Landfill Leachate PFAS Wastewater Management - DPW

Page 1 of 8 PURCHASING DIVISION Joni Laming, Manager (616) 632-7720 purchasing@kentcountymi.gov SOLICITATION Solicitation Type Request for Proposal (RFP) Solicitation Number 5637 Description Landfill Leachate PFAS Wastewater Management Date of Issuance 4/3/2024 Inquiries Deadline Date & Time (local) 5/2/2024, 2 PM Due Date & Time (local) 5/7/2024, 2 PM Pre-Submission Conference Yes: Mandatory Teleconference (attendance & pre- registration required) Conference Date & Time (local) 4/16/2024 9:00 AM Buyer Name Underhill INTRODUCTION The Kent County Purchasing Division is soliciting proposals from qualified environmental or engineering consulting firms, contractors, equipment manufacturers, and suppliers to provide per- and polyfluoroalkyl substances (PFAS) wastewater pretreatment at landfill sites operated or managed by the Kent County Department of Public Works (KCDPW). Proposals would be for the design and installation of

pretreatment system(s) and/or leachate management services for landfill leachate to meet federal, state, and local discharge limits for PFAS prior to discharge to a municipal wastewater treatment system or alternate offsite treatment/disposal. Kent County reserves the right to award by landfill project location or in total. PRE-SUBMISSION TELECONFERENCE A pre-submission conference is scheduled for this Solicitation. Conference registration is located here. Registration closes hour before the conference scheduled date and time. Attendee should join the conference a minimum of 5 minutes before the conference is scheduled to commence. Late attendees will not be admitted. The conference provides attendees equal opportunity to seek clarifications regarding this Solicitation. Failure to attend the pre-submission conference may result in rejection of non-attendee inquiries. Each Respondent will be given the opportunity to ask questions and is responsible for taking meeting notes. One person from the Respondent should be designated to ask questions when prompted by the meeting host for teleconference meetings. All additional attendees should remain muted. Attendees must fully review all Solicitation documents and correspondence prior to the conference. Attendee shall be an employee or authorized reseller of the Respondent with requisite knowledge, skills, and abilities to participate. Revised 4/24/24 xxxxxxxx May 23, 2024, 2pmxxxxx xxxxxxxxxxxxxxxx May 30, 2024, 2pm Kent _]| County https://www.accesskent.com/RFPWorkbench/LoadPublicTableAction.action Page 2 of 8 Attendee assumes all risks, costs, and expenses, including technological difficulties, associated with meeting attendance. Attendee may not screenshot or record any part of the meeting including the audio. An attendee requiring special services is asked to provide requirements to the Kent County Purchasing Division at least 48 hours in advance to allow for accommodations. SCOPE KCDPW provides solid waste management services and education programs to Kent and surrounding counties. Established by the Kent County Board of Commissioners and overseen by the Board of Public Works, the Department has provided solid waste management solutions for Kent Countys municipalities, businesses, and residents since the late 1960s that require ongoing environmental monitoring, treatment and remediation to ensure the protection of public health and local ecology. Due to PFAS-containing materials releasing mobile, aqueous PFAS to landfill leachate, the U.S. Environmental Protection Agency (EPA) and the Michigan Department of Environment, Great Lakes, and Energy (EGLE) have established PFAS limits applied to drinking water, surface water, groundwater, and wastewater requiring PFAS removal in landfill leachate prior to discharge to POTW at several sites managed by Kent County. Proposals may include pretreatment systems such as foam fractionation, sorptive media including granular activated carbon or ion exchange resins, electrochemical oxidation, ultraviolet, plasma or any other field proven leachate effluent PFAS removal/destruction technology, paired with a destruction technology, if required, such as hydrothermal alkaline treatment or supercritical water oxidation. Respondents may also propose any combination of services that would remove the need to discharge leachate directly to publicly-owned treatment works (POTW), including cementitious solidification/stabilization, equalization and hauling of total leachate volume, or foamate, for offsite treatment and disposal or pumping and piping directly to offsite treatment and disposal. Proposals are being accepted to provide treatment technology and/or services on a rental, throughput, or a total purchase basis to be incorporated into pretreatment processes at four sites to achieve regulatory compliance for four leachate discharges and two surface water discharges, each with varying PFAS loading and discharge volumes. KCDPW is not seeking externally sourced routine treatment system operations or maintenance personnel as it has the staffing capacity and experience to operate remediation systems internally. Analytical laboratory testing and flow data have been compiled and are available for all leachate discharges, see Table 1. With POTWs setting enforceable PFAS limits, the target concentrations are for PFOS, PFOA and PFBS, but no other parameters or criteria at this time. KCDPW is seeking technologies that treat leachate and surface water discharges to the individual PFAS parameter limits outlined in Table 1, given respective influent concentrations. KCDPW is seeking to begin necessary construction and/or modifying existing pretreatment building equipment and processes in 2024 based on a chosen treatment strategy to achieve discharge compliance in 2025. Respondents should layout an expected timeline and scope of completion. Consultants, equipment suppliers, and vendors are to provide background and experience regarding previous work on environmental service and wastewater treatment projects and highlight any previous PFAS treatment of landfill leachate. Page 3 of 8 SITE INFORMATION South Kent Landfill, 10300 South Kent Dr. SW, Byron Center, MI 49315 South Kent Landfill (SKL) is and active landfill located in Byron Center, Michigan, with expected closure within the next 10 years. This site has two leachate discharges requiring PFAS management; Municipal Solid Waste (MSW) leachate, and leachate generated from a separate ash monofill containing MSW incinerator ash generated at the Kent County Waste to Energy Facility. The MSW leachate generated at South Kent Landfill gravity flows through subsurface piping to the Byron Gaines Water Authority public sewer connection on the west side of the site, where it then flows to the City of Wyoming Clean Water Plant. The ash leachate is collected in a 34,500-gallon above ground holding tank near the ash monofill, where ash leachate is then hauled to the City of Wyoming Clean Water Plant via tanker truck as needed. Analytical PFAS and flow data for these discharges is available in Table 1. Additional parameters, with analyses isolating the historic cells 1-10 and more modern cells 11-42 is available in Table 2. A site drawing is available in Appendix A. Details on the above ground holding tank is available in Appendix B. Kentwood Landfill, 4980 Breton Rd. SE, Kentwood, MI 49512 Kentwood Landfill (KWL) is a closed Superfund landfill located in Kentwood, Michigan, with a single effluent leachate discharge. Leachate is collected onsite via pneumatic pumps which gravity flows to a central lift station before being pumped to an existing leachate pretreatment building onsite. Many of the historic pretreatment processes are no longer in use due to decreases in traditional contaminant concentrations. With pretreatment ceasing over a decade ago, it is expected that many of the historic components may be in need of some repair if they were to be incorporated into new novel treatment processes. Analytical PFAS and flow data for this discharge is available in Table 1. Site drawings are available in Appendix C and D. North Kent Landfill, 2908 10 Mile Rd. NE, Rockford, MI 49341 North Kent Landfill (NKL) is a closed landfill located in Plainfield Township, near Rockford, Michigan. This site has two wastewater management requirements; leachate from MSW landfill cells, and groundwater collected below the landfill liner in an underdrain system. Due to the nature of the underdrain groundwater, this source contrasts the other leachate discharges in that it represents a large volume of minimally impacted groundwater. KCDPW has been successfully treating leachate at NKL with a combined granular activated carbon and ion exchange system; however, due to the ongoing expense associated with this method applied to landfill leachate, KCDPW is considering alternate leachate management options. The pretreatment building constructed to house the existing leachate pretreatment system has planned space available for underdrain groundwater processes. Currently, underdrain groundwater is conveyed to two separate aeration ponds onsite prior to discharge. A tentative phase two project of the current pretreatment system has been designed, combining the two underdrain discharges and redirecting the combined flow to the existing pretreatment building prior surface water discharge. That design, while not required to be followed through for this work, is available in Appendix E. Analytical PFAS and flow data for these discharges is available in Table 1. Site drawings are available in Appendix F and G. Page 4 of 8 Waste to Energy Facility, 950 Market Ave. SW, Grand Rapids, MI 49503 The Waste to Energy Facility (WTE) incinerates non-hazardous solid wastes from municipal and commercial operations generating electricity. Located in Grand Rapids, Michigan. This site has one wastewater discharge requiring PFAS remediation, water that has come into contact waste. Due to the nature of the contact water, this source contrasts the other leachate discharges in that it has a large volume of minimally impacted water. KCDPW has been successfully treating contact water at WTE with a batch operated granular activated carbon system; however, KCDPW is considering alternate contact water management options. Analytical PFAS and flow data for this discharge is available in Table 1. The Kent County Standard Submission Terms posted on the Bid Opportunities page of the Kent County Purchasing Division website are incorporated by reference and shall be deemed to have the same force and effect as if fully set forth herein. INQUIRIES Any and all communication regarding this Solicitation shall be on the Kent County Purchasing Division Inquiry Blog via the Bid Opportunities page or during pre-proposal meetings. Kent County reserves the right to determine the response format or not respond, at its sole discretion. BID BOND No Bid Bond is required if Respondents offer is less than $500,000. If the offer is withdrawn after Solicitation opening, Respondent may be removed from the Bidder's List (Vendor Registration) pursuant to Kent County Purchasing Central Purchasing and Open Market Procedures for Goods and Services section D.13 Failure to Perform Satisfactory. Each offer over $500,000 must be accompanied by a Bid Bond executed by the Respondent and payable to County of Kent for 5% of the total amount of the offer. Attorneys-in-fact who sign Bid Bonds, Payment Bonds or Performance Bonds must file a certified dated copy of their Power of Attorney. A certified check, bank draft, cashier's check, or negotiable U.S. Government bond (at par value) may be submitted In lieu of a Bid Bond. Personal checks are NOT acceptable. If requested, the Original Bid Bond must be received by the Kent County Purchasing Division within 2 business days of request. Bid Bonds of unsuccessful Respondents will be returned after the Solicitation is awarded. The Bid Bond of the successful Respondent will be retained until the contract is fully executed by all parties involved. PERFORMANCE AND PAYMENT BOND Each contract over $50,000 must be accompanied by a Performance Bond and a Payment Bond, each payable to the Owner (County of Kent) and each in the amount of 100% of the contract price with a corporate surety approved by the funding agency, for the faithful performance of the contract. REQUEST FOR PROPOSAL SUBMISSION Complete submissions must be received in the Kent County Purchasing Division on or before the due date/time specified by the designated clock (local time). Late, faxed, or emailed submissions will NOT be considered. https://www.accesskent.com/RFPWorkbench/LoadPublicTableAction.action https://www.accesskent.com/RFPWorkbench/LoadPublicTableAction.action https://www.accesskent.com/Departments/Purchasing/vendor.htm https://www.accesskent.com/Departments/Purchasing/vendor.htm Page 5 of 8 Submissions may be submitted electronically on the Bid Opportunities page of the Kent County Purchasing Division's website. Respondent must include a complete proposal as 1 non-password protected PDF document. The time required to upload a submission may vary. Respondent assumes all risks associated with electronic submission, including technological difficulties, and deems the County and its service provider harmless and without fault. Successful electronic submissions are confirmed via Respondent's email. Respondent shall view the link in the confirmation email to determine accuracy prior to due date/time. Submissions must be in the format outlined below: Business Organization One (1) page maximum State the full names, addresses, phone numbers, emails, and websites of any parties and their prospective roles. Recommendation Ten (10) pages maximum Provide a recommendation focusing on the technical specification. Emphasize clarity and detail. The description of respondents proposed wastewater management process should fully detail the type of PFAS removal technology or process/service being proposed, including the methodology, proposed throughput, inputs and outputs. Explain the decision-making process for proposed wastewater management at each site. The description may include, for example, a process flow diagram, equipment arrangement, mass balance, and system performance data. Respondents should outline the material discharge which their technology or process targets. Descriptions should include ideal source wastewater, contaminant concentration and volume/flow of wastewater with ability to handle changes in properties due to seasonal fluctuations in leachate discharge volume. Treatment performance limitations related to additional wastewater co- contaminants should be specified, along with any additional remedial benefit gained through the pretreatment process, for example, removal of ammonia. If applicable, the need for interconnecting with utilities should be identified, such as electrical phase or voltage requirements. Infrastructure prerequisites such as the need for systems to be housed in a heated building, or placed on a concrete pad, for example, should be outlined. Any unique or outstanding feature of the technology should be presented, along with a description of the products produced, the types of air emissions, any pre-processing of leachate required prior to its introduction to the technology such as solids removal, and the potential need for any ongoing amendments or surfactants. The amount of building space needed to house treatment system components should be specified. The approximate capital investment required to develop, design, construct and commission the systems should be provided. The approximate operation and maintenance costs should be specified, including expected energy usage, media changeout, expected operator preventative maintenance, expected ongoing surfactant expenses, and so on. For purposes of bid comparison between a variety of potential solutions, provide an anticipated cost on a per gallon treated basis. The material presented should be descriptive only, any calculations, formulae, academic papers, articles, test results, press releases or other supporting material should be referenced and included in the supporting material section described below. Page 6 of 8 Risk Allocation Without disclosing confidential or proprietary information, respondents should describe their business model and the allocation of risk associated with their technology. As a public-sector entity, KCDPW is seeking demonstrated and commercially scaled projects with low technical, management or financial risk. Respondents should describe how their technology will be designed, planned, permitted, constructed, and tested. Additionally, provide conservative estimates with assumptions made related to the expected timeline associated with design, construction, and start up. Given the potential for PFAS to be a classified by the USEPA as a hazardous material, provide an explanation as to how this change in classification would affect the proposed methodology or supporting services, particularly associated with the transport of concentrated liquids or other waste and the associated impact on long-term O&M costs. Experience and Qualifications The purpose of this section is to provide the County with an overview description of the respondents organization and the respondents current and prior experience in applying its technology or services to wastewater pretreatment and environmental remediation. The respondent should: Summarize the organization of the company, a brief business history, current principal place of business, size, number and types of employees, and any other relevant organizational information. If the respondent Team includes other organizations (e.g., major technology providers, joint venture partners, subcontractors, etc.), such information should be provided for each respondent team organization. For proposers using commercially proven technologies, present the respondents experience record in applying the technology, including the location, magnitude (gallons/day, gallons/year, etc.), operating history and performance characteristics such as PFAS removal efficiency of a least one reference facility treating landfill leachate. For a technology to be considered as commercially proven, it must have at least one reference facility of a size at least 50 percent (50%) of that being offered and have continued successful operation. For each commercially proven reference facility, respondent should describe: o The nature of its involvement with the installation, o The name of the owner and/or host of the facility, if not the respondent, o The length of time that the facility has been in operation, including the start date and end date (if no longer in operation), and if not currently operating, the reason for the cessation. If an installation cited is not the respondents, then the respondent should identify the entity that developed that installation and the relationship of that entity to the respondent. o The project cost and any obstacles encountered during construction or implementation. For proposers of commercially demonstrated technologies, present the respondents experience in applying the technology, including the location, magnitude (gallons/day, gallons/year, etc.), operating history and performance characteristics such as PFAS removal efficiency of a least one reference or demonstration facility, treating landfill Page 7 of 8 leachate. For a technology to be considered as commercially demonstrated, it must have at least one reference site of a size at least 10 percent (10%) of that being proposed. For each reference or demonstration facility, respondents should describe: o The nature of its involvement with the installation, o The name of the owner and/or host of the facility, if not the respondent, o The length of time that the facility has been in operation, including the start date and end date (if no longer in operation), and if not currently operating, the reason for the cessation. If an installation cited is not the respondents, then the respondent should identify the entity that developed that installation and the relationship of that entity to the respondent. o The project cost and any obstacles encountered during construction or implementation. Timeline & Expectations Two (2) pages maximum Provide a timeline to implement the recommendation efficiently and effectively with emphasis on key deliverables and milestones. Disclose necessary County resources, staffing and/or other requirements to implement each phase of the recommendation. Pricing Methodology Two (2) pages maximum Provide a detailed pricing methodology for an all-inclusive, implemented recommendation including payment terms, unit costs, billable costs, and all other expenses, such as KCDPW purchasing, leasing, or being billed related to treated throughput. Reserving the right for all possible outcomes following this RFP, KCDPW could enter into a service agreement that embodies the proposed business relationship between the County and the respondent(s). Project Staffing One (1) page maximum plus resumes Provide a chart with the staff committed to the recommendation. Show lines of authority and provide a brief role description with responsibilities as they relate to the recommendation. For each individual, include a resume or description of his/her education and professional experience. Include phone number(s), email address(s) and respondents website address. If applicable, list the branch office, consultants, or other subordinate elements that will provide or assist in providing the service. References One (1) page maximum Provide 3 relevant references, preferably for projects of similar scope and complexity. Include the organization, contact person, current telephone number, email address, description, and dates of service and total cost. Do not include any current/past Kent County employees as a reference. Supporting Material, if needed Calculations, formulae, academic papers, articles, test results, press releases or other supporting material Contract - Unlimited Provide any contract and/or applicable agreements Kent County may be asked to sign, as well as the incorporation of economic and operational terms that have yet to be identified, such as the length of the initial service agreement term and proposed extensions, indicative pricing for treatment throughput, etc. Kent County reserves the right to present its own contract. Page 8 of 8 Page number maximums are strongly recommended but not compulsorily disqualifying. Kent County is not liable for costs incurred prior to award. A submission constitutes an irrevocable offer for a period of 45 days from the due date/time. In the event the notification of award is not made within 45 days from the due date/time, the Respondent may withdraw or provide a written extension of their submission. Submissions may only be withdrawn by written request if the request is received before the due date/time. Withdrawals after opening shall be subject to Kent County Fiscal Policy Centralized Purchasing 5(i)(2). NO BID Please provide feedback if you are electing not to participate in this Solicitation. https://www.accesskent.com/Departments/Purchasing/vendor.htm https://www.accesskent.com/Departments/Purchasing/vendor.htm https://forms.office.com/g/PSALYQZm1Z RIM: OUTLET INVERT: 793.99 783.54RIM: OUTLET INVERT: 792.99 783.18 RIM: OUTLET INVERT: 794.09 782.45 RIM: OUTLET INVERT: 786.08 776.7 RIM: OUTLET INVERT: 787.83 774.25 RIM: OUTLET INVERT: 778.08 764.45 RIM: OUTLET INVERT: 761 754.6RIM: OUTLET INVERT: 768.1 752.77 RIM: OUTLET INVERT: 760.12 749.9 RIM: OUTLET INVERT: 756.6 749.2 RIM: OUTLET INVERT: 754.95 749.05 RIM: OUTLET INVERT: 755 748.74 RIM: OUTLET INVERT: 757 747.75 RIM: OUTLET INVERT: 757 747.14 INACTIVE POND FEED Inactive Forcemain 6" C.O. Cell 38 Riser TO MH 62 6" C.O. 6" C.O. 6" C.O. 6" C.O.6" PORT SHOP TRENCH DRAINS OIL WATER SEPARATOR SEPTIC TANKS Cell 39 Riser Pad To MH 64 13 3' 8 " P VC (D ua l C on ta in ed ) @ 2 .0 % Lined 2017 Scent Tray UG Storage Tank Cells 45-47 Inactive MH 21B MH MS-1 Metering Station MH 65 Pumps To UG Storage Tank (Control Panel with Level Indicator) Scalehouse PUBLIC SANITARY SYSTEM BYRON GAINES UTILITY AUTHORITY FLOWS TO CITY OF WYOMING WASTEWATER TREAMENT PLANT CELL PUMP TO MH 61 CELL PUMP TO MH 62 MH 66 TO MH 65 CELL PUMP TO MH 64 CELL PUMP TO MH 64 CELL PUMP TO MH 64 CELL PUMP TO MH 28 CELL PUMP TO MH 28 CELL PUMP TO MH 28 CELL PUMP TO MH 28 Feet 0 200 400 Connection To Public Sewer System MH 67 TO MH 65 MH 68 TO MH 65 N MH 70 Lift Station To Above Ground Storage Tank ALL ASH LEACHATE FLOWS TO LIFT STATION & ABOVE GROUND 34,500 GAL STORAGE TANK Landfill Gas To Energy Bldg D R AW IN G # : R EV : BY : R EV : BY : R EV : BY : R EV : BY : CO UN TY MI CH IG AN O F KE NT KE N T C O U N TY D EP AR TM EN T O F PU BL IC W O R KS D W G B Y: R EV B Y: AP P BY : SC AL E: G :\S W O \S KL \E N G IN \D W G \M AS TE R \U TI LI TY \S an ita ry PF AS .d w g 3/ 18 /2 02 4 9: 51 A M 1 of 1 1" =2 00 ' R SM Cell 35 Riser Pad Cell 38 Riser Pad Cell 39 Riser Pad Cell 41 Riser Pad Cell 37 Riser Pad Cell 36 Riser Pad Cell 40 Riser Pad Cell 42 Riser Pad Cell 56 Riser Pad SO U TH K EN T LA N D FI LL SI TE W ID E SA N IT AR Y & LE AC H AT E PF AS T R EA TE M EN T Ash Force Main MSW Force Main Leachate Main Sanitary Main Lift Station Discharges to MH 28 Water Supply MH 52 MH 51 MH 50 MH 53 MH 54 MH 55 MH 56 MH 57 MH 58 MH 59 MH 60 MH 61 MH 62 MH 63 MH 64 MH 16B MH 18B MH 19B MH 20B MH 21A MH 22 MH 23 MH 24 MH 25 MH 26 MH 27 MH 28 MH 29 MH 30 MH 31 MH 32 MH 16A MH 15A MH 15 MH 14 MH 14AMH 3A WW-01 M H 6 9 M H 7 1 M H 7 2 M H 7 3 M H 7 4 M H 7 5 M H 7 6 MH 17A 34,500 Gal Ash Leachate Tank PFAS OPTION "A" PFAS OPTION "B" Leachate from Cells 1-10 C LY D E PA R K AV E 104th St. South Kent Dr. PFAS OPTION "C" Operations Building Forcemain from Scalehouse Potention PFAS Treatment Area Appendix A a a me = i - ea if btm iri rt i | wl rl ion ee Seer a a fe oa uf =~ ir if pt: wi a | as oe & a ci. 7 a Hi = oO ful a = 1 j es s = i ae. _ al * =) a sah u = = : | J i it - = a FE i aa fl a Sy i \ | f . a a a L -~ = = L = - i? = z . a - "hi: as nell = - ain = x pane = oa __ a == [ox Li =e. 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" 0 oe A i Ts b a a a rT i | | a Tr a a ae ' | te fo | a | _ a al a nF x a A all a i, . he i a ay ra } i e a 8 a ah ts ae i Yat) | ey Pe . 2 os : a ms baal = ie ie ll dl a & o- =. wi ns ll i Bs / IL i oll If | 1 ta ee | i Le he _ _ - ! i a a i HH = tl o r r - A i a | ae fai ai. & |). | a i : z , ti 1 | ee . a a ae ree iT! ll. el Pd fife 7 a Appendix B Municipal & Industrial Storage, Inc. Submittal For SOUTH KENT LANDFILL LEACHATE STORAGE TANK To Supply and install 17@ TEC~STORE LEACHATE TANK BYRON CENTER KENT COUNTY, MICHIGAN MARCH 02, 2010 REVISION -0- 4251 STAFFORD.S.W. Grand Rapids, Michigan 49548 * 616. 261-2860 . . ~ - - an resend TANK DESIGN FREEBDARD 12 IN. REL DESCRIPTION 304 mm NOTESt REL PER MIP 8082361 87/10/08 1, THIS DRAWING IS NOT TO SCALE 2 REFER TO TANK SCEMATIC DOCUMENT URIGINAL, TANK DESIGN 9/13/08 ~013 FUR NUMBER OF RINGS IN TANK AND RESPECTIVE SHEET THICKNESSES] 3. THIS TANK AND FLOGR ARE NOT DESIGNED FOR ANY EXTERNAL - ee A S\ cee A ee ere 16-9 7/16" REVISED TANK 3/01/10 ay De SLIG mm HYDROSTATIC LOADING, TANK TO BE RE-BUILT DIA. 24 ROUND MANWAY Co ROOF PANELS PLAN (18) REQUIRED ESPC PANEL INTERIOR COATING KUO-LON ESPC PANEL EXTERIOR COATING KUO-LON (URETHANE TOP COAT ROOF COLOR: GRAY SHELL COLOR: GRAY | rl TOP OF RGOF cap 3-58" 24 ROUND MANWAY. 1057 mm ftoP OF SHELL SHEET Se ENGINEERED STORAGE PRODUCTS COMPANY DEKALB, ILUNOIS 60115 aan RELL SHEET CONFIDENTIAL 6) PER RING THIS DRAWING IS THE PROPRIETARY PROPERTY OF AO. SMITH ENGINEERED STORAGE PRODUCTS COMPANY] AND SHALL NOT SE USED NOR REPRODUCED WITHOUT THE EXPRESS WRITTEN CONSENT OF THE COMPANY, AOSESPC COPYRIGHT 1997 21-10 5/8" ALL RIGHTS RESERVED 6670 mm, DRAWN BY MMB ACCESS DOUR & SHEET NOMINAL GPENING DATE 03/01/10 24" (610 mm Fe | ) d) REQUIRED 1722 SFWT FLOOR LEVEL GRADE LEVEL | __ SZ 1 Te SOUTH KENT LANDFILL LEVATION BYRON CENTER, MI. DRWG NO. 808236001 -~ _ 7 a a a we weer a _ ent ceneenen tecStore @)Kuo-Lon THE NEXT GENERATION EPOXY COATING FOR TECSTORE TANKS a Alkaline Wash All steel panels are cleaned with an alkaline wash. Mechanical Blast A controlled blast with steel _ 4 grit provides a minimum finish of SSPC-SP10 (SA 2.5) near-white blast with 2.0-3.0 mil profile. 3 Powder Coating Kuo-Lon is applied to the interior of the panels at 5.0 mils av: e DET. 1 exterior is coated to 3.0 mils minimu DFT. Higher build rates are available. a Initial Cure Partial cure of coating: t 330F (165C) Top Coat Application of-aliphatic polyurethane Op coal 4.5 mils average.DFT to he ext r-of.the panels on top. of oe he Ku n powder. Final Cure Final cure of coating system at 400F (204C). a TTT RESISTANCE Kuo-Lon, Typical Liquid Storage Applications Include sodium chloride potable water deionized water manure/sewage ed water xylene sodium hydro water (170F) wastewater distilled water salt water crude oil DOCUMENT NUMBER: 8082361/ TITLE TANK CALCULATIONS Page 4 REL.: 3 DATE: 08-26-08 BY: DS SUMMARY OF INPUT DATA STRUCTURE MODEL a 17 22 FOUNDATION TYPE SF SPECIFIC GRAVITY --- 1.000 HN PRESSURE RATIO - 1.000 FREEBOARD 12.000 in 305. mm WATER COLUMN PRESSURE ---- 8,000 In 1.991 kPa ROOF TYPE ~ STD ROOF WEIGHT 5.000 psf 24.412 kg/m2 SC ROOF HEIGHT 2,500 in 63.500 mm DC ROOF PROJ AREA 35.810 sq ft 3.327 sqm DC ROOF CENTROID - 14,910 in 378.714 mm TOTAL ROOF HEIGHT ae 41,570 in 1055.878 mm ROOF SNOW LOAD 5.000 psf 0.239 kPa WIND DESIGN - NONE WIND SPEED. --. NA mph NA m/s WIND STIFFENER ANALYSIS --- NONE SEISMIC DESIGN - AWWA D103 87 (EFFECTIVE MASS) SEISMIC ZONE ~-- 4 IMPORTANCE FACTOR - NA ALLOWABLES USED wren menen enue, AISC FLOOR 0.D. 16.875 ft 5143.500 mm SUMMARY OF INTERNALLY ASSIGNED PARAMETERS BOLT DIAMETER -- 0.500 In 12.700 mm HOLE DIAMETER -- 0.5625 In 14.287 mm TOP COURSE EDGE DIST - 1.000 in 25.400 mm STEEL FLOOR IN FNDN - 0.094 in 2.388 mm DIST T/ETG TO B/FLR -- 0.000 in 0.000 mm TOTAL FNDN THICKNESS -- 0.094 in 2.388 mm SHEET DENSITY 590.000 pcf 9457. kg/m3 STEEL ELASTIC MODULUS 30000000, psi 206843, MPa STEEL FLOOR DENSITY - 590, pef NET SHEET WIDTH 105.462 In 2678.735 mm 9451. kg/m3 = NET STANDARD SHEET HT. 54.990 in 1396.746 mm NET PARTIAL SHEET HEIGHT -- 23.265 In 590.931 mm STARTER PANEL HEIGHT -. - 18.308 in 465.023 mm INVENTORY FILE USED; --------- RUN2.DF ane DOCUMENT NUMBER: 8082361/: TITLE: TANK CALCULATIONS Page 2 17 22 AQUASTORE STRUCTURE DESIGN SUMMARY { 6 SHEETS PER RING/COURSE) COURSE SHEET THICK THICK PLACE GEOM MAT LIMITING i NUMBER in. mm CODE CODE CODE FACTOR(S) 094 2.388 1102 094 2.388 4101 094 2.388 1104 094 2.388 4101 099 2.515 1201 Garena OARWN- 132 3.353 2 A mk oa ee AD 6321 : Doooeca ANCHORS REQUIRED: NONE STRUCTURE DIAMETER 16.78 ft 5116.01 mm HEIGHT OF STRUCTURE TO EAVE 21,88 ft 6668.34 mm VOLUME OF STRUCTURE TO EAVE 4841. cu ft 137, m3 VOLUME OF CONTENTS 4620. cu ft 1317. m3 VOLUME OF CONTENTS 34557. gat 130813,L 1b ae nt 2. cu ft 0. m3 VOLUME OF STEEL FLOOR FND. 5521. tb WEIGHT OF EMPTY CYLINDER ABOVE FLOOR 2504. kg WEIGHT OF ROOF 1106. Ib 502. kg SNOW (LIVE) LOAD 1108, Ib 502. kg WEIGHT OF CONTENTS 288264, ib 130754. kg STEEL FLOOR WEIGHT 1034. Ib 469, kg TOTAL WEIGHT ON FOOTING HH Ut a 297032. Ib 134731. kg 0. Ib O.N WIND SHEAR AT TOP OF FOOTING WIND MOMENT AT TOP OF FOOTING 0. ft-lb 0. KN-m SEISMIC SHEAR AT TOP OF FOOTING 19496. Ib 86722,N SEISMIC MOMENT AT TOP OF FOOTING van 193738. ft-lb 263. kN-m dsrose Polygon DOCUMENT NUMBER: 8082361 - TITLE: TANK CALCULATIONS Page 3 HOOP STRESS ANALYSIS --- STRESS - PSI --- COURSE DEPTH PRESS NET ALLOW HOLE ALLOW BOLT ALLOW FT PSI TENS TENS BEAR BEAR SHEAR SHEAR 1.0 S 1068 18000 3316. 40500 794, 18163 5.6 3966. 18000 12316 40500 2948 18163, 10.2 6865, 18000 21315 40500 5102 18163 30314 40500 7256. 18163 14.8 9763 18000 19.4 12022. 33923. 18664. 2935 81000 4dA7 4705. 18163. 2489 E ZOAARONA Dp 20.9 WCeOOQnn @N NNN 8730. 33297, 4 2635, 81000 4247, 1 8183, AXIAL STRESS ANALYSIS = STRESS - PSI --- COURSE AXIAL ALLOW HOLE ALLOW BOLT ALLOW COMP COMP BEAR BEAR SHEAR SHEAR 45. 1809 453. 40500 409. 18163 64. 4809. 642, 40500 154, 18163, 83. 1809 831. 40500 199. 18163, 101. 1809 1019. 40500. 244, 18163 APwWN 115. 1902 1156. 81000. 291. 18163 FND 93. 2507 465. 81000 156. 48163 SEISMIC STRESS ANALYSIS -- STRESS - PSi --- COURSE AXIAL SEIS TOTAL ALLOW HOLE ALLOW BOLT ALLOW COMP BEND COMP COMP BEAR BEAR SHEAR SHEAR 27 1 28 3080. 280. 54000 67, 24217. 45. 45. 90. 4094 906. 54000 217, 24217. 64 162 226 4677 2268, 54000 543, 24217. 83 362 445 5057. 4469. 54000. 1070. 24217. 97 625 722 5493 7253, 108000. 1828. 24217. ZAROnNA 79 552. 631. 6534. 3170, 108000. 1066. 24217. Document Number 80823614/ 1 Rel. No. 2 Title: Tank General Notes Page 1 TANK DESIGN SPECIFICATIONS This tank is designed in accordance with ANSI/AISC 360-05, Specification for Structural Steel Buildings - Allowable Stress Design. COATINGS SPECIFICATIONS Coatings used on components of this tank are in compliance with the appropriate sections of AWWA Standard D103. STRUCTURE BOLT SPECIFICATIONS Structure bolts are carbon steel, zinc coated, with 1/2"-13 UNC-2A thread, and conform to AWWA D103, Section 2.2.1, as noted below. A. 1 inch long bolts conform to the mechanical properties of SAEJ429, Grade 2 - exceeding the mechanical properties of ASTM A307. B. 1-1/4 inch long bolts conform to the mechanical properties of SAEJ429, Grade 5 -equivalent to the mechanical properties of ASTM A325. C. 1-1/2 inch long and longer bolts conform to the mechanical properties of SAEJ429, Grade 8 - equivalent to the mechanical properties of ASTM A490. Unless noted, all tank structure connections are bearing type connections, snug-tight condition, per ANSVAISC 360-05, Tank manufacturer does not require special inspection per IBC, Sectlon 1704. APPURTENANCE AND PIPING ORIENTATION Orientation of all appurtenances and piping connections shall be established in the field. THROUGH-THE-SHEET PENETRATIONS All openings through the tank side wall greater than 4 inches (102mm) in diameter shall be reinforced in accordance with AWWA D103, Section 3.11. All openings through sheets having less than 24 inches (610 mm) between horizontal bolt lines, or having less than 24 inches (610 mm) of available sheet space from the floor surface up fo the first horizontal bolt line shall not exceed a diameter of 4 inches (102 mm). These openings of 4 Inches (102 mm) and less shall be reinforced in accordance with AWWA D103, Section 3.11. ROOF MANWAY OPENING Field cut roof manway opening from roof pane! and/or roof knuckle using the outside edges of the prepunched notches and holes as the opening outline. (Do not use a cutting torch to perform this operation.) Apply sealer to the appropriate roof surfaces and field cut edges. VENT An adequate pressure/vacuum vent must be provided by the builder in order to prevent tank damage. Document Number 8082361, Rel. No. 3 Title: Tank Fastener Schedule Page 1 Structure bolt quantities at (H)orizontal and (V)ertical seams Thru the sheet fasteners | Truss Fasteners BOLT LENGTHS: ? thw yy" 1%" " 24 ra 1% 2%" 3" 3% (mm) 25.40 34.75 38.10 44.45 50.80 57.15 63.50} 34.75 57.17 76,20 83,90 I C.S. CS. C.S. CS. CAP. 36 PANEL/KNUCKLE 410 4 MANWAY. 24 SEAM Wide H 4 124 SEAM Vi 60. SEAM Wide H 2 4120 12 SEAM V2 150 SEAM Wide H 3 120 12 SEAM V3 160 SEAM Wide H 4 120 42 SEAM V4 150 SEAM Wide _H 5 120 42 SEAM V5 306 SEAM Fnd._H 6 120 12 ACCESS DOOR 0 leo REINF. PLT. 90 > |S JO JO | Jo [9 [a Jo [9 Jo Jo lo TOTALS: 2100 76 8 SIO [9 JO 19 oO 12 [9 fO JO 19 Jo Jo Jo DID 12 19 [0 Io [9 | Io JO Jo [0 lo Io SIO 12 19 1o jo |e Jo lo Ja [Io lo Ia Jo SIO OO 9 Jo | JO Ia fo elo lo lo S(O 1D 12 [2 [2 [oO [a Jo Jo |9 [a Jo [oO IS 19 19 Jo [Oo [2 12 [9 Ia 0 DD Ia Jo |o D 12 [2 [oO [2 1@ JO |o 1a 1 Ja Io Oo Jo 2 [2 [ J@ JO |e [a |e Jo Jo I fo |o Jo Document Number 8082361 Rel. No. 3 Title: Tank Schematic Note: Ail brackets located at top of specified ring. RING # SHEET BRKT. BRKT. VERTICAL SHELL SHEET THICK. TYPE QTY. BOLT LINE PART NO. 1V 263569K0100 RING #: 4 0.094" ( 2.388 mm) (25 SHT.) NONE RING #: 2 0.094" ( 2.388 mm) NONE iv 256047K0100 RING #3 NONE 1v 256047K0100 0,094" ( 2.388 mm) RING #: 4 0.094" ( 2.388 mm) NONE qv 256047K0100 RING #5 0.099" ( 2.515 mm) NONE 2Vv 256050-0100 FND. 0.132" ( 3.353 mm) NONE eoa00oo 3V See fnd. parts list Document Number 8082361 - Rel. No. 3 Title: Tank Parts List Page 1 ITEM ary, PART No. DESCRIPTION 8082361-001 TANK ASSEMBLY 8082361-002 FOUNDATION ASSEMBLY 26614452300 ROOF CAP 1 016197J2200 ROOF PANEL, COLOR 262265-001 MANWAY DOOR ASSY., 24 OONAMNRWH 5 10 14 12 13 np 267692-000 EDGE TRIM 14 254672-202 SEALER 79, CARTONS (ALUMINUM) 15 16 17 18 19 20 2 25981 1-003 GASKET, 24" 266214-1300 REINFORCING PLATE, .197 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 2100 262000-001 STRUCTURE BOLT, 1, BLACK 45 66 262000-002 STRUCTURE BOLT, 1 1/4", BLACK 46 30 262000-003 STRUCTURE BOLT, 1 1/2", BLACK 47 48 49 50 51 52 53 54 56 56 2196 252275-000 WASHER, 1/2" ST 2196 262416-001 HEX. NUT, 1/2 HDZ 58 Document Number 8082361. Rel No. 3 Title: Tank Parts List Page 2 ITEM QTy. PART No. DESCRIPTION 59 60 61 62 63 64 65 66 262778-060 DANGER DECAL 67 267249-000 INFORMATION SIGN 68 266182-000 NAMEPLATE OPERATORS MANUAL 69 266254-000 70 262166-000 IMPORTANT DECAL mA 71 260581-000 TANK MOD. WARNING D GA 72 200 2 2N 0 266255-000 INSPECTION & MAINT. REVIEW 73 74 75 76 77 78 79 80 81 266216-0102 24 ROUND ACCESS DOOR SHEET 82 83 268605-017 24" DOOR, NORM DUTY EPOXY 84 85 263569K0100 EXTENTION SHEET, 25 86 18 256047K0100 SHELL SHEET .094 HRS 87 256050-0100 SHELL SHEET .099" BLK, STL. 88 89 90 91 92 93 94 95 96 97 98 99 00 104 102 103 104 05 106 07 108 09 110 411 112 113 14 15 16 17 18 | 2 Document Number: 8082361 Rel Title: Fnd. Parts List Page 1 ITEM Qry. PART No. DESCRIPTION 1 8082361-002 S.F, FOUNDATION ASSY. 261716-1200 .4320" FND. SHT.HSLA 1 2637450100 17 FT. DIA. FLOOR ASSEMBLY 261067-000 TAPERED SPACER Somronewna, a 8 oe = a 3 20 254672-202 3 SEALER 98, CARTONS (ALUMINUM) a oe s 8 8 3 R g 3 N 3 8 8 & 8 8 45 263156-0014 ENCAPSULATED NUT, PLASTIC g 8 8 102 262000-001 STRUCTURE BOLT 1", BLACK s 255 262000-002 STRUCTURE BOLT 1 1/4", BLACK 8 36 262000-003 STRUCTURE BOLT 1 1/2", BLACK 8 & a 393 262416-001 HEX NUT, 4/2 HDZ 8 408 282275-000 WASHER, 1/2" & E & & 3 & & Document Number: 8082364 Rel.: 2 Title: Fnd. Parts List Page 2 ITEM ary PART NO. DESCRIPTION 50 51 52 53 54 55 56 57 4 266346K0100 CENTER COVER PLATE 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 v7 78 79 80 vee Document Number: 8082361 Rel.: 2 Title: Fnd. Fastener Schedule BOLT LENGTHS: 4" 1%" 4%" 4%," an {mm) 25,40 34,75 38.10 44,45 50.80 VERTICAL 102 Q Q 0 0 HORIZONTAL 0 210 36 0 9 pe ses pe es Appendix C Appendix D a + name: SA7O24IOOD\CADT|DESON\KENT-D18.OWO Lost edited: 94/04/20 1222 ADA. GUNA | Crerts Semterin SiC OS-25,] tories DOL OSE | eorapent At. SORT, | Led Pentel MOLES | Propet, ere, Ooi ana | MATCH LINE : SHE SHEET D17 FOR CONTINUATION 4 - ee - P-5, @e) SHT DIT SHT O17 FROM TANK T~3 : TO TANK 1-2 CONTROL PANEL 1-5 GY GRAVITY. LEVEL SENSOR LE7, | Zww (PvC~ THE OPERATOR CONTROLS P-5 BY ENCE OF OPERATION: sm 4GHU_(PVCSW) yee (/STOP P~4. en i, 1@o| g ADJUSTABLE STROKE LENGTH ANO FREQUENCY ON THE PUMP, SUMP PUMPS POLYMER INTO CLARIFIER WHENEVER PUMP P1 IS RUNNING, {80 gpm) FEED TO CLARIFIER C~1 IS BY GRAVITY FLOW FROM MIXING TANK T3, PUMP P-4 CLARIFIER RAKE 1S Oh) BUILDING SUMP S-1 H 7 (OUNTED CONTROL SWITCH AND TIMER ON THE LOCAL SLUDGE FROM THE CLARIFER iS PUMPED TO THE FILTER PRESS SY AIR DIAPHRAGM PUMP WHEN TANK LEVEL 1S LOW A LOCAL ALARM AT THE TANK ANO AN INDICATION AT THE TORQUE ALARM AND RAKE STOPPED ALARM ARE INDICATED AT THE CONTROL PANEL. METERING PUMP P7 CONTROLLED FROM A LOCAL CONTROL PANEL ON THE CLARIFIER SUPPLIED WITH THE CLARIFIER. HIGH RAKE CONTROL PANEL WILL ALERT AN OPERATOR 70 REFHL TANIC CLARIFIER EFFLUENT FLOWS TO EFFLUENT TANK POLYMER TANK LEVEL S MONITORED BY TANK PUMP P- 7 IS MANUALLY ADJUSTED BY SUMP _HIGH LEVEL START P~4 SUMP ALARM LEVEL START P=4. L-. a tensa e Se ~ nent 1/Z-POLYMER_(PYO-SW) [SUMP LOW LEVEL STOP P4 SME ON Cee Stee eae. i Ee 5 4 | : spowac TANK IS LOW. ] #15 (FRE) POLYMER 1/2POLYMER ae PUMP P-7 4 BUILDING QUMP 84 A, SFEWENT TANK 5 AV r anna ap nnn ene HIGH TORQUE ALARM = ---|---------. (Pve-s)_~ Bt CLARIFIER RAKE RUNNING saan ate a eee Jenn ane LOCATED NEAR THE TANKER CONNECTOR. 480V, HHL TORQUE, RAKE STOPPED === meee ene ee | Sout (PvCSH) GF HimHt TORQUE RAKE STOPPED TANK LOW TAN T_9 OFACUFS MIA TRAY CHD BWA Wart | 6. SUMP LEVEL [S MONITORED BY LEVEL SENSOR LE~S. wM-2 Yee -tk BY GRAVITY FROM EITHER HIGH OR LOW TANK OUTLET. COAGULATING sme : POLYMER TANK 1-6 ; 1200 Lee a AES poco | TANK T=6 LOW LEVEL Se ee ee wenn rerecemeemn ce emeamreen rans anevats | manasanee ena a a at a DRY POLYMER EDUCTOR + THE PUMP WILL RUN UNTIL LEVEL IN THE SUMP DROPS TO LE-8 LOW. EFFLWENT TANK T-S RECEIVES FLOW BY GRAVITY FROM CLARIFIER C1. 3 a= |---| START START/STOP METERING PUMP. STOP METERING PUMP Pol. PZ. ae penne emer enenee, ne z Oc I TCA (PR) _ PUMP DOWN SUMP IF THE CONTROL SWITCH AT THE MAIN CONTROL PANEL 1S IN i@ g START/STOP_ Suu START/STOP_SLUDGE FEED PUMP: 10GE FEED PU IME Pe =| [rsreeetenten nanan -~ | ----} --- --- --- eae nr ener Rarer tn pence ee een beer or ont mesa tenses, wee Fane won [Bem | eee 14% eee nn | }--__-_4_. oh { AT SUMP HIGH LEVEL, TRANSFER PUNP P4 WILL START/STOP |. PUMP RUN {S iNDICATED ON THE MAIN CONTROL PANEL LEVEL FLOW OUT OF TANK TO POTW iS | P=4 PUMPS INTO YANK T-2 AND IF on Seentesinen fone fF Sith HIGH LEVEL NORS NOT TURN ON P4 ANT LES SENDS AN ALARM TO CONTROL PANEL WARNING OPERATOR OF AN IMPENDING OVERFLOW. CONTROL LE-S STOPS P IF T5 LEVEL DROPS TOO LOW AND SENDS INDICATION TO CONTROL PANEL THAT AND PUMPS EFFLUENT FROM TANK T5 TO AN EMERGENCY TANKER. START/STOP CONTROL FOR PUMP P-6 IS FINAL EFFLUENT PUMP P6 IS MANUALLY CONTROLLED gq x i aan anan. eases annem | } FLOW TO TANKER IS TOTALIZED BY FT-3. FLOW TO POTW iS TOTALIZED BY ISCO FLOW METER AND METERING FLUME. -@- 4 GWT 3 Cy jp i n : arenes aeee- | = pe TANK T=5 HIGH LEVEL CLOSE wet & CVZ, HIGH LEVEL ALARM rerrereeereremmneeinee | emma nem . --------- TANK T-5 LOW LEVEL STOPS: PUMP P6 (2) BP pe Ws INFLUENT STORAGE TANK OVERFLOW, fa wane fo weer =~ cae neta te --o--: ENTERING BUILDING. | 2) CLOSES CV=3-(AND CY1) INSIDE THE. BUILDING. : on == ae START/STOP PUMP P6 ann. - nn STAR START/STOP P-6 (Stop Pos : @s FLOWMETER momeeeand ag By 3 38 PE-FT : SLUDGE _ oe) isco. FLUME METERING FILTER PRESS. '& POLY SUBBLER TUBING INSIDE 1-1/2" NeW (PYCSW) 3 BJ cee me mate nae te a PNEUMATIC. FILTER. PRESS CONTROLLER CHT (PYO-Sw) PUMP, 3 gpm Lan 120VAC PANEL SYSTEM MUST BE RESET FROM PUSHA@UTTON OUTSIOE OF MANDOOR BEFORE TO ORAIN FILTER PRESS : ELECTR OPTIONAL a CoM WILL LIGHT WARNING LAMP LOCATED OUTSIOE OF BUILDING AT ENTRY DOOR THAT A GAS QUILD-UP EXISTS PUMP P8, DUMPSTER : ZVENT AR 4F METHANE IS DETECTED, ANALYZER WILL TURN ON EXHAUST FANS IF THEY ARE NOT ALREADY RUNNING ANO TWO HYDROCARBON SENSOR PROBES ARE LOCATED WITHIN THE PLANT AND WILL DETECT METHANE BUILD~UP. E me PRESS! ; 50 gpm PEAK (PvC-SH) 1) TRUCK HAUL, EMERGENCY 27 gpm AVERAGE CONTROL. THROUGH ROOF Hl (FO GRAND RAPIDS POTW) Dovokeped 8 WNH,MAC,TBK drm BF Sit : PROCESS FLOW DIAGRAM - PRETREATMENT SYSTEM ( 2 of 2) 70241 Reproved By: JFG Otte 9909-94 Sheet Humber REMEDIAL DESIGN 4. SUBMITTED FOR U.S. EPA INTERMEDIATE, DESIGN REVIEW 01-15-93 Orowing Hunter 18 of 37 KENTWOOD LANDFILL 2 SUBMITTED FOR FINAL DESIGN REVIEW 12-09-94 Reterenes: fii KENTWOOD, MICHIGAN Ruvisions: MISCELLANEOUS UPDATES: 04-19-94 BER p18 ne mtnpninint type nan oot tpettesespeesee ee ee _ ae . TO WATER CONTROL PANEL, TREATMENT dente pe rH MR eat ana nanan neM Ramen SHT O17 SHUT OFF VALVE PNEUMATIC COUNTER REGULATOR [ MANHOLE: ee 1 1/20 {PE-FD AIR SUPPLY COMPRESSED oh FROM SV3. 1/2 SAMPLE TAP (HYP) COMPRESSED t TCA (PE-FT) AR SUPPLY FROM SV4 WELL CAP- 2 BUTTERFLY VALVE (TYP) 3 GWU (FRP) _owu _(PE-FT) a, zg cwu (PE-T) > ow (PE~FD) SHT O17 Nt tt 2 OH (PE-FT) z ou (PE-FT) Z_oHY (PE-Ft) PATLESS ADAPTER g CORRECTED DIRECTION OF CA LINES, 04-19-84 BER EXISTING 480V FEED INDICATOR. PUMP, P-EWT EXISTING 480 Dewloped PF MAC,ELC Revisions: fy EWt (2 GPM) _-J BaunY Tomes sere St CO-OS95 | tetwon Seire ANDO 89 wenearveet Ree en RR. |e Patera MALE CROAS. Prarl erne B RAS ea OAS SAMPLE, te ire) a 33 Qin 18-95 08~09~93 92-09-94. LEACHATE. UFT STATION, Fems (PEF) CONTROL PAN! EXISTING 4 _MAIN amen ! LEVEL SIGNALS 3 | ene ESTING 47 MAIN cee ne cata pn et SEE SHT 32 ne | (1/4 GPM) EXTRACTION MANHOLE AND SHALLOW TRENCH a LEACHATE LE~-1 (6" PE-PF) EXT & LEAGHATE MHI (2_GPM) SEE EWt FOR TYPICAL WELL INSTALLATION DETAIL pao poy A penn ne tee tetnnen ef Li Se EXIST. iSt_&. (@ GPM) SEE EWI FOR TYPICAL WELL INSTALLATION OETA. eg STE. CIOTAL 2.1 GPM) ra ews a | ! | (4. GPM) SEE EWI FOR TYPICAL WELL INSTALLATION DETAIL | ! A | woe a! a LEACHATE. (LEACHATE MHS3 LEACHATE MHS. LEACHATE MH2 (3 GPM) SEE EWI FOR TYPICAL WELL INSTALLATION DETAIL a a a 2 LIFT GTATION SUBMITTED FOR U.S. EPA. INTERMEDIATE DESIGN REVIEW SUBMITTED FOR PRE-FINAL DESIGN REVIEW SUBMITTED FOR FINAL DESIGN REVIEW Kt LIFT STATION PUMPS, ow (PE-FT) 30 GPM, LSI, US2 (4 GPM) SEE EWI FOR TYPICAL WELL INSTALLATION DETAIL on | roe LEACHATE LE=2 (6 PE-PF) 2 GWU (PE-FT) (1GPM) SEE EW FOR TYPICAL WELL INSTALLATION DETAIL Exist 4 extst 41 LEACHATE LE--3 (6 PE-PF)_ . Z GWU _{(PE-! qo ed SEE EWt FOR TYPICAL WELL INSTALLATION DETAIL | G4 GPR) | ! Lee od Be a as SEE EWI FOR TYPICAL WELL INSTALLATION DETAIL LEACHATE LE~4 (6 PE-PF) (1/4 GPM) LEACHATE MHS4 LEACHATE MH6 SEE EWI FOR TYPICAL WELL INSTALLATION DETAIL & ramon] (1/2_GPM} (2 GPM) SEE EW1 FOR TYPICAL WELL INSTALLATION DETAIL sare MANHOLE PNEUMATIC COUNTER | en OFF VALVE: SEE DETAIL {t {- t co 2ow (FE-FY) ALL FLOWS SHOWN ARE STEADY STATE FLOWS. Tow (PEF) : (1.8 OPH) GROUNDWATER Pips PROCESS FLOW DIAGRAM - GROUNDWATER AND LEACHATE COLLECTION SYSTEMS: REMEDIAL DESIGN KENTWOOD LANDFILL KENTWOOD, MICHIGAN 1 GROUNDWATER PUMPS EW1 THRU EW12 AND LEACHATE PUMPS MH6 THRU MHi0 ARE. SUPPUED WITH i ro ~ A00 RISER sy _ AIR FROM AR COMPRESSOR THROUGH SOLENGID VALVES SV-3 ANO SV-4. WHEN SV-3 AND SV4 ARE 4 SEE DETAL Ga DE-ENERGIZED, SUPPLY AIR TO PUMPS [5S EXHAUSTED TO ATMOSPHERE. PUMPS WILL CYCLE ON THOR LEVELS CONTINUOUSLY PROVIDING THAT LEACHATE LIFT STATION PUMPS OPERATE TO PUMP Shest Number OWN THE UFT STATION AND THE INFLUENT TANK 1-2 IN TREATMENT BUILDING 1S NOT AT HIGH LEVEL. 1 , 19 of 37 LEACHATE LE-6_(6"_PE~I PF) LEACHATE LES (6 PE-FT) LEACHATE UET STATION SEQUENCE 70244 Dis | THE LEACHATE LUFT STATION DUPLEX PUMPS ARE CONTROLLED LEVEL SENSOR AT THE UFT STATION. qa BUTEA VALVE | | DUPLEX CONTROLLER WKL ALTERNATE PUMPS AND ST/ BOTH or i (PS WHEN LUFT STATION GOES TO 2 PITLESS ADAPTER re ee et sae te ene fer eed | HIGH LEVEL, IF LIFT STATION REACHES Hi~HI LEVEL, A SIGNAL IS SENT TO YHE TELEPHONE DIALER BE SHUT DOWN, TELEPHONE DIALER SSE Livre od | Lot Lf : a AV THE TREATMENT PLANT AND GROUNDWATER PUMPS: SENDS SIGNAL TO SHERIFFS DISPATCH. LEACHATE MHIO LEACHATE MHO (LEACHATE MG LEACHATE MHT LEACHATE MHS. name: AN 7D2ATOOC\ CAD OESIGNYIENT-O18.0"0 Laat ecfied: 94/04/20 @ 1020 ADOC, SEE NOTE 8, THIS SHT TRENCH ORAIN: HIGH PARTITION HANDRAIL WITH TOEPEATE OVERHEAD ROLLUP DOOR 4 DRY DISCONNECT ('-TW X 10'-CH) (BROW: FLOW METER DISPLAY] /| SEE OVERHEAD DOOR. AA 40 DOOR Bae, aie NOTE 14 r 42'-0" x 12'-0" WINDOW bee 92-0994 04-19-94 BER 04-27-94 BER go0 anon goa ao s neers Lo een el =" BES pe ae OF {oo *E. SODIUM bonnes boasuacos Soaaqunag} peucasa DOCK LEVELER, pagaaaa abagouauaal a a HMDRONOE bosogas basacac aRagagouog ;:ogeeanang Broan OF St OFFICE penagsnacoosdgn: agacan ango~ AonooGd| = (io x 8) past Soane goat S@acog ooecal EMERGENCY EYE oaao *aood Banco Boor agang} aaa = Bac bougoll -G DOOR _/ nIUM puc Oe Teanell Snag] POTASSIUM ROXIDE fos aaa] PERMANGANATE Sra, CABINETS SEE NOTE 13 FILTER: zi (PNC-SW) PRESS: Lae 4 POLYMER AND MODIFY NOTE $15. MIX TANK F=6) I FLOOR DRAIN ayuaunl Hl Ay MISCELLANEOUS UPDATES: TO SAN, 2 1/ZORAK 7 juenod (a X 6) al %, a) DRY POLYMER aoaaag sacana eoauo5) 24-6" 0. SAN (PYO-DR) Pod P=7 ;ngacaq ouanaa Oevetoped BF MAC,ELC Arrows BF Jeg Ravislom: VARIOUS PIPING CHANGES. C0. 1-1 TANK aeo50 oosaod soageual EMERG! ax050 booaned EYEWASH cana y Danan :oaoean), Gageao| AND SHOWER ~ oO Cees 35 1/2'PRI aacacol Wwaano| faye sine Sus 4 /2P WORKBENCH. banag| eS Probeet eroyar BER 00 O 9S. | Caren S| 4" BRN (PVCDR] Seger an WEF TAB FD. TTNPW, i /2NoOH = (POLY) COUNTER-TOP (PvcSw) POWER WASHER REFRIG. BELOW SEE NOTE 3, THIS SHT 10 GAL HW TANK 6.0. Re S| SEE ES OU O1=15=93 02-08-94 j 4. TRENCH COUPLING: NOTE 7: TRENCH =} DRAIN MM~-3 A HU ORAIN 4 Ste NOTE_12- laneo 29000 gas. CLARIFIER, 3 aoa B gegadanl 38 AY E TANK Te3 SL_(FRP) S'SL. (FRP) ES BQ 4 a yg EFFLUENT 4SAN (PCOR) TANK I-85 aS LE= = ! eel ea 2 SGWU (PE-RP} FROM EXTRACTION WELLS AND LUFT STATION 3 e"GWT (PVC 2GWU (PE-RP) FROM SOUTHERN EXTENSION MANHOLES AND WELLS EW11 AND 12 PCs OVERFLOW FROM T-2 a i = JE 1-1/ZCA(PE-RP) TO EXTRACTION WELLS Ps BISAN_(PYCDR) 7CA (PE-RP) TO SOUTHERN EXTENSION MANHOLES AND WELLS EWit AND 12 LE2A, Oo! INSTALL FLOOR AND GRADE eFRP) C0. Zs FRE) SEE DETAIL BEAM PENETRATION SLEEVES \ UPPER AND __e IF0 LOWER OUTLETS, ZH ee pee VALVES (2 EACH or Pp 5 olf-28 (ELUENT BACKFLOW. Joo" UMP SBOTTOM STORAGE, PREVENTOR =e DRAIN, TANK T=2 (SEE NOTE 3, WATER AR 2AL. (FRP) oe : PRESS 0 ZC (CPR) co. LOSED) SUSMITTED FOR U.S. EPA INTERMEDIATE DESIGN REVIEW SUBMITTED FOR FINAL DESIGN REVIEW Geese nr rte i DW (OWE) oH fe CA (CRP) 4 2 @ 4 | a= AIR COMPRESSOR: L-2ca (ore) C# oveRFLoW| BLOWER B-1 TO TANK 'T5} (Pvc! SEE NOTE 10, Te METER, THIS SHT APINTAKE (PvC-Si) (BY OTHERS) S-8 . 48'-0" TREATMENT BUILDING EQUIPMENT AND PIPING PLAN : BUILDING NOTES a HEAT TRACE CAUSTIC. 10H) an AUTOMATIC FIRE PROTECTION SYSTEM SHALL BE SUPPLIED AS DESIGN, BUILD PACKAGE BY BUILDING CONTRACTOR INCLUDING BACKFLOW HEAD AKO SUCTION Pi f ING, UKE PR SHT 022, HEAT TRACE PUMP POWERED PROVIDE MINIMUM 1000 GALLON PRECAST REINFORCED CONCRETE SUMP PRI OR, PIPING, SPRINKLER HEADS, CONTROLS, AND SMOKE ANO HEAT DETECTORS. SHOP DRAWINGS TO BE REVIEWED WITH 10. BASE, MINIMUM 10 INCHES THICK, CITY OF KENTWOOD FIRE MARSHALL PRIOR TO CONSTRUCTION, WwW UAINTAIN MINIMUM 3'-0" CLEARANCE BETWEEN FILTER PRESS PLATFORM PROVIDE, FOR ALL DRAINS TO SANITARY. 00 NOT TRAP AND CLARIFIER TANK AND LEGS, AND BUILDING SUMP. DRAINS TO BUILDING SUMP. 12. INSTALL 1/2 FLEXIBLE HOSE FROM POLYMER PIPING INTO TANK T-3 EFFLUENT PIPE. : 3 PROVIDE {HPW SERVICE WATER (I.c. DOMESTIC WATER AFTER LOOP TO HOSE BIBB FOR POWER WASHER, PROWe ONE HOSE a BS PER WALL OF BUILDING AT 3'-0" ABOVE 15, KM,04 STORAGE CABINETS WITH FUSIBLE LINK, SELF CLOSING . FM AND UL USTED, CABINETS SHALL STORE NOT MORE THAN R. PROVIDE SIGN ABOVE HOSE BIB THAT READS "NON-POTABLE 750 POUNDS OF POTASSIUM PERMANGANATE EACH, CABINETS SHALL BE WATER, UNSAFE FOR DRINKING. LABELED CLASS {1 OXIDIZERS" (NO. 75}. , a PROVIDE 1"NPW LINES TO 4 ABOVE TANK T~1, FOR DILUTION WATER, ANO TO TANK T-6 DRY POLYMER EDUCATOR. 14. EACH SODIUM HYDROXIOE CONTAINER SHALL CONTAIN NOT MORE THAN TREATMENT BUILDING EQUIPMENT PIPING PLAN REMEDIAL DESIGN KENTWOOD LANDFILL KENTWOOD, MICHIGAN 500 GALLONS, 5. PROVIDE REINFORCED EQUIPMENT/TANK PADS FOR Ali PUMPS AND PROVIDE SLUDGE DUMPSTER DEWATERING PUMP, P~8. TANKS, LEVEL ALL EQUIPMENT ZNON-SHRINK, NON-METALLIC Aw i GROUT. (SEE PUMP SCHEDULE ON SHEET 025) * 6 COMPRESSED AIR LOOP AROUND BUILDING (COPPER 16. PROVIDE 4PVC VENTS FOR FLOOR DRAINS PER BOCA. Sheet Kumber PP WITH 1 DROP 10 BALL VALVE, ONE DROP PER FALL OF BUILDING INSTA BALL VALVE, WITH THREADED END CONNECTION, AT 3 Ww PROMDE TANK T-2 WITH 4"OVERFLOW (4GHU) WITH TRAP TO 20 of 37 oe ABOVE FLOOR, HOLD 24 OF WATER COLUMN, Oreing Humber 18 PROVIDE FIRE EXTINGUISHERS PER 2A:408C, LOCATE SUCH THAT 7 NO MORE THAN 75 OF TRAVEL IS REQUIRED. 70241 TERMINATE 2 SL (FRE) CORE BLOW UNE 6 ABOVE INFLUENT 8. PROVIDE Z CONNECTION WITH THREADED BALL VALVE FOR EMERGENCY 10, PROVIDE NO SMOKING SIGNS ON OUTSIOE OF ALL DOORS AND ON ALL | COMPRESSOR HOOKUP. PROMIDE ISOLATION VALVE FROM AIR TANKS INDOORS, SS COMPRESSOR. SSS > ame: EN 7024 1OO\ CARN DESO KENT=020.000 Lant edited: 94/04/27 @ 00:36 ay MG 4VENT, V6" ABOVE ROOF, (PYCSW) ZVENT (PvC~SW) Gwr (PvC-SW) FROM P SW) REM, [ ZCA (CPR) po ro Ue I St ERP Po 02-09-94 | I, ee oe a 2 ww (PYC-Sw) 0419-84 BER fOP_OF 1 1/Z SAMPLE TAP ZCA (CPR) peer [ee CI St (FRE) | 4 a = 4" OVERFLOW Drown BE Sp 4GWT (PvO-S) Ee Wu ep EFFLUENT I | OA tee oF wee t s'Gwu (FRP) hi ZA (CPR) TANK ToS STORAGE, 1-1/2 OW GWT (PvO~s var senate 7 | FLEXIBLE COUPLING-| EFFLUENT ZA Psi : STORAGE, (cpr) = INFLUENT Lozan VALVE 186" STORAGE oFG FLOWMETER FM3 EXTERIOR OFFICE AR TANK I-23 18'=6 SEE DETAL 1/25 DOOR COMPRESSOR: 5 : =~ EMERGENCY FARK: Se eee CONCENTRIC, REDUCING FLEXIBLE EVE-WASH (SOLATION H bee 47AIR_INTAKE(PC: Developed By MAC, ELC Approved By Revision: AN CROSS SECTION REVISIONS EXPANSION JOINT. AND SHOWER CONTROL WATER METER j{-- 1 VALVE FR)| CA PR METER: PANEL we : A COMPRESSOR: AR iY Ha il J AL (FRP) ao) P-6 | cv-3, rats TLE [ed rN SMANWAY Ti) CLEANOUT AHS | (ENCLOSED) Ht Lt _ | PUMP P-6 in | WATER METER POTABLE @-_ f'DRN_(Pvc-pa) 8 SAN (PVCOR) SEE NOTE 2 FLOOR SLEEVE ORAIN VALVE OI-15 83, 02-09-94 Lan Lrog CONTINE OL, FILTER: [h_ rp COMPRESSOR PENETRATION SLEEVE. SEE oF YATION 46 TRAP 4 ORN. (PYCDR) RP ! SEE NOTE 2 #'ORN (PvC-DR) - P | j VALVE: FOOT. CONCRETE SUMP 6 x 6 x 4'DEEP im AG e A \ELUMBING SECTION (Peo eae) & GERUMPING SECTION ROOF, (PYC~SW) NENT, PoE" ABOVE (2 PRM # GWT (PYC~SW) Ue SAMPLE fF CA (CPR) _ 1/Z'PRN (PYC~SH) | pee $e re Og TANK T- fh SUBMITTED FOR U.S. EPA INTERMEDIATE DESIGN REVIEW SUBMITTED FOR FINAL DESIGN REVIEW ZSLG RP) AL, (FRP) 1 2 EY : FILTER PRESS 4" OVERFLOW SEE NOTE 3 Aft _ PRM TNPW (PvC~ ZAILTRATE (Pvc SSL (FRP) (Pvc OVER HEAD. ! ORY POLYMER: EOUCTOR ZPILTRATE. ANFLUENT POTASSIUM (SEE NOTE 1) ae {PYC-SH) TANK T-! STORAGE PERMANGANATE| [ a I CABINETS 7 ee feed _ 4 TAU TE LUNES: i {Pve~SH) EMERGENCY EYE WASH AND AUTOMATIC. VALVE eg a = 1d | 18-5 SHOWER SALIRATE, Hy NaOH TOTE. (ve=Sh) TNPW W/HOSE BIB i POTASSIUM PERMANGANATE | 4#ORY DISCONNECT ee os 10-0" SANK Tot i | a (BRONZ vA [ SLUDGE SLUDGE DUMPSTER T ZCA (CPR) 1/ZPRM eco BY OWNER) 3 W-2 * ; 23 | [| | | | Rien! Pat i IH 4 zeroes HOT WATER TANK POLYMER WX TANK J-8 POWER WASHER OTO BLOG SUMP ct ban #DRN (PC-DR) POWER WASHER (PORTA TRENCH DRAIN versse om ro-amt tf (GY OWNER) 4#DRN (PVC~0R) FLOOR SLEEVE DO Lost edited: 94/04/20 @ 10:35 SEE NOTE 2 ae | | | TREATMENT PLUMBING SECTIONS REMEDIAL DESIGN KENTWOOD LANDFILL KENTWOOD, MICHIGAN (2\P 4 NG =f ON \27/ SCALE: 1 A G \ELUMBING SECTION Shaet Number NOTES 21 of 37 MOUNT DRY POLYMER EDUCTOR 4" ABOVE POLYMER TANK WITH SST UNISTRUT. : ALL FLOOR AND GRADE BEAM PENETRATIONS SHALL GE LINKSEAL Orewing Number | TYPE, SEE DETAN 8/26, 70241 D2t 3, SEE SHT D34 FOR PULL-DOWN STAIRS. 4. SEE SHT D20 FOR ROUTING OF POTABLE WATER, SANITARY, AND FLOOR DRAIN PIPING. + reer JIA 7O26T OOK CAST DESIONM\ REMT=024, Aa MC, WARZYN D41994 BER Dawe BF Sy SFG Developed PF MACJELC Apptered By Revsiom AX CORRECT CROSS SECTION (Gree Sencarta lh =OS-O3 [omen noven OL RE QIR| erent Ren, [Sea [ere eek RRS eres OE eer Me ea 1/ZNAOH (PYC-SH) 1/2 POLY (PvC-SW) ZCA (CPR) STNPW (PYC-S) pron (pvo-sw) O1~15-93 92-09-94 A FOP OF TANK _ | E 4 OVERFLOW (PVC-SW) 1-1/4" OW CABINETS POTASSIUM PERMANGANATE | @T-3 EFFLUENT nef |j~ SPVC CONTAINMENT S'HIGH PARTITION OWT (pvC-s} WALL, Ss wecHT ABOVE TANK MMT 3 J 1/2 PE TUBING EYEWASH AND ETERMINED BY MIXER; MANUFACTURER; SHOWER 4 CLARIFIER SELF REGULATING HEAT TRACE 7 J i 1S) SHIP'S ALUMINUM TAPE LADDER: CABLE 3 WATT PER FOOT ay a }- 2CA (CPR) COMPRESSOR EMERGENCY AR POTASSIUM ad, ~~ AR DRYER . SUBMITTED FOR U.S. EPA INTERMEDIATE DESIGN REVIEW SUBMITTED FOR FINAL DESIGN REVIEW CONNECTION fe PERMANGANATE. 1 2 TANK (COVERED): TH1 Z yeausTiC LINE HEAT TRACE Seat H OST. PIPE PUMP P-5 (Ox 10x 1/2 PLATE wl LA U/Zx WEDGE : (CHORS (TYP OF 4) NOTES 1 INSTALL CAUSTIC UNE INSIDE ZPVC PIPE, 2/3 DOWN FROM PLUMBIN! ECTION TANK TOP. VF 2. CONNECT wv GHU, 1/2 POLYMER FEED TO CLARIFIER INFLUENT . REMEDIAL DESIGN KENTWOOD LANDFILL KENTWOOD, MICHIGAN ? TREATMENT PLUMBING SECTION AND DETAIL Sheet Humber 22 of 37 Drawing Humber 70241 D22 perme: EA 7TD241 KKK CANT DESCH\KENT~O22.000 Last edited: 94/04/20 @ 10:57 i