22 7440 43-9 Chromium 339000 mg/kg 795 50 _ 08/14/09 08:25 08/17/09 14:10 7440-70-2 Copper 8.6 mg/kg 93.1 mg/kg 0.79 1 08/14/09 08:25 08/14/09 19:22 7440-47-3 Lead 0.79 1 08/14/09 08:25 08/14/09 19:22 7440-50-8 Magnesium 5.9 mg/kg 0.79 1 08/14/09 08:25 08/14/09 19:22 7439-92-1 Molybdenum 2820 mg/kg 15.9 1 08/14/09 08:25. 08/14/09 19:22 7439-95-4 Nickel 1.1 mg/kg 0.79 1 08/14/09 08:25 08/14/09 19:22 7439-98-7 Potassium ISelenium 3.3 mg/kg 0.79 1 08/14/09 08:25 08/14/09 19:22 7440-02-0 3320 mg/kg 795 1 08/14/09 08:25 08/14/09 19:22 7440-09-7 Sodium 4.5 mg/kg 1.6 1 08/14/09 08:25 08/14/09 19:22 7782-49-2 Zinc ND mg/kg 795 1 .08/14/09 08:25 08/14/09 19:22 7440-23-5 17471 284 mg/kg 1.6 1 08/14/09 08:25 08/14/09 19:22 7440-66-6 Mercury Analytical Method: Yt EPA 7471 Preparation Method: EPA 7471 Mercury . 0.29 mg/kg 0.042 5 08/13/09 11:41 08/1410911:47 7439-97-6 1 nt Moisture Analytical Method: ASTM D2974-87 Percent Moisture 41.7 % 0.10 1 08/12/09 00:00 t045 pH Soil Analytical Method: EPA 9045 H at 25 Degrees C 11.9 Sid. Units 0.10 1 08/14/09 18:45 lant Available Nitrogen Analytical Method: 40CFR PART 503 (ant Available Nitrogen ` 2070 mg/kg 1.0 1 08/25/09 15:53 Total Nitrogen Calculation Analytical Method: 40CFR PART 503 itrogen 6830 mg/kg 40.0 1 08/25/09 15:53 7727-37-9 350.1. Ammonia Analytical Method: EPA 350.1 .. itrogen, Ammonia 208 mg/kg 19.1 1 08/13/09 15:41 7764-41-7 1.. 2 Total Kjeldahl Nitrogen , Analytical Method: EPA 351.2 itrogen, Kjeldahl, Total 11700 mg/kg .. 1450 50 08/16/09 11:18 7727-37-9 3.2 Nitrogen, NO2/NO3 Analytical Method: EPA 353.2 Nitrogen, Nitrate ND. mg/kg 14.3 1 trogen; Nitrite ND mg/kg 14.3 1 08/18/09 18:01 trogen, NO2 plus NO3 -- ND mg/kg 14.3 08/18/09 18:01 1 08/18/09 18:01 365:1 Phosphorus, Total Analytical Method: EPA 365.1 osphorus 206 mg/kg 16.3 2 08/1810913:22 7723-14-0 e ovzoos 12:14 PM REPORT OF I ABORATO W H1 Qua[ RY ANALYSIS Page 4 of 13 This report shall not be reproduced, except in full, without the written consent of Pace Analytical Services, Inc.. Analytical Results i�- Pace Analytical -Asheville For: 9250568 � T 2225 Riverside Drive. Asheville NG 28804 Entered 8/12/2009 �-Reported: 8/17/2009 Sample Remark__._ liample ID Parameter CCust I.D Result Units Method Date Analyzes! Analyst 090812-2 %.Solids 9250568001 58.3 % SM2540B , 8/12/09 MD ,090812-2. Fecal Colifoim MTF 9250568001 <20 MPN/g SM92210E 8/12/09 MD Respectfully submitted, C ena .Myers NG Cert #440,. f NCDW Cert #37755, P.O. Box 228 o Statesville, North Carolina 28687. 704/872/4697 Analytical Results Pace Analytical -Asheville For: 9251122 -12225 Riverside Drive -Ashevillum NC 28804 Entered 8/19/2009 Reported: '8i26/2009 Sample Remark Osample ID Parameter Cutt I*D Result Units -Metho'd Date Analyzed Analyst 09081.9-2 % Solids Linie Residual 57.2. SM2540B- 8/19/09 MD 090.819-2 Fecal Colif6rm MTF Lime Residual <20 MPN/g SM9221 CE 8/19/09 MD Respecffullysubmifted, fv� -A L NC Cert #440; NCDW C'ert#'37'7* EPA. NCO0909 P.O. Box 228 9 Statesville, North Oarolina, 28687 a 704/872/4697 Pace Analyticat Services, Inc. 2225 Riverside Dr. Asheville, NC 28804 (828)254-7176 ANALYTICAL RESULTS ct: Lime Residual OS/24 -ae.Proiect No:: 9251576. " Pace Analytical Services, Inc. 9800 Kincey Ave. Suite 100 Huntersville, NC 28018 (704)875-9092 ample: TWSA LIME RESIDUE .- Lab ID: 9251576001 Collected: 08/24/0911:00 Received: uaizaaua -1z:09 iwauix Qunu esults reported on'a "dry -weight" basis Parameters Results Units Report Limit DF Prepared Analyzed CAS No. Qual �i010 MET ICP - Analytical Method: EPA 6010 Preparation Method: EPA 3050 Aluminum 9460 mg/kg 17.4 1 08/25/0913:37 08/27/09 06:10 7429-90-5 :. 0.87 1 08/25/0913:37 08/27/09 06:10 7440-38-2 Igrsenic - ... admium 0.63 mg/kg 0.17 1 08/25/0913:37 08/27/09 08:10 .7440-43-9 331000 mg/kg 1740 100 08/25/0913:37 08/28/0912:54 7440-70-2 calcium Chromium 11.9 mg/kg 1.9 0.87 1 08125/0913:37 08/27/09 06:10 7440-47-3 tipper 04 mg/kg 0.87 1 08/25/09 13:37 08/27/09 06:10 7440-50-8 R-op mg/kg 0.87 1 08/25/0913:37 08/27/09 06:10 7439-92-1 29.0 mg/kg 20 17.4 1 .08/25/0913:37 08/27/09 06:10 7439-95-4 Magnesium Molybdenum mg/kg 0.87 1 08125/0913:37 08/27/09 06:10 7439-98-7 _Molybdenum i 4.6 mg/kg 0.87 1 08/25/0913:37 08/27/09 06:10 7440-02-0 otassium 3690 mg/kg 870 1. 08/25/0913:37' 08/27/09 06:10 7440-09-7 Selenium 5.8 mg/kg., 1.7 10 08/25/0913:37 08/27/09 06:10 7782-49-2 ND mg/kg 870 1 08/25/0913`:37 ' 08/27/09 06:10 7440-23-5 Sodium 324 mg/kg 1.7 1 08/2510913:37 08/27/09 06:10 7440-66-6 inc : Analytical Method: EPA 7471 Preparation Method: EPA 7471 7471 Mercury - ' 0.50 mg/kg 0.038 5 09/01/09 08:02 09/01/09 13:48 7439-97-6 eerrcury t Moisture Analytical Method: ASTM D2974-87 Percent Moisture 44.7 % 0.10 1. 08/31/0914:11 045.pH Soil Analytical Method: EPA 9045 pH at 25 Degrees C 12.4 Std. Units 0.10 1 09/04/0916:00 H1 lant Available Nitrogen.. Analytical Method: 40CFR PART 503 R-lant Available Nitrogen 3630 mg/kg. 1.0 1 08/31/0916:09 otal Nitrogen Calculation Analytical Method: 40CFR PART 503 itro en g 11900 mg/kg 40.0 1 08/31/09 16:06 , 7727-37-9 :�.-.-350.1 Ammonia Analytical Method: EPA 360.1 itrogen, Ammonia 286 mg/kg 15.1 1 08/27/09 17:01 7764-41-7 . 351.2 Total Kjeldahl Nitrogen Analytical Method: EPA 351.2 Kjeldahl, Total _ 11900 mg/kg 862 10 08/30/09 12:02 7727-37-9 .1 Wit.rogen, i,,53.2- Nitrogen, NO2IN03 Analytical Method: EPA 353:2 Nitrogen, Nitrate ND mg/kg 18.1 1 08/28/09 09:00 itrogen, Nitrite ND mg/kg4 18.1 1 08/28109 09:00 itrogen, NO2 plus NO3 ND mg/kg 18.1 1 08/28/09 09:00 i.1 Phosphorus, Total . Analytical Method: EPA 365.1 �sphorus 155.mg/kg 15.1 1 09107/0914:00 7723-140 it 09/11/2009 04:37 PM. REPORT OF LABORATORY ANALYSIS. This report shall not be reproduced, except in full, without the written consent of Pace. Analytical Services, Inc.. - ,N ♦CCpR�' 1 n Page 4 of 14 F - 'y Analytical Results !ace Analytica-A.4hevAlle For: 9251576 2225 Riverside Drive Asheville NC 28804 Entered 8/25/2009 Reported:, 9/2/2009 -Sample Remarks ' Sample OD Parameter. Cust.113 Result Unit Method Date Ana�yaed Analyst 090825-13 % Solids 9251576001 57.4 % SM2540B 8/25/09 CL 090825-13 Fecal Col'iform IVITF 9251576001 <3 MPN/g SM92210E 8/25109 CL Respectfully submitted, Dena Myers J =: NCDW Cert. #37755 EPA NC00909 P.O. Box 228 • Statesville, North Carolina 28687 0 704/872/4697 A., Appendix (d) zoo9 TCLP Analysis ace -Mali cal f www.pacebbs co.: Pace Analytical Services, Inc. 2225 Riverside Dr. Asheville, NC 28804 (828)254-7176 ANALYTICAL RESULTS Pace Analytical Services, Inc. 9800 Kincey Ave. Suite 100 Huntersville, NC 28078 (704)875-9092 Project: TWSA #1 Sludge 8/18/09 Pace Project No.: 9251120 Sample: Sludge Lab ID: 9251120001 Collected: 08/18/0910:30 Received: 08/18/09 13:00 Matrix: Water Parameters, Results Units Report Limit DF Prepared Analyzed CAS No. Qual 8081 GCS Pesticides, TCLP SPE Analytical Method: EPA 8081 Preparation Method: EPA 3535 Leachate Method/Date: EPA 1311; 08/25/09 14:42 gamma-BHC (Lindane) ND ug/L 0.50 1 08/28/09 14:00 09/02/09 11:36 (Technical) ND. ug/L 3.0 1 .58-89-9 08/28/09 14:00 09/02/09 11:36 57-74-9 UChlordane. ; Hepta Heptachlor epoxide. ND ug/L 0.50 1 08/28/09 14:00 09/02/09 11:36 72-20-8 Methoxychlor ND ug/L 0.50 1 08/28/09 14:00 09/02/09 11:36 1024-57-3 Toxaphene ND ug/L ND ug/L 1000 1 08/28/09 14:00 09/02/09 11:36 72-43-5 Decachlorobiphenyl (S) 11 % 3.0 1 08/28/09 14:00 09/02/09 11:36 8001-35-2 Tetrachloro-m-xylene (S) 19 % 10-138 1 08/28/09 14:00 09/02/09 11:36 2051-24-3 10-110 1 08/28/09 14:00 09/02/09 11:36 877-09-8 6010 MET ICP, TCLP Analytical Method: EPA 6010 Preparation Method: EPA 3010 Leachate Method/Date: EPA 1311; 08/24/09 15:13 Arsenic Barium ND mg/L 0.025 1 08/25/09 09:25 08/27/69 03:37 7440-38-2 . Cadmium 0.039 mg/L ND mg/L 0.025 1 0.0050 1 08/25/09 09:25 08/25/09 09:25 08/27/09 03:37 7440-39-3 i Chromium 08/27/09 03:37 7440-43-9 Lead ND mg/L 0.025 1 08/25/09 09:25 08/27/09 03:37 7440-47-3 ND mg/L 0.025 1 08/25/09 09:25 08/27/09 03:37 7439-92-1 ,'. rnium ND mg/L. 0.050 1 08/25/09 09:25 08/27/09.03:37 7782-49-2 (44f ND mg/L 0.025 1 08/25/09 09:25 08/27/09 03:37 7440-22-4 7470 Mercury, TCLP Analytical Method: EPA 7470 Preparation Method: EPA 7470 Leachate Method/Date: EPA 1311; 08/24/09 15:13 Mercury ND ug/L 0.20 1 08/25/09 09:16 08/25/09 12:37 7439-97-6 8270 MSSV TCLP Sep Funnel Analytical Method: EPA 8270 Preparation Method: EPA 3510 Leachate Method/Date: EPA 1311; b8/25/09 14:42 1,4-Dichlorobenzene ND ug/L 25.0 1 08/31/09 10:00 09/03/0914:58 106-46-7 _-:- 2,4-Dinitrotoluene Hex6chloro-1,3-butadiene ND ug/L 25.0 1 08/31/09 10:00 09/03/09 14:58 121-14-2 ` Hexachloeobenzene ND ug/L 25.0 1 08/3110910:00 09/03/09 14:58 87-68-3 . Hexachloroethane ND ug/L 25.0 1 08/31/09 10:00 09/03/09 14:58 118-74-1 2-Methylphenol(o-Cresol) ND ug/L ND ug/L 25.0 1 08/3110910:00 09/03/09 14:58 67-72-1 3&4-Methylphenol(m&p Cresol) 218 ug/L 25.0 1 08/31/09 10:00 09/03/09 14:58 95-48-7 Nitrobenzene 25.0 1 08/31/09 10:00 09/03/09 14:58 Pentachlorophenol ND ug/L 25.0 1 08/31/09 10:00. 09/03/0914:53 98-95-3 Pyridine ND ug/L 25.0 1 08/31/09 10:00 09/03/09 14:58 87-86-5 2,4,5-Trichlorophenol ND ug/L ND 25.0 1 08/31/09 10:00 09/03/09 14:58 110-86-1 -52- 4,6lrichlorophenol. ug/L ND ug/L 25.0 1 08/31/09 10:00 09/03/09 14:58 95-95-4 ; "Nitrobenzene d5 (S) 49 % 25:0 1 08/31/09 10:00 09/03/09 14:58 88-06-2 k. =rpheFluorobiphenyl (S) 56 % 30-150 1 08/31/09 10:00 09/03/09 14:58 4165-60-0 nyl d14 S) U-Te 55 % 30-150 1 08/31/09 10:00 09/03/09 14:58 321-60-8 i-- ;` Phenol-d6 (S) 30-150 1 08/31/09 10:00 09/03/09 14:58 1718-51-0 -... =-2=Fluorophenol (S) 25 % 34 % 25-150• 1 08/31/09 10:00 09/03/09 14:58 13127-88-3 .--.24,6-Tnbromophenol(S) 49 %. 25-150 1 08/31/09 10:00 09/03/09 14:58 367-12-4 ,Jas 25-150 1 08/31/09 10:00 09103/0914:58 118-79-6 09/04/2009 02:43 PM REPORT OF LABORATORY ANALYSIS This report shall not be reproduced, except in full, without the written consent of Pace Analytical Services, Inc.. `K\ 4 Page 5 of 15 Pace Analytical Services, Inc. Pace Analytical Services, Inc. aceMal rtcal 2225 Riverside Dr. 9800 Kincey Ave. Suite 100 /r nnvwpeceia6s°com: Asheville, NC 28804 Huntersville, NC 28078 t (828)254-7176 (704)875-9092 ANALYTICAL RESULTS Project: TWSA #1 Sludge 8/18109 Pace -Project No.: 9251120 Sample: Sludge Lab ID: 9251120001 Collected: 08/18/09 10:30 Received: 08/1.8/0913:00 Matrix Water Parameters Results Units - Report Limit DF Prepared Analyzed CAS No. Qual 8260 MSV TCLP Analytical Method: EPA 8260 Benzene ND ug/L 125 25 08/24/09 15:20 71-43-2 2-Butanone (MEK) 319 ug/L 250 25 - 08/24/09 15:20 78-93-3 Carbon tetrachloride ND ug/L 125 25 08/24/09 15:20 5 Chloroform Chiorobenzene —_ --_— -- - " ND ug/L 125 25 08/24/09 15:20 56-23-56-23--7 ND ug/L 125 25 08/24/09 15:20 67-66-3 1,4-Dichlorobenzene ND ug/L 125 25 08/24/09 15:20 106-46-7 ®1,2-Dichloroeth:ug/L 125 25 08/24/09 15:20 107-06-2 1,1-Dichloroethene ne ND ND ug/L 125 25 08124/0915:20 75-35-4 Tetrachloroethene ND ug/L 125 25 08/24/09 15:20 127-18 4 Trichloroethene ND ug/L 125 25 08/24/0915:20 79-01-6 Vinyl chloride ND u /L 08/24/09 15:20 75-01-4 bl*uei *e-d8 S) ' d4 (S) 94 % 79-120 25 08/24/09 15:20 17060-07-0 Toluene-d8 (S) 101 % 70-120 25 4Bromofluorobenzene (S) 96 % 08/24/09 15:20 2037-26-5 87-109 25 08/24/09 15:20 460-00-4 Dibromofluoiomethane (S) 94 % 85-115 25 08/24/09 15:20 1868-53-7 9095 Paint Filter Liquid Test' Analytical Method: EPA 9095 Free Liquids 0 mL/5min 1.0 1 08/28/0919:45 i l 09/04/2009 02:43 PM REPORT. OF LABORATORY ANALYSIS Page 6 of 15 This report shall not be reproduced, except in full, r without the written consent of Pace Analytical Services, Inc.. R" Analytical Environmental Services, Inc Date: 26-Aug-09 Client: Pace Analytical Services, Inc. Client. Sample ID: SLUDGE - Project: 9251120 Collection Date: 8/18/2009 10:30:00 AM Lab ID: 090809-001 Matrix: Aqueous, Analyses Result Reporting Qual Units BatchED Dilution Date Analyzed Analyst Limit Factor HERBICIDES, TCLP SW1311/8151A (SW3510B) 2,4,5-TP (Silvex) BRL 0.20 mg/L. 117392 1 08/2412009 21:38 AK 2,4-D BRL 0.20 mgIL 117392 1 08/24/2009 21:38 AK S.: DCAA 94.9 36.6-149 %REC .117392 1 08/24/2009 21:38 AY, w Qualifiers: Value exceeds maximum contaminant livtil E Estimated (value above quantitation range) BRL Belowrepqrting limit S Spike Recovery outside limits due to matrix H Holding times forprdparation oranalysis exceeded a Nan' See case narrative N Analyte not NELAC certified NC Not confirmed B Analyte detected in the associated method blafik� < Less than Result vain > Greater than Result value Page 3 of 5 j A Appendix (e) v Pathogen and.' Vector Attraction Reduction Form 7 ANNUAL PATHOGEN AND VECTOR ATTRACTION REDUCTION FORM Facility Name: p P-e- Permit Number: (Arc) 0006 9/93 i... Ak VNffPNanie: NPDES. Number: AE Monitoring Period: From Th To Pathogen Redix6tion. (40 CFR 503.32) - Please indicate level achieved and alternative performed: Class A: Alternative 1 D Alternative 2 ❑ Alternative 3 ❑ .... .. . .... ........ . . Alterndtive.4 Alternative 5 Al Alternative ive' 6 0 ....... If applicable to alternativeperformed (Class A only) indicate "Process to Further Reduce Pathogens": Compost E3 Heat Drying �Ej Heat Treatment ❑ Thermophilic ❑ Beta Ray 'a Ray [I Pasteurization _77 Alternative2 [3 --C-4ass-B.—I���—Alte-mative--IEI:& - . . Alternative 3 El if.applicable to alternative performed (Class B only) indicate "Process to- Significantly Reduce Pathogens": — Lime Stabilization ❑ Air Drying El Composting. El ' jAerobic Digestion 0 Anaerobic Digestion[] ........... ................ ........................................ X ................... ................. .. ........ : ....... 1.1.!.-.1...-....1.*.1.*:1 ................................. ....... ........ ....... If -applicable to alternative performed (Class A or. Class B) complete the following monitoring data: iAllo . wdble-Ltiel Pathogen Density Number of Excee- Frequency 'Sample Analytical Paradneter, in Sludge Minimum Geo. Mean MaximuTr Uni S dences (if Amalygis Type Tech -pique 2 x .10 to..the 6th. power 1M.PN per gram of total . solids or2x 10to 'Fecal'Co"lifdrm tho 6t4: power ..gj= CFU'1j 'um of i000 rapfiper of total.solid ,rA P P11r M. (dry weight)' '[ Salmonella badtPria. 3 NTN per 4. jffi.lieu.of fecal. granis total solid. (di* Weight). Vector Attraction Reductio*11:.(4.0'CFR 503.33) Please indicate .option performed: ............ Op tion 'El] - Option 3 -0" JOption El' Option 5 [1 ........... Option 0joption-7. 111Option 8. .0. option 9 ❑ 1.Option 10 . ................ .................. e1.'.'.'.*.1 ................ ................ .................... .... ............ ................................. ................ No: vector attraction reduction options were performed 0 .............. I ... X.7 ................... .. .......................................... CERTIFICATION STATEMENT (please check the appropriate -statement) "I certify,. nn . der penalty of law, that the: . pathogen. requirements in 40 CFR 503.32 and the vector , -attraction -t e-duction- requirement -in 40 CFR 503.33 have been met." El ."I- certify, under penalty of law,, that the.pathogeii requirements in 40 CFR 503.32 and the vector attraction reduction requirein e*n*t in 40 CFR 503.33 have not been biet." (Please note if you check this. statement attach an explanation why you have not met one or both of the requirements.) "This determination has been made under my direction and supervision in accordance with the system designedlo. ensure that qualifie.d.pers6nnel properly gather and evaluate. the information 'used to determine that the pathogen athogen and vector attraction reduction requirements -have been met. I ,,*g'axn aware that there are significant penalties for false certification including fine and imprisonment." Sb r ,4;5W _W w P-repar r Nameand Title .(type or print) Land Applier Name and Title (if applicable)(type'or print) '* Appendix (g) 2009 SLUDGE DATA TWSA PLANT # 1 (1.5 mgd) NPDES # NC0039578 SLUDGE TO DIGESTOR............................................................... 11,467,000 gallons total lbs....................................................................497,315 lbs total tons.............................................................. .248.7 tons -- -- - -- - total metric tons........................................................225.5 metric tons TWSA PLANT # 2 (.5 mgd) NPDES # NCO020214 SLUDGE HAULED TO PLANT # 1................................................ 322,746 gallons total tons...................................................................24.86 tons total metric tons........................................................22.55 metric tons TWSA PLANT # 3 (.1 mgd) NPDES # NCO063321 SLUDGE HAULED TO PLANT # 1.................................................... 47,006 gallons total tons............................:........................................ 4.36 tons total metric tons...........................................................3.95 metric tons Septage Receiving Station................................................347209 gallons total tons................................................................20.25 tons total metric tons......................................................18 37 metHe tons A portion of the sludge that was generated at the Tuckaseigee Water and Sewer Authority during 2009 was hauled by a private contractor to a designated landfill. Landfill: R&BLandfill 610 Frank Bennett Road Homer GA 30080 A total of 93a 2 wit tons were hauled to the landfill during 2009. Copies of haul tickets can be provided if needed. PROCESS SUMMARY SHEET PLANT NAME TWSA #1 . ANNUAL (2009) )R THE PERIOD OF 1/1/2009 THROUGH 12/31/2009 ANT FLOW, mgd 0.887 daily avg FLUENT BOD, mg/I 180.8 daily avg 'FLUENT SS, mg/I 27.2 daily avg LSS, mg/l 2636 daily avg 3SS, mg/I 5254 daily avg AS RATE, mgd 0.03142 daily avg _R. BASIN VOL., mg 0.468 .ARIFIER VOL, mg 0.1508 M RATIO LB APPLIED/LB UNDER AERATION CRT i It , ;1 DAYS _._..- -- - -._ ._ _ ---.-----AC-T-IVAT-ED SLUDGE DATA 30 MIN SETT. SLUDGE 485 MLSS m /I 3044 MLVSS m /I 2462 EFF FLOW MGD 0.979 RSSS m /I 6679 ZSV ftthr 4.6 SVI 159 MCRT da s 13 SLUDGE WASTING allons Ibs 522,000 26,939 704 2932 2494 0.889 5358 3.2 E34 794,500 37,830 ;10 510 2332 1975 0.857 5375 6.3 210 1,033,500 41,016 653 2765 2262 0.901 - 5823 4.8 231 8 954,000 46,677 528 2670 2133 0.914 5423 5.1 194 10. 828,000 37,905 542 2590 2060 0.706 4666 4.3 205 8 1,134,000 46,690 530 2351 1884 0.665 4271 4.7 219 9 1,035,000 38,218 562 2468 2048 0.719 4305 5.2 223 8 1260,000 47,013 591 2560 2033 0.995 4818 3.4 230 8 1,161,000 45,672 587 2852 2270 0.949 6020 4.2 203 8 974,250 50,550 401 2642 2169 1.015 5298 5.7 148 8 999,000 44,566 403 2429 1955 1.049 5007 5.8 160 9 771,750 34,239 541 2636 2145 0.887 5254 4.8 201 9 704 3044 2494 1.049 6679 6.3 234 13 401 2332 1884 0.665 4271 3.2 148 8 Total Gallonsil1,467,000 Daily Averag Te%+mi +nnc X 9n7 metric 955,583 1,260,000 522,000 1363 50550 `26939 497,315 31 416 248.7 ton/English ton= 225.5 My Metric Ton �datly;; dotal lbs. Total tons 2009 TWSA #2 SLUDGE PRODUCTION MONTH DATE Gals Hauled To TWSA # 1 % SOLIDS TOTAL DRY TON Hauler JanuarV 0 0.00 .,IT,... ta'l Februa 2116 24,729 2.66 2.74 Plank 1 1! 41 March 3/26 19,132 2.08 1.66 Cooper 3/27, 6,936 2.11 0.61. Cooper 1 If I H 11 i I I I I iM, April 4/14 4.,494 1.87 0.35 Plank 4/15 16,738 1.79 1.25 Cooper 4/16, 4,843 1.72 0.35 Cooper 4/21 13,671 1.81 1.03 Plank 4/29 25,303 2.11 2.22 Plank May 5/22 23,478 1.97 1.93 Cooper a 4n 7 in it June 6/3 22,891 2.14 2.04 Plank 6/23 26,629 2.10 2.33 Cooper M, July 7/27 19,077 1.23 0.98 Cooper 7/28 7269 1.17 0.35 Cooper 7/30 23342 1.44 1.40 Plank t .14 August 8/27 11,649 1.79 0.,87 TWSA 8/28 4,795 1.33 0.27 TV1JSA n ffill T:, A 1 '3 September 913 21,584 1.33 1.20 TWSA 914 16904 1.35 0.95 TWSA 9/10 7210 1.46 0.44 TWSA 9/17, 7200 0.41 TWSA jw it it ij:. if 1 R! October 0.00 TWSA Manthl 0ti 5i il Pildbo November 11/18 7,082 1.44 0.42 TWSA 11/19 14,330 1.78 1.06 TWSA M - - 1� ----T..-b -1-111.112* -11A Tl Decemberl -fl W-9. TOTAL 3227461 TOTAL 24.86 X.907 metric ton/English Ton 22.55 = Dry Metric Tons .2009 TWSA #3 Sludge Production MONTH Date Gals Hauled To TWSA # I AVG % SOLIDS TOTAL DRY TON Hauler JanuarV Feb. 0 H. ...... R nth ;,TotalMarch HLA lit" '060*0 HNM-;Iji' Nil ---------- A. 40011Y.-Twi April 7777777 11 t hthh-.IT NOW May 5/15 6,194 2.82 0.75 Coopers 5116 4,039 0.39 Coo ers 5/18 4,682 1.52 0.30 Coopers 5/19 7,016 1.63 0.48 Coo ers 5/20. 2,342. 3.39. 0.33 Coopers N�'. t*tbI.vhiITb June M hthk:Tote Julyl vil-r-jr-l-Ill-il"' Auaust Mill n t h 1, T-f - I 11/9 4,581 2.54 Hit M.0 0.48 Coopers Sep. 11110 4602 2.54 0A9 Coo ers 11/11 2202 2.57 0.24 Coopers 11112 2340 2.59 0.25 Coopers 11116 4413 1.76 0.32 Coopers 11/17 4405 . . P, 1 " I i -. 0.32 Coopers IN.p[liq -.M - h, 1 IT H 22 fiQ Oct Mon. Tote t IiIN N Nov. , Toll[; i7l'ifl-11 00 Dec. 11, Mfg 47.006 1 4.36 TOTAL 1 TOTAL 4.36 X .907 metric ton/English Ton 3.95 = Dry Metric Tons 2009 Septage Receiving Station MONTH Beginning Reading Ending Reading Gals Received @ TWSA # 1 - Gals of Sludge from TWSA # 2 & 3 = total gallons se to a received January 11882,660 1904,881 881 22,171 0 22,171 February 1,904,831 1,983,471 78,640 24,729 53 911 March 1,983,471 2,035,792 52,321 26,068 26,253 _Aril _ _ 2,035,792, 2,140 043 104,251 65 049 39 202 Ma 2 140 043 2 237 394 97 351 47 941 49 410 June 2,237,394 2,314 773 77,379 49,520 27,859 July,2,314,773 2 406 789 92,016 43,148, 48,868 August 2,406,789 2,469,350 62,561 16,444, 46,117 September 2,469 350 2,553,049 83,699 52,898 30,801. October 2,553,049 2,602,583 49,534 0 49534 November 2,602,583 2,651,765 49,182 21,412 27770 December 2,651,765 2,700,047 49.182 0 49 182 TOTAL 818,287 347 209 471 778 . TOTAL _347.209 gallons x 1 4% (1994 long term monitoring) 24000 = 20.25 tons x .907metric tons/English ton =18.37 dry metric tons SECTION 11244 POLYMER FEED SYSTEM PART 1: GENERAL 1.01 SCOPE OF WORK A. The polymer feed system shall include all components necessary for the mixing, storage and metering of emulsion polymer, the metering of the water supply, and all necessary starters, and control panels. The system shall be furnished complete with all components described herein to ensure uniformity of appearance of the installation and eliminate divided responsibility for parts, service, and operation. The equipment furnished shall be installed at the location indicated on the plans. B. Unless otherwise noted, all materials and equipment supplied under this Section shall be new, of good quality, and in good condition. 1.02 SYSTEM DESCRIPTION A. General: The polymer feed system shall automatically meter, dilute, activate and feed emulsion polymer and water. The system shall be a self contained unit supplied on a skid with connections for power, water supply, emulsion polymer, and mixed polymer discharge. 1.03 QUALITY ASSURANCE A. The polymer feed system shall be the product of a company which has manufactured chemical feeders of comparable type and capacity for at least five years. 1.04 SUBMITTALS A. Shop Drawings: The Contractor shall submit at least six (6) copies of complete shop drawings to the Engineer for approval. B. Operation and Maintenance Manuals: The Contractor shall submit at least three (3) sets of operation and maintenance manuals to the Engineer. 1.05 DELIVERY, STORAGE AND HANDLING A. All materials and equipment shall be delivered, stored and handled in strict accordance with the manufacturer's recommendations. Rev. 6123/09 PROJECT # 05734 11244 - Page 1 1.06 WARRANTY A. The manufacturer shall warrant the equipment to be free from defects in material and workmanship for a period of one (1) year after being placed into operation. 1.07 MANUFACTURER AND SUPPLIER INFORMATION A. Manufacturer Nameplate:A manufacturer's nameplate shall be securely and permanently mounted to each individual piece of equipment furnished under this Section. The nameplate shall be constructed of a durable, non- corrosive material. Critical information shall be clearly engraved or otherwise permanently stamped on the nameplate, and shall be fully legible. The information contained on the manufacturer nameplate shall include at least the following: 1. Manufacturer's Serial Number 2. Name, address and telephone number of equipment manufacturer 3. Model and/or Part Number, including pump impeller sizes, when applicable 4. Performance Criteria (i.e., capacity, design point, etc.) 5. Motor size, speed and voltage 6. Enclosure Type or Rating 7. Any other pertinent information Note: All equipment shall include a nameplate with a manufacturer serial number validating the equipment as new. Failure to meet these requirements will be cause for rejection of the equipment. B. Supplier and Service Information: A durable nameplate, stamp or sticker shall be adhered to each individual piece of equipment containing the name, address, and telephone number of the local business that supplied the equipment, and the name, address and telephone number of the local business that can provide service and replacement parts for the equipment. A 24-hour emergency service telephone number should also be included. Rev. 6/23/09 PROJECT # 05734 11244 - Page 2 PART 2: PRODUCTS 2.01 EQUIPMENT A. GENERAL REQUIREMENTS The polymer feed system shall automatically meter, dilute, activate and feed emulsion polymer and water. Concentrated polymer and water shall be blended in a completely mixed environment that shall meet polymer supplier's recommendations at maximum throughput. The equipment furnished shall be installed at the location indicated on the plans. B. POLYMER SYSTEM The system shall include a progressive cavity type polymer metering pump capable of pumping emulsion type polymer at an output range suitable for a 1.0 meter belt filter press. The system shall include a metering pump calibration assembly with isolation valves. The system shall have a solenoid valve for on -off control of dilution water supply and a flow indicator equipped with an integral rate adjusting valve. The water flow rate shall be adjustable in a flow range suitable for a 1.0 meter belt filter press. Solids concentration of the sludge as fed to the belt filter press shall be 1.0 to 4.0 percent oven dried solids (ODS). C. Drum Mixer The manufacturer shall provide (1) mechanical mixer sized to completely mix the contents of a 55 gallon drum. D. CONTROLS An independent polymer system control panel shall be provided for the operation of the system. The complete system shall be UL listed and labeled as a system. Provision shall be made for both manual and automatic control with individual stop and start pushbuttons for all motor -driven components and actuation of the water supply. The controls shall be arranged such that in the event of water supply failure it shall shut down automatically. Upon restoration of the water supply, or of power after power failure, the system must be restarted in automatic mode. Timing controls shall be provided for adjustment of polymer mixing cycle. The control panel shall obtain a 4-20ma control signal from the Belt Filter Press Control Panel to set the polymer flow rate. The control panel shall provide an output signal to the Belt Filter Press Control panel in the event of polymer system failure. Control panel shall be designed to accept 120/208 V, 1 phase, 3 wire power supply. Rev. 6123109 PROJECT # 05734 11244 - Page 3 PART 3: EXECUTION 3.01 INSTALLATION A. All equipment shall be installed as shown on the drawings, and in strict accordance with the manufacturer's recommendations. 3.02 QUALITY CONTROL AND FIELD TESTING A. Quality Control: The polymer system manufacturer shall provide a trained service engineer for initial start-up, calibration and adjustment of equipment and instruction of plant personnel for one (1) eight hour day. The manufacturer shall, during the warranty period of one year, furnish all service necessary to repair defective equipment or work, and no charge will be made for any service due to these reasons. A complete written report shall be furnished to the Owner and' -Engineer after each service visit giving the reason for failure and recommendations to prevent recurrence. B. Field Testing: The Contractor shall demonstrate to the Owner and the Engineer that all equipment is operating as designed and specified. 3.03 SPARE PARTS A. The Contractor shall furnish one (1) complete set of manufacturer recommended spare parts and convey the spare parts to the Owner. END OF SECTION Rev. 6/23109 PROJECT # 05734 11244 - Page 4 SECTION 11315 PROGRESSIVE CAVITY SLUDGE PUMPS PART 1: GENERAL 1.01 SCOPE OF WORK A. This section shall include the furnishing and installing of electrically operated progressive cavity sludge pump with all accessories and appurtenances as specified herein and shown on the plans. All electrical appurtenances shall be furnished and installed in accordance with the Electrical Section of these specifications. B. Unless otherwise noted, all materials and equipment supplied under this Section shall be new, of good quality, and in good condition. 1.02 QUALITY ASSURANCE A. All equipment shall be supplied by reputable manufacturers with at least five (5) years of experience in the manufacture of progressive cavity sludge pumps. The manufacturer shall have at least five (5) successful installations of similar design, and shall submit evidence of experience if requested by the Engineer. 1.03 SUBMITTALS A. Shop Drawings: The Contractor shall submit six (6) sets of complete shop drawings, including performance curves, dimensions, catalogue cut sheets and materials of construction. B. Operation and Maintenance Manuals: The Contractor shall submit three (3) copies of operation and maintenance manuals to the Engineer. 1.04 DELIVERY STORAGE AND HANDLING A. All materials and equipment shall be delivered, stored and handled in strict accordance with the. manufacturer's recommendations. 1.05 WARRANTY A. All complete pumping units, including electric motors, auxiliary units, and mounts shall be warranted by the Contractor against all defects in materials and workmanship for a period of one (1) year from the date of final acceptance. The Contractor shall be obligated within one year at no cost to the Owner. Rev. 6123/09 PROJECT # 05734 11315 - Page 1 C. The performance of all pumps, motors and auxiliary units shall be guaranteed at the specified pumping conditions. 1.06 MANUFACTURER AND SUPPLIER INFORMATION A. Equipment shall be as manufactured by Monoflow Inc., Moyno Inc., Seepex Inc., or Tarby. Manufacturers are listed only to denote the quality standard of product desired, general style, type, character and do not restrict bidders to a specific manufacturer. Substitution of equipment of equivalent or equal design shall be submitted to the Engineer for approval or disapproval in accordance with Article 11 of the Instructions to Bidders. B. Manufacturer Nameplate: A manufacturer's nameplate shall be securely and permanently mounted to each individual piece of equipment furnished under this Section. The nameplate shall be constructed of a durable, non- corrosive material. Critical information shall be clearly engraved or otherwise permanently stamped on the nameplate, and shall be fully legible. The information contained on the manufacturer nameplate shall include at least the following: 1. Manufacturer's Serial Number 2. Name, address and telephone number of equipment manufacturer 3. Model and/or Part Number, including pump impeller sizes, when applicable 4. Performance Criteria (i.e., capacity, design point,, etc.) 5. Motor size, speed and voltage 6. Enclosure Type or Rating 7. Any other pertinent information Note: All equipment shall include a nameplate with a manufacturer serial number validating the equipment as new. Failure to meet these requirements will be cause for rejection of the equipment. B. Supplier and Service Information: A durable nameplate, stamp or sticker shall be adhered to each individual piece of equipment containing the name, address, and telephone number of the local business that supplied the equipment, and the name, address and telephone number of the local business that can provide service and replacement parts for the equipment. A 24-hour emergency service telephone number should also be included. Rev. 6/23/09 PROJECT # 05734 11315 - Page 2 PART 2: PRODUCTS 2.01 EQUIPMENT A. Pump Design and Construction: 1. The pump shall be capable of handling sludge generated from water and wastewater treatment plants, and sized to pump 25 - 100 gpm over a 50 PSI range at a maximum speed of 175 RPM. Maximum total dynamic head at the higher operating condition is 67 feet. 2. The pump shall be cradle mounted with the suction port capable of being rotated through a full 3600. The pump unit shall be provided with anti -rotation devices to prevent reverse rotation of the pump when stopped. The drive unit shall be standard integral electric motor direct connected into the pump unit. The complete pump and motor unit shall be steel base mounted with anchor bolts provided. 3. The pump shall be driven by a direct -connected variable speed 7.5 HP drive or gear reducer. Pump motor shall be TEFC inverter duty rated design for 480 volt service. A heat sensor thermostat shall be imbedded in top of winding and be connected in series with the motor starter coil in control box to stop motor if temperature rises in excess of the manufacturers recommendation for any reason. 4. The pump casing shall be of cast iron with all exposed nuts and bolts to be stainless steel. The pump shall be constructed such that a single helix rotor revolves eccentrically within a double helix stator of twice the pitch length so that the formed cavities progress toward the discharge end of the pump. The suction and discharge connections shall be standard flanged. The stator shall be compounded elastomers and the rotor chromium plated steel. The pump drive shaft shall be a machined steel, chromium -plated hollow shaft with a gear -type universal joint. The packing and stuffing box shall contain a packing gland and lantern ring with fittings for grease lubrication. 5. Progressive Cavity Sludge Pump shall be controlled by the Sludge Processing Area Control Panel (SPACP-550) via the Sludge Feed Control Panel (SFCP-550) over the fiber optic network. Refer to Division 13 and the system architecture plan for the composition of this system. Rev. 6/23/09 PROJECT # 05734 11315 - Page 3 PART 3: EXECUTION 3.01 INSTALLATION A. All equipment shall be installed as shown on the drawings and in strict accordance with the manufacturer's recommendations. 3.02 QUALITY CONTROL AND FIELD TESTING A. Quality Control: The manufacturer shall provide the services of a qualified field representative for one (1) 8-hour day to inspect the installation and provide start-up, field testing and operator training services. B. Field Testing: The pump(s) shall be field tested after proper installation. The field running tests shall be conducted by the Contractor and witnessed by the Engineer and shall demonstrate the following under all conditions of operation, insofar as the available flow will permit; that the unit has been properly installed and has no mechanical defects, that the unit is in proper alignment and has: been properly connected, that the unit is free from undue vibration over the full range of operating conditions, that the unit is free from overloading or overheating of any parts; that the unit is performing in accordance with the specifications. All power equipment, supplies, materials, labor, and instruments required for the field running tests shall be furnished by the Contractor. 3.03 SPARE PARTS 01 The Contractor shall furnish to the Owner one (1) complete set of manufacturer's recommended spare parts. The Contractor shall be responsible for furnishing any special tools and lubrication devices required to perform maintenance power unit. Three (3) copies of printed instructions other preventive maintenance operations shall be Engineer with the shop drawings. END OF SECTION or any pumping or for lubrication and furnished to the Rev. 6123/09 PROJECT # 05734 11315 - Page 4 SECTION 11365 PART 1: GENERAL 1.01 DESCRIPTION OF WORK SLUDGE DRYER SYSTEM A. Scope: The work to be performed under this item consists of furnishing and delivering one (1) complete sludge drying and conveying system as shown on the drawings and specified herein. All equipment shall be furnished by a single supplier. The system shall include all equipment and appurtenances required to produce a Class A material as defined by 40 CFR Part 503. B. Type: The sludge dryer system shall be a prefabricated unit consisting of a skid mounted dewatered sludge hopper, sludge dehydration chamber, hot oil heat exchanger fired by either liquid petroleum (LP) or natural gas, control panel, scrubber/condenser and required integral and external conveying devices. This dryer shall be an automated batch, indirect heated, sludge dehydration system. All equipment shall be mounted on skids for installation by the Contractor. C. Design Data: The indirect heated sludge dryer system shall be designed to operate in an automated batch process. The system shall have a design capacity to process 9.5 cubic yards of, wet sludge per batch, and 3,500 pounds per hour wet weight of municipal sludge that has been dewatered to 16% dry solids. 1.02 QUALITY ASSURANCE A. Standardization: All parts of the equipment shall be the product of one manufacturer experienced in the design and fabrication of automated batch biosolids dehydration systems. The manufacturer shall have constructed at least two (2) units of similar design. B. Coordination: The contract documents provide details of a complete equipment installation for the purpose specified. It shall be the responsibility of the Contractor to coordinate all the details required for a complete operating system, such as protective coatings, piping, pumps and wiring. The Contractor shall provide for all work required to properly install, adjust and place into operation a complete working system. C. Manufacturer's Quality Control: The manufacturer shall be responsible to assure compliance with all material and fabrication requirements of these specifications. Rev. 6123109 PROJECT # 05734 11365 - Page 1 1.03 0 1.04 SUBMITTALS The Supplier shall submit eight (8) copies of the following shop drawings to the Engineer for approval. 1. Complete outline dimension drawings, including front view, side view, arrangement, and interface points for piping, foundation, electrical and controls. 2. Complete electrical wiring and instrumentation diagrams and control panel layouts showing dimensions and power requirements at each and every connection. 3. The 'motor HP, RPM, WR2 value, motor dimensions, and any special/pertinent motor information. 4. Mounting details and foundation loads. 5. Complete diagrams of the variable speed drive(s), (if required). 6. Location, size and type of all bolts and welds, (if required). 7. Edge preparation of joints to be welded shall be detailed with shop and field welds distinguished, (if required). 8. Calculations and details for hold down lugs including foundation loads and anchor bolt uplift (if required). 9. Speed reducer information and ratings, (if required). 10. Any other auxiliary equipment information as well as performance information. 11. Weights of equipment. 12. Complete bill of materials (catalog number and rating of all devices). 13. Spare parts furnished by Manufacturer with equipment. 14. Spare parts recommended to be purchased by Owner for stock. 15. Source and current prices of replacement parts and supplies. 16. Original Manufacturer's part or model number of identification number. 17. Special storage or handling requirements. 18. Copies of operation and maintenance manuals for all equipment provided. 19. Calculations for determination of conveyor speeds. 20. Any other information required to obtain approval of the items included. 21. Copy of Process Guarantee and Performance Bond. PROCESS GUARANTEE The supplier of the sludge dryer equipment shall guarantee the performance of the equipment shall be such that a Class A biosolid is consistently produced that meets the regulatory definition of 40CFR 503 for a Class A product. The supplier shall furnish a performance guarantee secured by a Performance Bond issued by the supplier. The face value of the performance bond shall be equal to the cost of the equipment, including installation. The Bond shall remain in effect until completion of successful demonstration of the equipment. Rev. 6123/09 PROJECT # 05734 11365 - Page 2 1.05 FUNCTIONAL REQUIREMENTS A single supplier shall furnish the complete sludge dryer system and be responsible for its proper design and subsequent operation. The supplier shall be responsible for coordination with other portions of the project including structural, electrical and instrumentation, be the prime supplier of materials and equipment in the system, and provide all of the manufacturer's service as required for a complete and operable system. The Contractor shall perform all electrical work necessary to provide a complete and operable system based on the approved shop drawings and the Contract Drawings and Specifications. Contractor shall coordinate with the equipment manufacturer prior to bidding and during construction to determine scope of supply and installation requirements. The system shall be designed and furnished in accordance with all applicable codes and regulations. The sludge dryer equipment shall produce Class A sludge in accordance with 40CFR 503. Specifically, Class A pathogen reduction shall be met by reducing the moisture content of the sludge to 10% or lower. Additionally, either the temperature of the sludge particles shall exceed 80 degrees C (176 deg F), or the wet bulk temperature of the gas in contact with the sludge as the sludge leaves the dryer shall exceed 80 degrees C (176 deg F). Vector attraction reduction in accordance with 40CFR 503 shall also be accomplished by increasing the solids content of the sludge to 90% or greater. Compliance with 40CFR 503 Class A shall be verified at start-up. 1.06 PATENTS LICENSES AND ROYALTIES A. Patents: The supplier shall guarantee the Owner that all equipment offered under these specifications or that any process resulting from the use of such equipment in the manner stated, is not the subject of patent litigation, and that he is not knowingly offering equipment, the installation or use of which is likely to result in a. patent controversy, in which the Owner as user is likely to be made the defendant. B. Licenses and Royalties: Where patent infringements are likely to occur, the supplier shall submit with the prequalification submittal the license agreement between himself, or the manufacturer of the equipment, and the patent owner or the controller of the patent, which will permit the use in the specified manner of the equipment. In the event that the supplier is the controller or owner of the patent, the supplier shall submit, with the prequalification submittal, a license agreement to be executed by the supplier and the Owner. Any and all fees to be paid by the .Owner shall be clearly specified in the license agreement. Rev. 6/23/09 PROJECT # 05734 11365 - Page 3 C. Liability: The supplier shall submit a hold harmless agreement in which the supplier agrees to hold and save the Owner or its officers, agents, servants and employees harmless for liability of any nature or kind, including cost and expenses, for, or on account of, any patented or unpatented invention, process, article or appliance manufactured or used in the performance of the work under this contract, including the use of same by the Owner. 1.07 SHOP DRAWINGS The Contractor shall submit to the Engineer at eight (8) copies of shop drawings of all items listed in paragraph 1.03. Each submittal shall be clearly marked with the project name, dated and accompanied by a letter of transmittal listing all items included in the submittal and referencing the project specification page and article numbers applicable to each item. The equipment supplier has tested its system and has designed the equipment and selected the components; therefore, approval of shop drawings by the Engineer will be general only, and such approval will not relieve the supplier of responsibility for accuracy of such shop drawings, proper fitting, coordination, construction of work and furnishing materials and work required by the Contract, but not indicated on shop drawings. Approval of shop drawings shall not be construed as approving departures from any Contract requirements particularly the requirement for production of Class A product pursuant to 40CFR Part 503. 1.08 OPERATIONS AND MAINTENANCE MANUALS The equipment supplier shall furnish three (3) sets of O&M manuals for all the equipment provided. All equipment shall be warranted by the equipment supplier to be free from all defects in workmanship and material for a period of one year after the date of final acceptance. All defects that are detected during the, one-year warranty period shall be repaired by the equipment supplier at no cost to the Owner. PART 2: PRODUCTS 2.01 MANUFACTURING CODES AND SPECIFICATIONS A. Codes: The system shall comply with all applicable codes, including, but not limited to: • National Electrical Code (NEC) Rev. 6/23/09 PROJECT # 05734 11365 - Page 4 Plastic Piping Handbook AGE and IRI Gas System Specifications and Standards OSHA ASME B. Electrical 1. Control enclosure: Stainless steel, NEMA 4X, with UL stamp. 2. Machine wiring: Wired to National Electrical Codes. C. Gas Burner 1. Arranged and piped to Industrial Risk Insurer requirements. D. Steel Fabrications 1. All welds will be minimum 3/16 fillets. 2. All welds related to the inner heater coil and a minimum of 10% of the welds related to the outer heater coil shall be subjected to an x-ray inspection at the manufacturing facility. 3. The system will designed and manufactured for galvanizing and bolt up assembly under ASTM A143, A384 and A385. 4. The thermal oil system will be designed and "U" stamped according to the specifications of the ASME Sectioin VIII-Pressure Vessel Code for 750 degrees. F at 250 psig. The coils will be hydrotested per ASME. The expansion tank will be ASME Section VIII Code Stamped. E. Galvanizing 1. Steel fabrications specified to be galvanized will be hot dipped galvanized in accordance with ASTM A123-97. 2. Any defects or damage caused in manufacturing will be thoroughly cleaned, wire brushed, wiped clean with a suitable solvent and dried. The prepared area will be coated with a zinc rich compound specifically formulated for touch up of galvanizing. The zinc rich coating will be a minimum of 3.4 mills thick and will be in accordance with SSPC standards. F. Seals 1. The thermal fluid pump shall be manufactured by a major manufacturer of pumping equipment for heat transfer fluids. Seal specifications are: a. Stationary member- Silicon Carbide. b. Rotary member- Carbon. c. O-ring- Viton. d. Spring- CrNi steel. Rev. 6/23/09 PROJECT # 05734 11365 - Page 5 2. Thermal Fluid rotary seals: a. Seals are of stuffing box design; using carbon impregnated braided Teflon packing. 3. Dehydration Chamber end seals a. One (1) reinforced silicon gasket b. Multiple rings of carbon impregnated braided Teflon packing. G. Bearings 1. Bearings will be oil or grease lubricated, with lubrication points piped to a central lubrication block for accessibility. 2. Bearings shall be a minimum of L-10 rated life of 50,000 hours. H. Balance 1. Drive motors shall be manufactured by a major supplier of Premium Efficiency electric drive motors. Balancing specifications are to ISO 1940/73 Condenser Blower 1. The condenser blower shall be manufactured by a major manufacturer of blower units. Balancing specifications are to AMA 204, section 6, quality grade G2.5 standards. J. Thermal Fluid Heater Gas Burner 1. The oil heater gas burner shall be manufactured by a major manufacturer of industrial burner systems. Blower balancing specifications are to ISO 1940-73'. K. Equipment Guards 1. Equipment guards are designed for OSHA regulations and are 14 gauge hot rolled steel with expanded metal insert, where applicable, to allow visual inspection. All guards are designed for easy removal. 2. Guards shall be sand blasted to near white and painted with safety orange. 3. Chemical and fade resistant decals shall be affixed to the equipment where equipment may start automatically, have rotating parts or heat zones. Decals will be displayed in areas that are visually obvious. Decals are to be black print with yellow background. L. Hardware 1. Bolts shall be ASTM Class 449, Type 5 or greater. Rev. 6123/09 PROJECT # 05734 11365 - Page 6 2. Flanges, other than structural connections, shall be ANSI B16, class 150 type raised face, slip on weld. 3. Pipe threads shall be ANSI 11.5 V or 8V, depending on size. M. Couplings 1. Where couplings are used where the drive is greater then 1/2 hp, and where angular misalignment, parallel misalignment, end float and cushion shock or vibration dampening may need to be addressed, a flexible member with synthetic tension member bonded in rubber shall be provided. The flexible member shall be attached to the flanges by meads of clamps, rings and caps screws. The flanges shall be attached to the shaft by key seat and setscrews. N. Electrical 1. Contactors shall be Square D, Telemecanique, and Thermal Magnetic. Rated for 30 million operations. 2. Contactors shall be UL, ASE, and CSA approved. 3. Switches shall be 22 mm. 4. 9300 Rades Ethernet Modem 5. Allen Bradley Panel View Plus 1000 O. Gauges 1. Manufacturer to supply a water flow switch, natural gas test plugs, one magnehelic airflow gauge and one thermal fluid pressure switch. 2.02 EQUIPMENT A. Materials of Construction: (Note: All painted surfaces to be sand blasted to near white metal prior to painting) ITEM Structural Steel Main Skid MATERIALS 10" x 22# beam FINISH Galvanized Main Skid Floor 1/8 "floor plate Galvanized Hopper walls & ends 3/8" hot rolled steel Galvanized Hopper structural support steel 4" x 9.5 # beam Galvanized Hopper chain guard housing 12-ga hot rolled steel Orange paint Motor bases Dehydrator frame 1" plate 6" x 15# beams Galvanized Galvanized Dehydration chamber end plates Y2" plate Blasted & hi temp black paint Dehydration chamber 3/8" rolled steel Insulated and wrapped 18ga 304 S.S. Electro polish to #3 finish D- chamber crown and lid 10 ga 304 S.S. Hand polish Rev. 6/23109 PROJECT # 05734 11365 - Page 7 Steam exhaust duct 14 ga 304 S.S. Hi temp black paint Condenser 10 ga hot rolled steel Galvanized Hot oil combustion tank Base 18 ga 304 S.S. 3" x 4.1# channel N/A Galvanized Cover 10 ga hot rolled steel Black paint Combustion exhaust stack 14 ga 304 S.S. Black paint Hot oil expansion tank 3/16" thick hot rolled steel Black paint Support legs Product discharge head box 4" x %" angle 1/" hot rolled steel Galvanized Black paint Discharge screw conveyor body & cover 10 ga hot rolled steel Galvanized Condenser fan piping 6" dia. - .187" wall pipe Galvanized Hot oil piping Sch 40 - SA1O6B seamless pipe Insulated except valves and overflow/piping Chain hopper #140 roller chain w/ cotter ins N/A Dehydrator rotor #180 roller chain w/ cotter pins N/A/ Gear hopper Forged steel to meet ANSI Type II N/A Dehydration rotor Forged steel to meet ANSI Type II N/A Dehydrator 1/" S.S. tubing N/A Hopper 1/" S.S. tubing N/A Control Panel 40" w x 18" d x 84" h — NEMA 12 polished 304 S.S. N/A Electrical conduit Steel properly sized Galvanized J-Boxes Steel properly sized Galvanized Condenser water piping Drain pipe Gas piping Steel pipe/Buns-N hose & S.S. noz. 6" dia. x .187" wall pipe 2" dia. Sch. 40 black pipe Galvanized steel Galvanized I N/A B. Wet Sludge Conveying Equipment: Product conveying equipment shall be supplied by the sludge dryer equipment supplier in the general arrangement shown on the plans. The sludge dryer supplier shall provide the feed product screw conveyor to transport the feed stock to the dryer and to the outside of the building. The screw conveyors shall be shipped loose to be installed by the Contractor. The conveyor shall be suitable for transporting wet sludge at 14 to 18 percent dry solids. All materials of construction shall be suitable for contact with dewatered municipal sludge. The equipment supplier shall be responsible for determining conveyor speeds and shall submit calculations to document the determination. Rev. 6/23/09 PROJECT # 05734 11365 a Page 8 Cable operated OSHA safety stop switches shall be provided on both sides of each conveyor with pull cord along both sides of the full length. Each shall have a SPDT contact rated 5 amperes at 120 volts. A zero speed switch shall be provided on each conveyor, which will trip off the conveyor in a "jamming" condition. Each switch shall have a SPDT contact rated 5 amperes at 120 volts. Power supply to equipment will be 480 volts, 3 phase, 60 Hertz. All conveyor frames and supports will be constructed of ASTM-A-36 structural members with spreaders sized as required to limit deflection to 1/400 at longest support span. All necessary supports shall be provided by the Equipment Manufacturer. The top of the channel frame will be covered with a fiberglass reinforced plastic or aluminum return cover to prevent product spillage onto return run of belt. The entire frame assembly is to be hot dip galvanized after fabrication. Additional supports as required shall be designed and furnished by the conveyor manufacturer. All conveyors are to be provided with OSHA style guards at all "nip points" and motor driven rotating components, specifically including motor drive and tail pulley guards. The drive guard is to be constructed of FRP or aluminum. The conveyor manufacturer shall design and furnish all chutes between screw conveyors. Materials of construction for all chutes shall be minimum 3/16- inch 304 stainless steel, with external reinforcement as required. The equipment supplier shall provide all necessary equipment and appurtenances for a complete and operable system. All screw conveyors shall be constructed of carbon steel. Flights shall be full pitch and shall be minimum 3/16" thick, and shall be designed and sized by the manufacturer to for the specified carrying capacities. Troughs shall be "U" type, minimum 1/4 inch thick. Trough covers shall be 12 gauge minimum. The center pipe of the screw shall be sized so that intermediate hanger bearings are not required and deflection is 1 /4 inch or less. Tail bearings shall be grease lubricated flanged ball bearing. A plated type seal shall prevent sludge from passing the seal. Transfer chutes shall be flange connected to the screw conveyor and shall be minimum 12 gauge carbon steel. The screw conveyors shall be belt driven by a motor and speed reducer. Motors shall be sized by the equipment supplier. Each speed reducer shall have a service factor of 1.4 based on the calculated developed horsepower. Rev. 6/23/09 PROJECT # 05734 11365 - Page 9 The motor shall be connected to the speed reducer through a belt drive which is suitably covered with a 14 gauge OSHA approved guard. Motor starters and controls for the alkaline screw conveyors shall be provided as part of the biosolids processor main disconnect panel. C. Wet Sludge Feed Hopper: A. One (1), custom sludge feed hopper, fabricated from 3/8"thick mild steel with fifty (50) cubic yard holding capacity. Internals include two (2) mild steel rotary wiper mechanisms and two (2) 11" diameter mild steel augers. Externals include a chain and sprocket system to turn the rotary wiper and auger. Sprockets will be industrial quality to accept heavy- duty roller chains. Two (2) mild steel motor shelves will be properly designed and mounted to the hopper to support the drive motors and gearbox assembly. Chain guards are provided to comply with OSHA regulations. The hopper interior and exterior will be hot dip galvanized. One (1) custom 11" dia. Auger system installed between the feed hopper discharge and the dehydrator wet feed inlet complete with properly sized motor and gearbox. One (1) linear screw operated door installed in the feed port to act as an airlock. One (1) 9" dia. auger coupled to a Y2" hp drive is mounted on the hopper rim for automatic sludge leveling. D. Dehydration Unit: Each unit is designed, fabricated and supplied as follows: 1. One (1) structural steel frame designed and fabricated to support the dehydration chamber and motor drive package. All external steel surfaces will be finished per the Construction Materials and Finishes section. The cylindrical dehydration chamber is insulated with 2" high -density ceramic insulation and wrapped with an aluminum skin to prevent external heat loss. The inspection cover is left uninsulated. Dehydrator wet sludge feed port is equipped with an electrically operated shut off gate. Dehydrator top is furnished with two (2) 304 stainless steel inspection covers. Dehydrator crowned top is furnished with one (1) stainless steel exhaust duct, which is connected to the provided condenser system. 2. One dehydrator end is furnished with a linear screw actuated discharge gate. One (1) 3/8" steel dehydration chamber measuring approximately 72" dia. .x 144" long. The chamber has a smooth inner surface. One (1) thermal fluid external jacket integrally welded to the dehydration chamber for heat transfer to the dehydration chamber wall. One (1) 72" dia. thermal fluid type hollow disk / blender fabricated from 5/16" steel, complete with wall wipers. Two (2), rotary joints to provide thermal fluid inlet and outlet to the rotating disks. Two (2) '/z" thick steel plate ends enclose the dehydration chamber. 3. One (1) heavy-duty structural steel support base to support the dehydrator drive package. One (1) engineered dehydrator rotary disk drive package complete with reversible motor, gearbox, chain and bearings to drive the disks. One (1) dried sludge discharge system consisting of a linear screw Rev. 6123/09 PROJECT # 05734 11365 - Page 10 operated door and an enclosed auger drive package to convey the dried sludge to a discharge point on one side of the dehydration chamber. Multiple thermocouple probes for temperature readings and control including thermal fluid, exhaust, dehydration vapor, thermal fluid expansion tank and thermal fluid return from shell and rotor disks. E. Thermal Fluid System: One (1) custom natural gas fired thermal fluid heater fabricated from stainless steel and A36 steel, with a maximum rating of 8.25 Mbtus per hour. Internals of the air to thermal fluid heat exchanger are steel and designed for industrial use. The outer shell of the thermal fluid heater is 10-gauge stainless steel, with a chamber top constructed with A36 steel. The top section is painted with high temperature paint. The outer shell is insulated with 2" of high -density ceramic insulation. An industrial natural gas system will be supplied consisting of natural gas burners, control valves, temperature controls and piping. The natural gas system will conform to ASME CSD 1.The entire unit will be fabricated, assembled and tested before shipment. A thermal fluid expansion tank complete with a relief port is mounted in an elevated position. A special thermal fluid pump, filter, and valves will be furnished to circulate the thermal fluid through the dehydrator system. The combustion gasses will be collected in a 22" dia. duct, which will terminate above the unit. F. Natural Gas Burner: One (1) industrial natural gas system consisting of one (1) natural gas burner with modulating controls configured to meet ASME CSD 1. The system will be pre -piped and pre -mounted. The programmable controller will run various time / temperature recipes for total control of the dehydration process. Times and temperature regimes will be established during machine start-up and entered into the programmable controller. All necessary thermocouples and instrumentation are furnished in this proposal. The flue gasses are collected in a 22 dia. duct and terminated above the machine. Thermal fluid heater has an 8.25 Mbtus maximum firing rate. Actual natural gas usage will vary depending on the amount of actual water being evaporated however; since we must elevate the total load (solids and water) to 2120 F, the solids differential between applications does not significantly change the estimated cost of dehydration. G. Condenser/Scrubber: One (1) condenser/scrubber unit will be provided with the dehydration unit. The unit shall be connected to the plant re -use water system with a minimum of 140 gpm at 40 psi (not to exceed 45 psi). Pressure reducing valves and flow meters shall be supplied and installed by the General Contractor. Reuse water supplied to the Condenser/Scrubber will be filtered through 300-micron Y-Strainer (provided and installed by the Contractor) prior to connection to the Condenser/Scrubber system. The scrubber will be a high efficiency enclosed Venturi type to remove air borne particulate, and will be piped to the supplied Biofilter and carbon pack. The Rev. 6/23/09 PROJECT # 05734 11365 - Page 11 blow -down water will be piped to a drain where it will return to the head of the plant. H. Bio-Filter with Carbon Pack: One (1) 8'D x 9'8"H @ 500 CFM bio-filter package mounted on a 8' x 12' galvanized steel skid will be provided. The basic concept of biofiltration is to have odorous airflow through a media that supports biological active organisms. Organisms specific for the degradation of the specific odorous compounds accumulate on the media and multiply. Temperature, humidity, pH and nutrients are controlled to optimize the multiplication and effectiveness of these organisms. The warm 90 - 100 deg. F moist air is pulled through the scrubber/condenser system and piped to the bio-filter through 8" dia. CPVC pipe. The correct moisture level is maintained through the manual adjustment of a valve and tubing arrangement from the condenser water system. The heat is controlled by manually adjusting the water flow through the scrubber system. Once field set upon startup these adjustments are infrequently reset if conditions change. The bio-filters configuration of media trays are easily removed for media replacement or maintenance. Air flows into the bottom of the vessel and passes through the series of media and exits out the top. The bio-filter canister shall be manufactured of high quality, fiberglass. The segregated internal trays are made of fiberglass reinforced plastic grating, polypropylene media retention screen and tray supports. There will be a total of 300 cubic feet of organic, natural, fully biodegradable, non -synthetic composition. Malodorous compounds will be removed in the organic bio-filter media. The media will consist of three components, shredded wood (65%), nugget bark (25%), and compost (10%). The mixture shall have a pH between 6 and 8, an air -filled pore space of 25%-55% and moisture content of 40%. A carbon pack is added after the bio-filter. The carbon pack will filter foul air as it flows into the bottom of the linear PE canister. The foul air moves up through the inlet plenum, which diffuses the air and then up through the high capacity coconut shell carbon and potassium impregnated media bed where odorous compounds are removed by the active sties on the media. Dried Product Surge Bin: One (1) dried product surge bin shall be provided with the sludge dryer system, fabricated from 3/16" steel plate with a galvanized finish. 1. Capacity 86 cu. ft. 2. Cover with 2" FPT vent fitting. (Piped to dryer water-cooled condenser). Rev. 6/23109 PROJECT # 05734 11365 - Page 12 K. L 3. Discharge flanged outlet. 4. Two (2) Y2" FPT fittings for addition of spray nozzles. 5. One (1) 12" dia. access cover. 6. One (1) 10 hp motor drive package with gearbox. 7. One(1) dried biosolids eductor, for feeding dried biosolids to the storage silo. 8. Two (2) positive displacement blowers sized as necessary to move the dried biosolids from the dried product storage bin through the eductor to the storage silo. Control Panel: One (1) master control panel shall be provided to conform to National Electrical Code, specifications. The cabinet will be a NEMA 4X, stainless steel enclosure. An Allen Bradley SLC 5/05 programmable controller shall be provided, complete with internal timers to control the time/temperature regimes and all machine functions. Necessary 1/0 devices shall be furnished to operate the equipment safely and efficiently and to monitor and certify that the dried sludge meets the requirements for Class A sludge classification. One (1) main disconnect shall be provided in the enclosed cabinet. The panel shall be equipped with an Allen Bradley 9300 RADES Ethernet modem for connection to a designated phone line. Manufacturer will also supply ladder logic diagrams and initial cycle programming for one (1) time temperature dehydration cycle. All hard wiring schematics are furnished. Control Voltage: One 3 KVA step down transformer (120V/1 ph/60HZ) is furnished in the control panel General Operation PLC Controlled Automated Batch The master control panel shall be designed to accommodate the following general operation, or other operation as determined by the Sludge Dryer Manufacturer: i. The Sludge Dryer, under PLC control, is started to heat the thermal fluid to a system operating temperature. ii. The infeed hopper receives waste material from the belt filter press, with a storage capacity as specified previously. iii. The process temperature is raised to an optimum operating temperature as determined and specified by the sludge dryer manufacturer. iv. The PLC calls for dewatered biosolids to be fed to the drier chamber. 2. lnfeed airlock door opens. 3. lnfeed auger feeds biosolids to the drier chamber per level control. Rev. 6/23109 PROJECT # 05734 11365 - Page 13 4. The internal, oil heated, rotor moves and breaks up the biosolids to create maximum exposure to the heated surface of the rotor and the oil heated drier chamber. 5. The PLC senses the satisfaction of the time/temperature requirement of the dehydration process. 6. The discharge door opens, integral discharge and final product conveyors are activated, the rotor is changed to a one direction rotation to move the dried material to discharge. 7. When the discharge time is satisfied the discharge door is closed and the PLC resets to automatically infeed a new batch and start the process over. 8. This automatic batch process continues to cycle until the operator stops the sequence and sets the system to cool down cycle. M. Dried Solids Storage Silo: The Sludge Dryer System manufacturer shall provide a new dried solids storage silo with a minimum working capacity of 94 CY. Silo structure shall be designed for installation at the location shown on the plans and in accordance with all local codes and regulations. Silo shall consist of a welded carbon steel tank, 60 degree hopper with 12" diameter flanged outlet, with support and truck drive through 14' width and 13' vertical clearance. Tank shall include name plate, level indicator, thermocouple, 20" square flush mount tophat manway in hopper, 24" roof combination manway pressure relief valve, aluminum deck perimeter handrail, outside ladder with safety cage. and lockable hoop, full area working platform at 14' above grade, stairtower from grade to 14' above grade per drawings. System shall also include a separate baghouse sized for the proposed application. 2.03 MODULARIZATION A. All equipment in this proposal will be factory mounted on five (5) heavy-duty structural steel bases. 1. The main skid will include the dehydration chamber, the condenser/scrubber (including ductwork), and the electrical control panel with all motors and sensors wired to the panel. The ductwork with precooling and duct cleaning spray and the precooling manifold will be piped for one point connection. 2. The second skid includes the thermal fluid heat exchanger, the gas burner and gas valve train. 3. The third skid includes the wet sludge hopper and the wet sludge feed conveyor. 4. The fourth skid includes the biofilter, carbon pack, and the condenser blower. Rev. 6/23109 PROJECT # 05734 11365 - Page 14 PART 3 EXECUTION 3.01 INSTALLATION AND STARTUP SERVICES A. During installation and before the equipment is placed in operation, the equipment supplier shall inspect and certify that the unit and accessories have been properly installed and adjusted, all by a qualified properly trained representative at no additional cost to the Owner. Inspection shall consist of a minimum of three trips with 8 hours on site for each trip. B. The equipment supplier shall start up all equipment, supervise the initial operation thereof, and be responsible for the satisfactory operation of all equipment furnished under this Contract. The supplier shall allow a minimum of five days (40 hours) on site by the qualified properly trained representative for installation and start up. 3.02 TRAINING SERVICES A. The Supplier shall provide the services of a qualified properly trained representative to instruct the Owner's WWTP operators. The instructions shall include hands on operations of the proposed equipment and the furnishing of any and all technical guides that are required. At least twenty four (24) hours of instruction during two (2) trips shall be provided and shall be coordinated with the start-up of the other sludge processing equipment. B. Furnish for the Engineer's approval six (6) sets of instructions for the job which shall fully instruct the employees of the Owner in correct practice and method of operations and maintenance of equipment furnished. 3.03 TESTING A. Acceptance Test: After all equipment has been placed in service, a performance test will be conducted over a two day period. The Equipment Supplier shall furnish all instruments, meters, gauges, recorders and any other devices necessary to verify that the equipment meets the performance specifications. In the event the equipment fails to meet the performance requirements described in these Specifications, the equipment supplier will have 30 days to modify said equipment and complete additional tests to demonstrate the ability of the equipment to meet these Specifications. After said modifications have been made, a second performance test will be conducted over a two day period. The performance test run shall be for a period of two (2) eight hour working days with data from the final day of testing used to determine compliance. Delays due to inclement weather or auxiliary equipment malfunction shall be Rev. 6/23/09 PROJECT # 05734 11365 - Page 15 excluded as determined by the Engineer. All sampling and sample testing during the one day certification run shall be performed at the expense of the supplier by an independent laboratory approved by the Owner. Samples shall be taken before and after each batch, for a minimum of two batches. Each sample shall be analyzed as required by 40CFR 503 for the pathogen reduction and the vector attraction reduction method used. In addition, sampling to determine the throughput in pounds of sludge per hour shall be conducted. Each sample shall meet the requirements of 40CFR 503 for a Class A product. B. Failure of Equipment to Meet Performance Requirements: If the equipment supplier is unable to meet the performance requirements within 60 days of start up of the equipment, the equipment supplier shall, at no cost to the Owner, remove all equipment from the job site and refund to the Owner the full amount paid. The manufacturer shall also refund the installation cost for their equipment including all labor, and materials that are not utilized by subsequent equipment installed by the Owner 3.04 SPARE AND REPLACEMENT PARTS A. Replacement Parts: The equipment supplier shall furnish all replacement parts for a period of one (1) calendar year after the end of the one year warranty period. These parts shall include defective parts, parts that fail due to normal wear including consumable parts, and parts that render the machines ineffective due to wear. These will be installed by the Owner at no cost to the supplier. B. Spare Parts to be Furnished: The equipment supplier shall furnish one set of recommended spare parts. At a minimum, the spare parts to be provided shall consist of the following: 1 — Proximity Switch 1 — Rotary Union Packing Gland 1 — Chamber Packing Gland 1 — Solenoid Valve 1 — Dual Lead Thermocouple 1 — Single Lead Thermocouple 1 — Input / Output Card for the PLC Controller. END OF SECTION Rev. 6/23109 PROJECT # 05734 11365 - Page 16 SECTION 11376 POSITIVE DISPLACEMENT BLOWER PART 1: GENERAL 1.01 SCOPE OF WORK A. Furnish all labor, equipment, materials and incidentals required to completely install and place into operation three (3) prefabricated positive displacement blower packages at the locations shown on the drawings. B. Unless otherwise noted, all materials and equipment supplied under this Section shall be new, of good quality, and in good condition. 1.02 SYSTEM DESCRIPTION A. Blowers: 1. Post Aeration Basin: Three blowers, 154 SCFM @ 4 PSI, 5HP max 2. Existing Sludge Holding Basin: Two blowers, 1145 SCFM @ 10 PSI, 100 HP max 3. Proposed Sludge Holding Basin: Two blowers, 1375 SCFM @ 10.5 PSI, 100 HP max B. Each system shall be furnished and installed with all necessary accessory equipment and appurtenances, whether specifically mentioned in these specifications or not. Each unit shall be prefabricated and shall include the positive displacement blower, drive system, drive motor, inlet filters, inlet silencers, combination base/discharge silencer/relief valve, and expansion joint. C. Existing Sludge Holding Basin and Proposed Sludge Holding Basin blowers shall be identical models with the exception of the blower speed. 1.03 QUALITY ASSURANCE A. General: All blowers shall be given the following factory tests: 1. Standard factory slip test: Standard factory slip RPM test at one (1) psig pressure. This slip RPM (uncorrected) must meet the maximum 1 psig factory slip Rev. 6/23/09 PROJECT # 05734 11376 - Page 1 RPM specified for the frame blower tested. The test consists of blocking off the discharge and measuring the speed of the blower to maintain discharge pressure of 1 psig. 2. Certified Performance Test: For all blowers of 30 hp and larger, a performance test in accordance with ASME PTC-9 (latest revision) shall be conducted on each blower to be supplied. A test report confirming capacity and power will be furnished to the Engineer. 1.04 SUBMITTALS A. Shop Drawings: Shop Drawings for the equipment to be furnished under this specification shall include at least the following: 1. Descriptive literature, bulletins, catalog cuts and drawings for the equipment and accessories. 2. Complete bill of materials. 3. Performance curves for each type of blower. 4. Certified performance curves for each blower prior to shipment of the blowers. 5. List of spare parts. 6. Warranty. B. Operation and Maintenance Manuals: The Manufacturer shall furnish at least three (3) copies of operation and maintenance manuals for all equipment supplied. 1.05 DELIVERY, STORAGE AND HANDLING A. No shipment shall be made until the equipment and the certified performance curves have been approved by the Engineer. B. All equipment shall be properly protected so that no damage or deterioration will occur during shipment or storage. C. All equipment and ports shall be properly protected from damage and deterioration during storage at the site. 1.06 WARRANTY A. All equipment shall be warranted to be free from defects in workmanship, design and materials for a period of one (1) year under normal use, Rev. 6123/09 PROJECT # 05734 11376 - Page 2 operation and service. Should any part of the equipment fail during the one (1) year warranty period, it shall be replaced and the unit restored to service at no expense to the Owner. 1.07. MANUFACTURER AND SUPPLIER INFORMATION A. Equipment shall be as manufactured by Dresser Roots, Inc., Gardner Denver Sutorbuilt, Hibon Inc., Kaeser Compressors, Inc. Tuthill Vacuum and Blower Systems, United Blower Inc. Manufacturers are listed only to denote the quality standard of product desired, general style, type, character and do not restrict bidders to a specific manufacturer. Substitution of equipment of equivalent or equal design shall be submitted to the Engineer for approval or disapproval in accordance with Article 11 of the Instructions to Bidders. B. Manufacturer Nameplate: A manufacturer's nameplate shall be securely and permanently mounted to each individual piece of equipment furnished under this Section. The nameplate shall be constructed of a durable, non- corrosive material. Critical information shall be clearly engraved or otherwise permanently stamped on the nameplate, and shall be fully legible. The information contained on the manufacturer nameplate shall include at least the following: 1. Manufacturer's Serial Number 2. Name, address and telephone number of equipment manufacturer 3. Model and/or Part Number, including impeller sizes, when applicable 4. Performance Criteria (i.e., capacity, design point, etc.) 5. Motor size, speed and voltage 6. Enclosure Type or Rating 7. Any other pertinent information Note: All equipment shall include a nameplate with a manufacturer serial number validating the equipment as new. Failure to meet these requirements will be cause for rejection of the equipment. B. Supplier and Service Information: A durable nameplate, stamp or sticker shall be adhered to each individual piece of equipment containing the name, address, and telephone number of the local business that supplied the equipment, and the name, address and telephone number of the local business that can provide service and replacement parts for the equipment. A 24-hour emergency service telephone number should also be included. Rev. 6/23/09 PROJECT # 05734 11376 - Page 3 PART 2: PRODUCTS 2.01 EQUIPMENT A. Blowers: General: The air blowers shall be of the rotary positive displacement type, and shall be constructed with inlet and discharge connections oriented as shown on the contract drawings. Each blower shall be equipped with steel mounting feet. Maximum blower speed shall be 3,000 rpm. 2. Casing: One-piece close -grained cast iron. 3. Impellers: High -strength cast iron, straight, tri-lobe involute type. The impellers shall operate without rubbing or liquid seals or lubrication. The impellers shall be dynamically balanced and center -timed to permit rotation in either direction. 4. Shafts: Alloy steel, pressed into the impeller body and pinned. 5. Impeller/Shaft Assemblies: Each impeller and shaft assembly shall be supported by oversized anti -friction bearings engineered for long service life and fixed to control the axial location of the impeller/shaft unit. A cylindrical roller bearing shall be provided at the drive shaft designed to handle the stresses of V-belt drive, while single -row ball bearings shall be used at all other locations. 6. Timinq Gears: The impellers shall be timed by a pair of carbolized and ground steel spur gears, mounted on the shafts with a tapered fit, and secured by a locknut. 7. Lubrication: Each bearing shall be provided with a positive lip -type oil seal designed to prevent lubricants from entering the air stream. Further provisions shall be made to vent the impeller side of the oil seal to atmosphere to eliminate any possible carry-over of lubricant into the air stream. The drive end bearings shall be grease lubricated, and shall be provided with grease fittings. The timing gears and the gear and bearings shall be lubricated by splash from the gears dipping into the oil. B. Drive System: V-belt drive with weatherproof guard meeting all applicable Federal, State and Local health and safety requirements. C. Drive Motor: Motors shall be 480 V, 60 Hz, 3 phase, totally enclosed fan cooled (TEFC) with a 1.15 service factors, and shall be non -overloading at Rev. 6123109 PROJECT # 05734 11376 - Page 4 the design conditions specified. A heat sensor thermostat shall be imbedded in top of winding and be connected in series with the motor starter coil in control box to stop motor if temperature rises 'in excess of the manufacturers recommendation for any reason. Pressure Switches shall be provided on the discharge of each blower. Refer to Specification Section 13420 for information regarding this device. D. Inlet Filter: The inlet filter shall have a weatherhood mounted upright for maximum watershed with capacity equal to or greater than design conditions, and shall include air filter restriction gauge to measure pressure drop across the filter element. Inlet filter shall be as manufactured by Universal Silencers, Division of Nelson Industries, Inc., or equal. E. Inlet Silencers: Horizontal arrangement, carbon steel plate, rigidly connected to the blower suction, multi -chamber design with internal tubing and porting. Silencers shall be a standard grade silencer as manufactured by Universal Silencer or equal. F. Combination Base/Discharge Silencer/Relief Valve: The discharge silencer shall be of horizontal arrangement connected to the blower discharge by a reinforced silicone rubber flexible connector to isolate the blower from thermal related stresses. The silencer shall be of carbon steel plate with two (2) shell layers, multi -chamber design with internal tubing and porting. The silencer shall be welded to a heavy steel machinery base with anti -vibration welded reinforcements. The silencer shall be Model RD as manufactured by Universal Silencer or equal. Bolted construction is not acceptable. Fork lift access shall be provided and identified by prominent markers. The relief valves shall be mounted on the exit chamber of the silencer, and shall be as manufactured by Roots, or equal. G. Noise Enclosure: An 80 dBA or less free field guaranteed noise enclosure should be provided for each blower system. The enclosure outer material must be zinc coated steel with a surface preparation and paint as follows: Powder coat with texture finish 40-100 microns (65 microns average) powder coat process to be proven to- pass 500 hour salt spray test satisfactory with no rust evidence. The enclosure must be suitable for outdoor installation, 20 lb per square foot snow load and 90 MPH wind speed. The enclosure shall include a vent system with cooling fan and (3) removable panels for easy access and maintenance. The noise enclosure shall be provided with min. 1" foam and the foam shall comply with UL94-HF 1 for flammability. The noise enclosure shall provide up to 22-dba attenuation, free field. Rev. 6/23/09 PROJECT # 05734 11376 - Page 5 PANT 3: EXECUTION 3.01 INSTALLATION A. Installation of the equipment shall be in strict accordance with the manufacturer's instructions and recommendations. 3.02 QUALITY CONTROL AND FIELD TESTING A. Quality Control: The equipment manufacturer shall provide the services of a qualified service engineer for one (1) day to inspect the installation of the equipment and provide operation and maintenance training. B. Field Testing: The equipment manufacturer representative will also verify the performance of the blowers during the inspection, including air flow and pressure, and shall demonstrate to the Owner and the Engineer that the equipment is operating as specified. END OF SECTION Rev. 6/23109 PROJECT # 05734 11376 - Page 6