Ten State Standards (Water)2003

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2003 EditionGreat Lakes - Upper Mississippi River Board of State and ProvincialPublic Health and Environmental Managers

Illinois Indiana Iowa Michigan Minnesota MissouriNew York Ohio Ontario Pennsylvania Wisconsin


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RecommendedStandardsFor Water Works2003 Edition

Policies for the Review and Approvalof Plans and Specifications for Public Water Supplies

A Report of the Water Supply Committee of theGreat Lakes--Upper Mississippi River Boardof State and Provincial Public Health and Environmental Managers

MEMBER STATES AND PROVINCEl1Iinois Indiana Iowa Michigan Minnesota MissouriNew York Ohio Ontario Pennsylvania Wisconsin

Copies available from:Health Educations ServicesPO Box 7126Albany, NY 1222451843972865184397022www.hes.org

Copyright 2003 by the Great Lakes Upper Mississippi River Board of State and ProvincialPublic Health and Environmental ManagersThis book, or portions thereof, may be reproduced without permission from the author if proper credit is given.


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TABLE OF CONTENTS

FOREWORD viiiPOLICY STATEMENT ON PRE-ENGiNEERED WATER TREATMENT PLANTS xPOLICY STATEMENT ON CONTROL OF ORGANIC CONTAMINATIONFOR PUBLIC WATER SUPPLIES xiiPOLICY STATEMENT ON INTERNAL CORROSIONCONTROL FOR PUBLIC WATER SUPPLIES xivPOLICY STATEMENT ON TRIHALOMETHANE REMOVAL AND CONTROLFOR PUBLIC WATER SUPPLIES xviPOLICY STATEMENT ON REVERSE OSMOSIS AND NANOFILTRATIONFOR PUBIC WATER SUPPLIES xviiiPOLICY STATEMENT ON AUTOMATED/UNATIENDED OPERATIONOF SURFACE WATER TREATMENT PLANTS xxPOLICY STATEMENT ON BAG AND CARTRIDGE FILTERS FORPUBLIC WATER SUPPLIES xxiiPOLICY STATEMENT ON CONTROL OF ZEBRA MUSSELS FORPUBLIC WATER SUPPLIES xxv

POLICY STATEMENT ON MICROFILTRATION ANDULTRAFILTRATION FOR PUBLIC WATER SUPPLIES xxviiPOLICY STATEMENT ON ULTRA VIOLET LIGHTFOR TREATMENT OF PUBLICWATER SUPPLIES xxixPOLICY STATEMENT ON INFRASTRUCTURE SECURITY FOR PUBLIC WATERSUPPLIES xxxiiINl:ERIM STANDARD - NITRATE REMOVAL USING SULFATE SELECTIVEANION EXCHANGE RESIN xxxivINTERIM STANDARD - USE OF CHLORAMINE DISINFECTANTFOR PUBLIC WATER SUPPLIES xxxvi

PART 1 - SUBMISSION OF PLANS1.0 GENERAL 11.1 ENGINEER'S REPORT 11.1.1 General Information 11.1.2 Extent of water works system 21.1.3 Justification of project 21.1.4 Soil, groundwater conditions, andfoundation problems 2

1.1.5 Water use data 21.1.6 Flow requirements 21.1.7 Sources of water supply 31.1.8 Proposed treatment processes 41.1.9 Sewerage system available 41.1.10 Waste disposal 41.1.11 Automation 41.1.12 Project sites 41.1.13 Financing 41.1.14 Future extensions 5

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PLANS1.2.1 General layout1.2.2 Detailed plansSPECIFICATIONSDESIGN CRITERIAREVISIONS TO APPROVED PLANSADDITIONAL INFORMATION REQUIRED

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PART 2 - GENERAL DESIGN CONSIDERATIONS2.0 GENERAL2.1 DESIGN BASIS2.2 PLANT LAYOUT2.3 BUILDING LAYOUT2.4 LOCATION OF STRUCTURES2.5 ELECTRICAL CONTROLS2.6 STANDBY POWER2.7 SHOP SPACE AND STORAGE2.8 LABORATORY FACILITIES

2.8.1 Testing equipment2.8.2 Physical facilities2.9 MONITORING EQUIPMENT2.10 SAMPLE TAPS2.11 FACILITY WATER SUPPLY2.12 WALL CASTINGS2.13 METERS2.14 PIPING COLOR CODE2.15 DISINFECTION2.16 OPERATION AND MAINTENANCE MANUAL2.17 OPERATOR INSTRUCTION2.18 SAFETY2.19 SECURITY2.20 FLOOD PROTECTION2.21 CHEMICALS AND WATER CONTACT MATERIALS2.22 OTHER CONSIDERATIONSPART 3 - SOURCE DEVELOPMENT3.0 GENERAL3.1 SURFACE WATER

3.1.1 Quantity3.1.2 Quality3.1.3 Minimum treatment3.1.4 Structures3.1.5 Impoundments and reservoirs3.2 GROUNDWATER3.2.1 Quantity.3.2.2 Quality3.2.3 Location3.2.4 Testing and records3.2.5 General well construction3.2.6 Aquifer types and construction methods Special conditions3.2.7 Well pumps, discharge piping and appurtenances

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PART 4 - TREATMENT4.0 GENERAL4.1 CLARIFICATION4.1.1 Presedimentation4.1.2 Rapid mix4.1.3 Flocculation4.1.4 Sedimentation4.1.5 Solids contact unit4.1.6 Tube or plate settlers4.1.7 High rate clarification processes4.2 FILTRATION4.2.1 Rapid rate gravity filters4.2.2 Rapid rate pressure filters4.2.3 Diatomaceous earth filtration4.2.4 Slow sand filters4.2.5 Direct filtration4.2.6 Deep bed rapid rate gravity filters4.2.7 Biologically active filters4.3 DISINFECTION4.3.1 Chlorination equipment4.3.2 Contact time and point of application4.3.3 Residual chlorine4.3.4 Testing equipment4.3.5 Chlorinator piping4.3.6 Housing4.3.7 Ozone4.3.8 Chlorine dioxide4.3.9 Ultra violet light4.3.10 Other disinfecting agents4.4 SOFTENING4.4.1 Lime or lime-soda process4.4.2 Cation exchange process4.4.3 Water quality test equipment4.5 AERATION4.5.1 Natural draft aeration4.5.2 Forced or induced draft aeration4.5.3 Spray aeration4.5.4 Pressure aeration4.5.5 Packed tower aeration4.5.6 Other methods of aeration4.5.7 Protection of aerators4.5.8 Disinfection4.5.9 Bypass4.5.10 Corrosion control4.5.11 Quality control4.6 IRON AND MANGANESE CONTROL4.6.1 Removal by oxidation, detention and filtration4.6.2 Removal by the lime-soda softening process4.6.3 Removal bymanganese coated media filtration4.6.4 Removal by ion exchange4.6.5 Biological removal4.6.6 Sequestration by polyphosphates4.6.7 Sequestration by sodium silicates

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4.6.8 Sampling taps4.6.9 Testing equipment shall be provided for all plants4.7 FLUORIDATION4.7.1 Fluoride compound storage4.7.2 Chemical feed equipment and methods4.7.3 Secondary controls4.7.4 Protective equipment4.7.5 Dust control4.7.6 Testing equipment4.8 STABILIZATION4.8.1 Carbon dioxide addition4.8.2 Acid addition4.8.3 Phosphates4.8.4 "Split treatment"4.8.5 Alkali feed4.8.6 Carbon dioxide reduction by aeration4.8.7 Other treatment4.8.8 Water unstable due to biochemical action

In distribution system4.8.9 Control4.9 TASTE AND ODOR CONTROL4.9.1 Flexibility4.9.2 Chlorination4.9.3 Chlorine dioxide4.9.4 Powdered activated carbon4.9.5 Granular activated carbon4.9.6 Copper sulfate and other copper compounds. 4.9.7 Aeration4.9.8 Potassium permanganate4.9.9 Ozone4.9.10 Other methods4.10 MICROSCREENING4.10.1 . Design

PART 5 - CHEMICAL APPLICATION5.0 GENERAL5.0.1 Plans and specifications5.0.2 Chemical application5.0.3 General equipment design

5.1 FACILITY DESIGN5.1.1 Number of feeders5.1.2 Control5.1.3 Dry chemical feeders5.1.4 Positive displacement solution pumps5.1.5 Liquid chemical feeders - siphon control5.1.6 Cross-connection control5.1.7 Chemical feed equipment location5.1.8 In-plant water supply5.1.9 Storage of chemicals5.1.10 Solution tanks5.1.11 Day tanks5.1.12 Feed lines5.1.13 Handling5.1.14 Housing

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5.2

5.3

5.4

CHEMICALS5.2.1 Shipping containers5.2.2 Specifications5.2.3 AssayOPERATOR SAFETY5.3.1 Ventilation5.3.2 Respiratory protection equipmeht5.3.3 Chlorine leak detection5.3.4 Protective equipmentSPECIFIC CHEMICALS5.4.1 Chlorine gas5.4.2 Acids and caustics5.4.3 Sodium chlorite for chlorine dioxide generation5.4.4 Sodium hypochlorite5.4.5 Ammonia

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PART 6 - PUMPING FACILITIES6.0 GENERAL6.1 LOCATION6.1.1 Site protection6.2 PUMPING STATIONS6.2.1 Suction well6.2.2 Equipment servicing6.2.3 Stairways and ladders6.2.4 Heating6.2.5 Ventilation6.2.6 Dehumidification6.2.7 Lighting6.2.8 Sanitary and other conveniences6.3 PUMPS6.3.1 Suction lift6.3.2 Priming6.4 BOOSTER PUMPS6.4.1 Duplicate pumps6.4.2 Metering6.4.3 Inline booster pumps6.4.4 Individual home booster pumps6.5 AUTOMATIC AND REMOTE CONTROLLED STATIONS6.6 APPURTENANCES6.6.1 Valves6.6.2 Piping6.6.3 Gauges and meters6.6.4 Water seals6.6.5 Controls6.6.6 Standby power6.6.7 Water pre-lubrication

PART 7 - FINISHEDWATER STORAGE7.0 GENERAL7.0.1 Sizing7.0.2 Location of reservoirs7.0.3 Protection from cohtamination

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7.0.4 Protection from trespassers7.0.5 Drains(.0.6 SloredWaterTurnover7.0.7 Overflow7.0.8 Access7.0.9 Vents7.0.10 Roof and sidewali7.0.11 Construction materials7.0.12 Safety7.0.13 Freezing7.0.14 Internal catwalk7.0.15 Silt stop7.0.16 Grading7.0.17 Painting and/or cathodic protection7.0.18 Disinfection7.0.19 Provisions for sampling

7.1 TREATMENT PLANT STORAGE7.1.1 Filter washwater tanks7.1.2 Clearweli7.1.3 Adjacent storage7.1.4 Other treatment plant storage tanks7.2' HYDROPNEUMATIC TANK SYSTEMS

7.2.1 Location7.2.2 System sizing7.2.3 Piping7.2.4 Appurtenances7.3 DISTRIBUTION SYSTEM STORAGE7.3.1 Pressures7.3.2 Drainage7.3.3 Level controls

PART 8 - DISTRIBUTION SYSTEM PIPiNG AND APPURTENANCES

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GENERALMATERIALS8.1.1 Standards and material selection8.1.2 Permeation by organic compounds8.1.3 Used materials8.1.4 JointsSYSTEM DESiGN8.2.1 Pressure8.2.2 Diameter8.2.3 Fire protection8.2.4 Dead endsVALVESHYDRANTS8.4.1 Location and spacing8.4.2 Valves and nozzies8.4.3 Hydrant leads8.4.4 Hydrant drainageAIR RELIEF VALVES8.5.1 Air relief vaives8.5.2 Air relief valve pipingVALVE, METER AND BLOW-OFF CHAMBERS

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8.7 INSTALLATION OF WATERMAINS8.7.1 Standards8.7.2 Bedding8.7.3 Cover8.7.4 Blocking8.7.5 Pressure and leakage testing8.7.6 Disinfection8.7.7 External corrosion

8.8 SEPARATION DISTANCES FROM CONTAMINATION SOURCES8.8.1 General8.8.2 Parallel installation8.8.3 Crossings8.8.4 Exception8.8.5 Force mains8.8.6 Sewer manholes8.8.7 Separation of water mains from other sources of contamination8.9 SURFACE WATER CROSSINGS8.9.1 Above-water crossings8.9.2 Underwater crossings8.10 CROSS-CONNECTIONS AND INTERCONNECTIONS8.10.1 Cross-connections8.10.2 Cooling water8.10.3 Interconnections8.11 WATER SERVICES AND PLUMBING8.11.1 Plumbing8.11.2 Booster pumps8.12 SERVICE METERS8.13 WATER LOADING STATIONS

PART 9 - WASTE RESIDUALS9.0 GENERAL9.1 SANITARY WASTE9.2 BRINE WASTE9.3 PRECIPITATIVE SOFTENING SLUDGE9.4 ALUM SLUDGE

9.4.1 Lagoons9.4.2 Mechanical dewatering9.4.3 Land application9.5 "RED WATER" WASTE9.5.1 Sand filters9.5.2 Lagoons9.5.3 Discharge to community sanitary sewer9.5.4 Recycling "red water" wastes9.6 WASTE FILTER WASH WATER9.7 RADIOACTIVE MATERIALS

FIGURE 1 - SUGGESTED FILLING DEVICE FOR WATERLOADING STATIONSTABLE 1 - STEEL PIPE

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FOREWORD

Th G eat Lakes-Upper Mississippi River Board of State and Provincial Public Health and EnvironmentalM ea;ers in 1950 created a Water Supply Committee consisting of one associate from each stater e ~ ~ e s e n t e d on the Board. A representative from the Province of Ontario was added in 1978. Throughoutthis document the term state shall mean a representative state or the Province of Ontario. The Committeewas assigned the responsibility for reviewing existing water works practices, policies, and procedures, andreporting its findings to the Board. The report of the Water Supply Committee was first published in 1953,and subsequently has been revised and published in 1962, 1968, 1976,1982,1987,1992,1997, and2003.This document includes the following:1. Policy Statements - Preceding the standards are policy statements of the Board concerning waterworks design, practice, or resource protection. Some policy statements recommend an approach tothe investigation of innovative treatment processes which have not been included as part of thestandards because sufficient confirmation has not yet been documented to allow the establishment ofspecific limitations or design parameters. Other policy statements recommend approaches,alternatives or considerations in addressing a specific water supply issue and may not develop intostandards.2. Interim Standards - Following the policy statements are interim standards. The interim standards givedesign criteria which are currently being used for new treatment processes, but the use of the criteria

is limited and insufficient for recognition as a recommended standard.3. Recommended Standards - The Standards, consisting of proven technology, are intended to serve asa guide in the design and preparation of plans and specifications for pUblic water supply systems, tosuggest limiting values for items upon which an evaluation of such plans and specifications may bemade by the reviewing authority, and to establish, as far as practicable: uniformity of practice.Because statutory requirements and legal authority pertaining to public water supplies are not uniformamong the states, and since conditions and administrative procedures and policies also differ, the useof these standards must be adjusted to these variations.The terms shall and must are used where practice is sufficiently standardized to permit specific delineationof requirements or where safeguarding of the public health justifies such definite action. Other terms, suchas should, recommended, and preferred, indicate desirable procedures or methods, with deviationssubject to individual consideration.Most quantified items in this document are cited in US customary units and are rounded off at twosignificant figures. Metric equivalent quantities, also rounded off at two significant figures, follow inbrackets where compound units are involved. The metric unit symbols follow International Systemconventions. In the event of a conflict between quantities in US units and the metric equivalent thequantity in US units shall take precedence.It is not possible to cover recently developed processes and equipment in a pUblication of this type.However, the policy is to encourage, rather than obstruct, the development of new processes andequipment. Recent developments may be acceptable to individual states if they meet at least one of thefollowing conditions: 1) have been thoroughly tested in full scale comparable installations undercompetent supervision, 2) have been thoroughly tested as a pilot plant operated for a sufficient time toindicate satisfactory performance, or 3) a performance bond or other acceptable arrangement has beenmade so the owners or official custodians are adequately protected financially or otherwise in case offailure of the process or equipment.

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The Board recognizes that many states, other than those of the Great Lakes-Upper Mississippi RiverBoard of State and Provincial Public Health and Environmental Managers, uliiize this publication as part oftheir design requirements for water works facilit ies. The Board welcomes this practice as long as credit isgiven to the Board and to this publication as a source for the standards adopted. Suggestions fromnon-member states are welcome and will be considered.Adopted April, 1997

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POLICY STATEMENTONPRE-ENGINEERED WATER TREATMENT PLANTS

Pre-engineered water treatment plants are becoming available and being used for production of potablewater at public water systems. Many applications being proposed are for smallsystems having relativelyclean surface water sources which are now being required to provide filtration underthefederal SafeDrinking Water Act.Pre-engineered water treatment plants are normally modular process units which are pre-designed forspecific process applications and flow rates and purchased as a package. Multipie units may be installedin parallel to accommodate iarger flows. .Pre-engineered treatment plants have numerous applications but are especially applicable at smallsystems where conventional treatment may not be cost effective. As with any design the proposedtreatment must fit the situation and assure a continuous supply of safe drinking water for waterconsumers. The reviewing authority may accept proposals for pre-engineered water treatment plants on acase by case basis where they have been demonstrated to be effective in treating the source water beingused.Factors to be considered include:1. Raw water quality characteristics under normal and worst case conditions. Seasonal fluctuationsmust be evaluated and considered in the design.2. Demonstration of treatment effectiveness under all raw water conditions and system flow demands.This demonstration may be on-site pilot or full scaie testing or testing off-site where the source wateris of similar quality. On-site testing is required at sites haVing questionable water quality orapplicability of the treatment process. The proposed demonstration project must be approved by thereviewing authority prior to starting.3. Sophistication of equipment. The reliability and experience record of the proposed treatmentequipment and controls must be evaluated.4. Unit process fleXibility which allows for optimization of treatment.5. Operational oversight that is necessary. At surface water sources full-time operators are necessary,except where the reviewing authority has approved an automation plan. See POlicy Statement onAutomated/Unattended Operation of Surface Water Treatment Plants.6. Third party certification or approvals such as National Sanitation Foundation (NSF) for a) treatmentequipment and b) materials that will be in contact with the water.7. Suitable pretreatment based on raw water quality and the pilot study or other demonstration oftreatment effectiveness.8. Factory testing of controls and process equipment prior to shipment.9. Automated troubleshooting capability built into the control system.10. Start-up and follow-up training and troubleshooting to be provided by the manufacturer or contractor.

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11. Operation and maintenance manual. This manual must provide a description of the treatment, controland pumping equipment, necessary maintenance and schedule, and a troubleshooting guide fortypical problems.12. On-site and contractual laboratory capability. The on-site testing must include all required continuousand daily testing as specified by the reviewing authority. Contract testing may be considered for otherparameters.13. Manufacturers warranty and replacement guarantee. Appropriate safeguards for the water supplier

must be included in contract documents. The reviewing authority may consider interim or conditionalproject approvals for innovative technology where there is sufficient demonstration of treatmenteffectiveness and contract provisions to protect the water supplier should the treatment not perform asclaimed.14. Water supplier revenue and bUdget for continuing operations, maintenance and equipmentreplacement in the future.Additional information on this topic is given in the State Alternative Technology Approval Protocol datedJune, 1996 which was developed by the Association of State Drinking Water Administrators, U.S.Environmental Protection Agency and various industry groups.Adopted April, 1997

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POLICY STATEMENTONCONTROL OF ORGANIC CONTAMINATIONFORPUBLICWATER SUPPLIES

Although standards and advisories for organics are being developed, there have been numerous cases oforganic contamination of public water supply sources. In all cases, pUblic expOsure to organiccontamination must be minimized. There is insufficient experience to establish design standards whichwould apply to all situations. Controlling organic contamination is an area of design that requires pilotstudies and early consultation with the reviewing authority. Where treatment is prdposed, best availabletechnology shall be provided to reduce organic contaminants to the lowest practical levels. Operationsand monitoring must also be considered in selecting the best alternative. The following alternatives maybe applicable:1. Alternate Source Development2. Existing Treatment Modifications3. Air Stripping For Volatile Organics

(See 4.5.4 Packed Tower Aeration)4. Granular Activated Carbon

Consideration should be given to:a. using contact units rather than replacing portion of existing filter media;b. series and parallel flow piping configurations to minimize the effect of breakthrough withoutreliance on continuous monitoring; .c. providing at least two units. Where only two units are provided, each shall be capable of meetingthe plant design capacity (normally the projected maximum daily


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1. For organic contaminants found in surface water sources:a. type of organic chemicals, sources, concentration, frequency of occurrence, water pollutionabatement schedule, etc.,b. possible existing treatment plant modifications to lower organic chemical levels. Results of bench,pilot or full scale testing demonstrating treatment alternatives, effectiveness and costs,c. a determination of the quality and/or operational parameters which serve as the best

measurement of treatment performance, and a corresponding monitoring and process controlprogram.2. For organic contamination found in groundwater sources:

a. types of organic chemicals, sources, concentration, estimate of residence lime within the aquifer,plume delineation, flow characteristics, water pollution abatement schedUle, etc.,b. results of bench or pilot studies demonstrating treatment alternatives, effectiveness, and costs,c. a determination of the quality and/or operational parameters which serve as the best measure oftreatment performance, and a corresponding monitoring and process control program,d. development and implementation of a wellhead protection plan.

The collection of this type of data is often complicated and lengthy. Permanent engineering solutions willtake significant time to develop. The cost of organic analyses and the availability of acceptablelaboratories may further complicate both pilot work and actual operation.Alternative source development or purchase of water from nearby unaffected systems may be a moreexpedient solution for contaminated groundwater sources.Adopted April, 1987Revised April, 1991Revised April, 1997

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POLICY STATEMENTONINTERNAL CORROSION CONTROLFORPUBLIC WATER SUPPLIES

Internal and external corrosion of a public water supply distribution system is a recognized problem thatcannot be completely eliminated but can be effectively controlled. Aside from the economic and aestheticproblems, the possible adverse health effects of corrosion products, such as lead and copper, is a majorconsideration. See section 8.5.7 for external corrosion control.Corrosion Df metallic pipes is a chemical oxidatiDn process which requires that both water and an Dxidizingagent be present at metal surfaces. The process is driven by the energy released when atoms from themetal surface are cDnverted intD hydrated metal catiDns. The three main factDrs which can acceleratecDrrDsiDn are:a) failure Df the water chemistry to provide a cDherent protecting film of cDrrosiDn products Dn themetal surface,b) increased biofilm activity as a result of loss of the regular cDntrolling disinfectant residual, andc) direct electricai contact between different metals in the presence of high conductance water.Control Dfcorrosion is a function of the design, maintenance, and operation of a public water supply.These functions must be considered simultaneously in order for the corrosion control prDgram to functionproperly. Corrosion problems must be solved on an individual basis depending on the specific waterquality characteristics and materials used in the distribution system. Specific information can be obtainedfrom publications of technical agencies and associations such as USEPA (Corrosion Manual for InternalCorrosion of Water Distribution Systems, 1984; Control of Lead and Copper in Drinking Water,_1993; Leadand Copper Regulations, 1994) and the American Water Works Association (Lead and Copper Strategies,1990; Chemistry of Corrosion Inhibitors in Potable Waters, 1990; Internal Corrosion of Water DistributionSystems, 2" ' edition, 1996) BrDad areas Df cDnsideratiDn for a cDrrosion cDntrol program foliDw.Internal CDrrosion1. Provide fDr a system Df records bywhich the nature and frequency Df cDrrosion problems arerecDrded. On a plat map of the distribution system, show the IDcatiDn Df each problem SD thatfollDw-up investigations and improvements can be made when a cluster Df problems is identified.2. When complaints are received frDm a customer, follDw up with an inspectiDn by experiencedpersDnnel or consultant experienced in corrosion cDntrol. Where advisable, Dbtain samples Df waterusing appropriate sampling protocols fDr chemical and micrDbiDlogical analyses and piping andplumbing material samples. Analyses shDuld be made tD determine the type and, if pDssible, thecause Df the cDrrDsiDn.3. Establish a program or cDnduct desktop analyses Dr pipe IDDp studies to determine the cDrrosivenessDf the water in representative parts Df the distributiDn system. Analysis fDr alkalinity, pH, temperature,calcium, specific cDnductance or total dissolved solids, chlorides, sulfates and corrosion products(such as lead, cadmium, copper, zinc and iron) shDuld be performed on water samples collected atthe treatment plant or wellhead and at representative pDints Dn the distribution system including firstdraw samples taken after the water had sat Dvernight at IDcations where lead-soldered copper internalplumbing is in use. By comparing the analyses Df the SDurce water with the distribution system water,significant changes in alkalinity, pH, or cDrrosion products would indicate that cDrrosion may be takingplace and thereby indicate that corrective steps may need to be taken.

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4. Where possible, especially when corrosion has been detected provide a program that will measureboth the physical and chemical aspects of the corrosion phenomena. Physical measurement of therate of corrosion can be made by the use of coupons, easily removed sections of pipe, connectedflow-through pipe test sections or other piping arrangements. At the same site, estimate the relativedegree of corrosivity on a routine basis by using desktop analyses or corrosion indices such as theLangelier Index, Ryznar Index, calcium carbonate precipitation potential or Aggressiveness Index(AWWA C-400). Correlation of the data from the physical measurement with the data from theselected corrosion analysis may provide information to determine the type of corrective treatmentneeded (though the different indices may not always agree) and nay ailow for the subsequent use ofthe corrosion analysis alone to determine the degree of corrosivity in select areas of the distributionsystem.

5. If corrosion is found to exist throughout the distribution system, corrective measures at the treatmentplant, pump station or well head should be initiated. A chemical feed can be made to provide a stableto slightly depositing water or water quality which mitigates the soiubility of targeted parameters. Incalculating the stability index and the corresponding chemical feed adjustments, consideration mustbe given to items such as the water temperature, if it varies with the season and within various parts ofthe distribution system; the velocity of flow within various parts of the distribution system; the degree ofstability needed by the individual customer; and the dissolved oxygen content of distributed water,especially in waters having low hardness and alkalinity. Threshold treatment involving the feeding of aortho- or blended phosphate or a silicate to control corrosion may be considered for both ground andsurface water supplies.6. Additional control of corrosion problems can be obtained by a regulation or ordinance for the materialsused in or connected to a distribution system. Careful selection of materials compatible with thephysical system or the water being delivered can aid in reduction of corrosion product production.Note: Adjustment of pH for corrosion control must not interfere with other pH dependent processes (e.g.,color removal by alum coagulation) or aggravate other water quality parameters (e.g., THM formation). Inaddition, the use of ortho- or blended phosphates should not aggravate distribution microbial concerns oradversely impact wastewater facilities.Adopted April, 1982Revised April, 1997Revised April, 2003

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POLICY STATEMENTONTRIHALOMETHANE REMOVAL AND CONTROLFORPUBLIC WATER SUPPLIESTrihalomethanes (THMs) are formed when free chlorine reacts with organic substances, most of whichoccur naturally. These organic substances (called "precursors"), are a complex and variable mixture ofcompounds. Formation of THMs is dependent on such factors as amount and type of chlorine used,temperature, concentration of precursors, pH, and contact time. Approaches for controlling THMs include:1. Control of precursors at the source.

a. Selective withdrawal from reservoirs -- varying depths may contain lower conbentrations ofprecursors at different times of the year.b. Plankton Control -- Algae and their by-products have been shown to act as THM precursors.c. Alternative sources of water may be considered, where available.

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4. Use of Alternative Disinfectants -- Disinfectants that react less with THM precursors may be used aslong as microbiological quality of the finished water is maintained. Alternative disinfectants may beless effective than free chlorine, particularly with vinuses and parasites. Alternative disinfectants,when used, must be capable of providing an adequate distribution system residual. Possible healtheffects of by-products that may be produced by using alternative disinfectants must be taken intoconsideration. The following alternative disinfectants may be used:a. Chlorine Dioxideb. Chloraminesc. Ozone

Using various combinations of THM controls and removal techniques may be more effective than a singlecontrol or a treatment method.Any modifications to eXisting treatment process must be approved by the reviewing authority. Pilot plantstudies are desirable.Adopted April, 1987Revised April, 1997

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POLICY STATEMENTONREVERSE OSMOSIS AND NANOFILTRATIONFORPUBLIC WATER SUPPLIESReverse osmosis (RO) is a physical process in which a suitably pretreated water is delivered at moderatepressures against a semipermeable membrane. The membrane rejects most solute ions and molecules.while allowing water of very low mineral content to pass through. The process produces a concentratedwaste stream in addition to the clear permeate product. Reverse osmosis systems have beensuccessfully applied to saline ground waters, brackish waters, and seawater, as well as for inorganiccontaminants such as radionuclides, nitrates, arsenic, etc. and other contaminants such as pesticides,viruses, bacteria and protozoa. A lower pressure RO called nanofiltration (NF), also known as membranesoftening, has been successfully utilized for hard, high color and high organic content feed waters. NFhas a lower monovalent ion rejection, making it more attractive to water with low salinity, thereby reducingpost treatment and conditioning as compared to RO.The following items should be considered in evaluating the applicability for reverse osmosis andnanofiltration:1. Membrane Selection: Two types of membranes are typically used. These are cellulose acetate basedand polyamide composites. Membrane configurations typically include tubular, spiral wound andhollow fiber. Operational conditions and useful life vary depending on type of membrane selected,

quality of feed water, and process operating parameters.2. Useful Life of the Membrane: The membrane replacement represents a major cost component in theoverall water production costs. Membrane replacement frequency can significantly affect the overallcost of operating the treatment facility. Power consumption may also be a significant cost factor forRO plants.3. Pretreatment Requirements: Acceptable feedwater characteristics are dependent on the type ofmembrane and operational parameters of the system. Without suitable pretreatment or acceptablefeed water quality, the membrane may become fouled or scaled and consequently shorten its usefullife. Pretreatment is usually needed for turbidity reduction, iron or manganese removal, stabilization ofthe water to prevent scale formation, microbial control, chlorine removal (for certain membrane types),and pH adjustment. Usually, at a minimum, cartridge filters should be provided for the protection ofthe membranes against particulate matter.4. Treatment Efficiency: RO is highly efficient in removing metallic salts and ions from the raw water.Efficiencies, however, do vary depending on the ion being removed and the membrane utilized. Formost commonly encountered ions, removal efficiencies will range from 85% to over 99%. Organicsremoval is dependent on the molecular weight, shape and charge of the organic molecule and thepore size of the membrane util ized. Removal efficiencies may range from as high as 99% to less than30%, depending on the membrane type and treatment objective.5. Bypass Water: RO permeate will be virtually demineralized. NF permeate may also contain lessdissolved minerals than desirable. The design should provide for a portion of the raw water to bypassthe unit to maintain a stable water within the distribution system and to improve process economics aslong as the raw water does not contain unacceptable contaminants. Alternative filtration is requiredfor bypassed surface water or ground water under the direct influence of surface water.6. Post Treatment: Post treatment typically includes degasification for carbon dioxide (if excessive) andhydrogen sulfide removal (if present), pH and hardness adjustment for corrosion control anddisinfection as a secondary pathogen controi and for distribution system protection.7. Reject Water: Reject water may range from 10% to 50% of the raw water pumped to the reverseosmosis unit. For most brackish waters and ionic contaminant removal applications, reject is in the10-25% range while for seawater it could be as high as 50%. The reject volume shoUld be evaluatedin terms of the source availability and from the waste treatment availabilities. The amount of reject

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POLICY STATEMENT ONAUTOMATED/UNATTE:NDED OPERATION Of'" SURFACE WATER TREATMENT PLANTSR t 'd'" 'In computer technology equipment controls and Supervisory Control and Dataecen avances . , ... ' t' (SCADA) Systems have brought automated and off-site operation of surface water treatmentCqUISI Ion . , II th' t t' h d fI t . t th realm of feasibiiity. COJncldenta y, IS comes a a Ime w en renewe concern ore ~ sb!nlo 9 i c ~ 1 contamination is driving optimization of surface water treatment plant facilities and~ ~ ~ ~ ~ t i ~ n ~ a n d finished w ~ t ~ r treatment goals are being lowered to levels of


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9. Operations manual which gives operators step by step procedures for understanding and using theautomated control system under all water quality conditions. Emergency operations during power orcommunications failures or other emergencies must be included.10. A plan for a 6 month or more demonstration period to prove the reliability of procedures, equipmentand sUNeiliance system. A certified operator must be on-duty during the demonstration period. Thefinal plan must identify and address any problems and alarms that occurred during the demonstrationperiod. Challenge testing of each critical component of the overall system must be included as part ofthe demonstration project.11. Schedule for maintenance of equipment and critical parts replacement.12. Sufficient finished water storage shall be provided to meet system demands and CT requirementswhenever normal treatment production is interrupted as the result of automation system failure or plantshutdown.13. Sufficient staffing must be provided to carry out daily on-site evaluations, operational functions andneeded maintenance and calibration of all critical treatment components and monitoring equipment toensure reliability of operations.14. Plant staff must perform as a minimum weekly checks on the communication and control system toensure reliability of operations. Challenge testing of such equipment should be part of normalmaintenance routines.15. Provisions must be made to ensure security of the treatment facilities at all times. Incorporation ofappropriate intrusion alarms must be provided which are effectively communicated to the operator incharge.Adopted April, 1997

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POLICY STATEMENTONBAG AND CARTRIDGE FILTERSFORPUBLIC WATER SUPPLIESBag and cartridge technology has been used for some time in the food, pharmaceutical and industrialapplications. This technology is increasingly being used by small publiC water supplies for treatment ofdrinking water. A number of states have accepted bag and cartridge technology as an alternatetechnology for compliance with the filtration requirements of the SurfaCe Water Treatment Rule.The particulate loading capacity of these filters is iow, and once expended the bag or cartridge filter mustbe discarded. This technology is designed to meet the low flow requirement needs of small systems. Theoperational and maintenance cost of bag and cartridge replacement must be considered when designing asystem. These filters can effectively remove particles from water in the size range of Giardia cysts (5-10microns) and Cryptosporidium (2-5 microns).At the present time, filtration evaluation is based on Giardia cyst removal. However, consideration shouldbe given to the bag or cartridge filters ability to remove particles in the size range of Cryptosporidium sincethis is a current public health concern.With this type of treatment there is no alteration of water chemistry. So, once the technology hasdemonstrated the required removal efficiency, no further pilot demonstration may be necessary. Thedemonstration of f iltration is specific to a specific housing and a specific bag or cartridge filter. Any othercombinations of different bags, cartridges, or housings will require additional demonstration of filterefficiency.Treatment of a surface water should include source water protection, filtration, and disinfection.The following items should be considered in evaluating the applicability of bag or cartridge fiitration.

Predesign/Design1. The filter housing and bag/cartridge filter must demonstrate a filter efficiency of at least 2-log reductionin particles size 2 micron and above. Demonstration of higher log removals may be required by thereviewing authority depending on raw water quality and other treatment steps to be employed. The

reviewing authority will decide whether or not a pilot demonstration is necessary for each installation.This filtration efficiency may be accomplished by:a. Microscopic particulate analysis, including particle counting, sizing and identification, whichdetermines occurrence and removals of micro-organisms and other particle across a filter arsystem under ambient raw water source condition, Or when artificially challenged.b. Giardia/Cryptosporidium surrogate particle removal evaluation in accordancewith proceduresspecified in NSF Standard 53 or equivalent. These evaluations can be conducted by NSF or byanother third-party whose certification would be acceptable to the reviewing authority.c. "Particle Size Analysis Demonstration for Giardia Cyst Removal Credit" procedure presented inAppendix M of the EPA Surface Water Treatment Rule Guidance Manual.d. "Nonconsensus" live Giardia challenge studies that have been designed and carried out by athird-party agent recognized and accepted by the reviewing authority for interim evaluations. Atthe present time uniform protocol procedures for live Giardia challenge studies have not beenestablished. If a liVe Giardia challenge study is performed on site there must be proper crossconnection control equipment in place and the test portion must be operated to waste.e. Methods other than these that are approved by the reviewing authority.

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2. System components such as housing, bags, cartridges, membranes, gaskets, and O-rings should beevaluated under NSF Standard 61 or equivalent, for leaching of contaminants. Additional testing maybe required by the reviewing authority.3. The source water or pre-treated water should have a turbidity less than 5 NTU.4. The flow rate through the treatment process shall be monitored with a flow valve and meter. The flowrate through the bag/cartridge filter must not exceed 20 gpm, unless documentation at higher flowrates demonstrates that it will meet the requirements for removal of particles.5. Pretreatment is strongly recommended (if not required by the reviewing authority). This is to provide amore constant water quality to the bag/cartridge filter and to extend bag and cartridge life. Examples ofpretreatment include media filters, iarger opening bag/cartridge filters, infiltration galleries, and beachwells. Location of the water intake should be considered in the pretreatment evaluation.6. Particle count analysis can be used to determine what level of pretreatment should be provided. Itshould be noted that particulate counting is a 'snap shot' in time and that there can be seasonalvariations such as algae blooms, lake turnover, spring runoff, and heavy rainfall events that will givevaried water quality.7. It is recommended that chlorine or another disinfectant be added at the head of the treatment processto reduce/eliminate the growth of algae, bacteria, etc., on the filters. The impact on disinfection-by

product formation should be considered.8. A filter to waste component is strongly recommended (if not required by the reviewing authority), forany pretreatment pressure sand filters. At the beginning of each filter cycle and/or after everybackwash of the prefilters a set amount of water should be discharged to waste before water flowsinto the bag/cartridge filter. Filter to waste shall be provided for the final fi lter(s) and a set amount ofwater shall be discharged to waste after changing the filters.9. If pressure media filters are used for pretreatment they must be designed according to Section 4.2.2.10. A sampling tap shall be provided ahead of any treatment so a source water sample can be collected.11. Pressure gages and sampling taps shall be installed before and after the media filter and before andafter the bag/cartridge filter.12. An automatic air release valve shall be installed on top of the filter housing.13. Frequent start and stop operation of the bag or cartridge fllter should be avoided. To avoid thisfrequent start and stop cycle the following options are recommended:

a. a slow opening and closing valve ahead of the filter to reduce flow surges.b. reduce the flow through bag or cartridge filter to as low as possible to lengthen filter run times.c. install a recirculating pump that pumps treated water back to a point ahead of the bag or cartridgefilter. Care must be taken to make sure there is no cross connection between the finished waterand raw water.

14. A minimum of two bag or cartridge filter housings should be provided forwater systems that mustprovide water continuously.15. A pressure relief valve should be incorporated into the bag or cartridge filter housing.16. Complete automation of the treatment system is not required. Automation of the treatment plantshould be incorporated into the ability of the water system to monitor the finished water quality. It isimportant that a qualified water operator is available to run the treatment plant.17. A plan of action should be in place should the water quality parameters fall to meet EPA or the localreViewing authorities standards.

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Operations1. The filtration and backwash rates shall be monitored so that the prefilters are being optimally used.2. The bag and cartridge filters must be replaced when a pressure difference of 30 psi or other pressuredifference recommended by the manufacturer is observed. It should be noted that bag filters do notload linearly. Additional observation of the filter performance is required near the end of the filter run.3. Maintenance (o-ring replacement) shall be performed in accordance with the manufacturersrecommendations.4. Sterile rubber gloves and a disposable face mask covering the nose and mouth shall be worn whenreplacing or cleaning the cartridge or bag filters.5. The filter system shall be properly disinfected and water shall be ran to waste each time the cartridgeor bag filter vessels are opened for maintenance.6. The following parameters should be monitored:

Flow rate, instantaneousFlow rate, totalOperating pressurePressure differentialTurbidity

Adopted April, 1997Revised April, 2003

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POLICY STATEMENTONCONTROL OF ZEBRAMUSSELSFORPUBLIC WATER SUPPLIES

The zebra mussel (Dreissena polymorpha) is a freshwater bivalve that was believed to have beenaccidentally introduced into the Great Lakes ecosystem around 1986. The zebra mussel has the potentialto biofoul public water supply intake facilities and cause loss of intake capacity as well as contribute totaste and odor problems. The zebra mussel has spread rapidly throughout the Great Lakes andMississippiRiver Basins and could potentially affect surface water supplies throughout the country.The zebra mussel breeds prolifically in waters with temperatures between 45-52 degrees Fahrenheit withthe larval, or veliger, stage being highly mobile in water currents. The post veligers settle out and attachthemselves to a hard substrate (such as an intake structure) where they become adults; reaching sizes upto two inches. Many common construction materials can serve as substrates on which the mussels canbuild onto themselves and form deep layers within a few seasons.Water suppliers should periodically assess the condition of their intakes to determine if zebra musselveligers or adults are or potentially may be present and implement a system of control. Physical controlstypically include removal of adults by mechanical scraping (pigging) and hydroblasting; whereas chemicaltreatment has proven to be most effective for short and long term control and elimination.The most accepted and currently recommended forms of chemical treatment for public water supplies arethe use of oxidants such as chlorine, chlorine dioxide, potassium permanganate and ozone. Variousapproved molluscicides have also been used. Chemical dosages are typically applied at the intakethrough solution piping and a diffuser to prevent the formation of zebra mussel colonies within the intakeand piping. The type of chemical selected and frequency of application will depend on the type of existingchemical treatment facilities, zebra mussel breeding season, potential for THM formation, otherpretreatment objectives such as taste and odor control, safety and economy.The follOWing i tems should be addressed in the design:1. Chemical treatment design shall be in accordance with applicable sections of RecommendedStandards ForWater Works and shall be acceptable to the reViewing authority.2. Plant safety items, including but not limited to ventilation, operator protective equipment,eyewashes/showers, cross connection control, etc., shall be provided.3. Solution piping and diffusers shall be positively anchored. Piping shall have appropriate valving andshall be preferably installed within the intake pipe or in a suitable carrier pipe. Provisions shall be.made to prevent dispersal of chemical into the water environment outside the intake. Diffusers shallbe located and designed to protect all intake structure components.4. Consideration shall be given to providing a spare solution line to provide redundancy and to facilitatethe use of alternate chemicals.5. Chemical feeders shall be interlocked with plant system controls to shut down automatically when raw

water flows stop.6. Provisions for obtaining raw water samples not influenced by chemical treatment.

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7. When alternative control methods are proposed, for example, sonic energy, non-adhering surfaces orinfiltration galleries, appropriate piloting or demonstration studies, satisfactory to the reviewingauthority, should be considered.All designs of zebra mussel control systems shall be submitted to and receive the approval of thereviewing authority prior to installation.Adopted April 1997

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POLICY STATEMENTONMICROFILTRATION AND ULTRAFILTRATIONFORPUBLIC WATER SUPPLIES

Low pressure membrane filtration technology has emerged as a viable option for addressing current andfuture drinking water regulations related to treatment of surface water sources and groundwater under thedirect influence of surface water s')urces. Recent research and applied full scale facilities havedemonstrated the efficient performance of both Microfiltration (MF) and Ultrafiltration (UF) as feasibletreatment alternatives to traditional granular media processes. Both MF and UF have been shown to beeffective in removing identified parameters of the Surface Water Treatment Rule, such as: giardia,cryptosporidium, bacteria, turbidity and possibly viruses (for UF). The followil")g provides a briefdescription and characteristics of each process as well as general selection and design considerations.Characteristics: MF and UF membranes are most commonlymade from organic polymers such as:cellulose acetate, polysulfones, polyamides, polypropylene, polycarbonates and polyvinylidene fluoride(PVDF). The physical configurations includes hollow-fiber, spiral wound and tubular. MF membranes arecapable of removing particles with sizes down to 0.1-0.2 microns. UF processes have a lower cutoff ratingof .005-.01 microns.Typical flux (rate of f inished water permeate per unit membrane surface area) at 20 degrees C for MFranges between 50-100 gallons/sq.ft.lday (gsfd) whereas the typical UF flux range is 10-50 gsfd.Required operating pressures ranges from 5-10 psi for MF and 7-50 psi for UFoSince both processes have reiatively small membrane pore sizes, membrane fouling, caused by organicand inorganic compounds as well as physical contaminants, can occur if the system is not properlyselected or operated. Automated periodic back flushing and cleaning is employed on a timed basis oronce a targeted transmembrane pressure differential has been reached. Some systems utilize air/waterback flush. Typical cleaning agents utilized include acids, bases, complexing agents, surfactants,enzymes and certain oxidants, depending upon membrane material and foulants encountered. Chemicalsused for cleaning and the method and procedure of cleaning process must be acceptable to themembrane manufacturer and approved by the reviewing authority.Overall treatment requirements and disinfection credits must be discussed with and approved by thereviewing authority. Disinfection is required with membrane filtration for additional pathogen control anddistribution system protection.Selection and Design Considerations:1. A review of historical source raw water quality data, including turbidity and/or particle counts, seasonalchanges, organic loading, microbial activity, and temperature differentials as well as other inorganicand physical parameters should be conducted. The data should be used to determine feasibility andcost of the system. The degree of pre-treatment may also be ascertained from the data. Designconsiderations and membrane selection at this phase must also address the issue of target removalefficiencies and system recovery versus acceptable transmembrane pressure differentials. Onsurface water supplies, pre-screening or cartridge filters may be required.2. Prior to initiating the design of a MF or UF treatment facility, the state reviewing authority should becontacted to determine if a pilot plant study will be reqUired. In most cases, a pilot plant study will benecessary to determine the best membrane to use, particulate/organism removal efficiencies, cold andwarm water flux, the need for pretreatment, fOUling potential, operating and transmembranepressure and other design and monitoring considerations. Any virus removal credit must also bedocumented through an appropriate piloting process. The state reviewing authority should becontacted prior to conducting the pilot study to establish the protocol to be followed.

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3. The life expectancy of a particular membrane under consideration should be evaluated during the piiotstudy or from other relevant available data. Membrane replacement frequency is a significant factor inoperation and maintenance cost comparisons in the selection of the process.4. Some membrane materials are incompatible with certain oxidants. If the system must rely on pretreatment oxidants for other purposes, for example, zebra mussel control, taste and odor control, oriron and manganese oxidation, the selection of the membrane material becomes a significant designconsideraiion.5. The source water temperature can significantly impact the flux of the membrane under consideration.At low water temperatures, the fiux can be reduced appreciably (due to higherwater viscosity and.resistance of the membrane to permeate), possibly impacting process economics by the number ofmembrane units required for a full scale facility. Seasonal variation of design fiow rates may be basedon documented lower demand during colder weather.6. Back flushing volumes can range from 5 -15 percent of the permeate flow depending upon thefrequency of flushing/cleaning and the degree offouling and this should be considered in thetreatment system siZing and the capacity of the raw water source.7. An appropriate level of finished water monitoring as well as periodic integrity testing shall be providedto (outinely evaluate membrane and housing integrity and overall filtration performance. Monitoringoptions may include particle counters, manual and/or automated pressure testing, air diffusion tests,

sonic testing, and biological testing. Consult the appropriate regulato'Y agency regarding processmonitoring requirements.8. Cross connection control considerations must be incorporated into the system design, particularly withregard to chemical feeds and waste piping used for membrane cleaning, waste stream andconcentrate.9. Redundancy of critical control components including but not limited to valves, air supply, andcomputers shall be required as per the reviewing authority.10. Other pre- and post-membrane treatment requirements must be evaluated in the final design toaddress other contaminants of concern such as color and disinfection by-product precursors.

Adopted April, 1997Revised April, 2003

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POLICY STATEMENTONULTRA VIOLET LIGHTFOR TREATMENT OF PUBLIC WATER SUPPLIESUltra Violet (UV) Light treatment devices may be used to treat bacteriologically unsafe groundwater fromdrinking water wells. However, reviewing authorities expect water system owners to take all stepspossible to obtain a naturally safe water source before considering treatment. A naturally safe watersource provides the best long-term public health protection and there is no reliance on a treatment deviceto assure safe water. There must be a determination that the bacteriologically unsafe water is not due tothe influence of surface water.Recent research has demonstrated the effectiveness of UV as a primary disinfectant. While this policystatement does not specifically cover UV treatment for surface water or groundwater under the directinfluence of surface water, it is not the intent of this policy to discourage such use. Portions of this policyare applicable to the treatment of effectively filtered surface water. The reviewing authority shall becontacted regarding use of UV treatment for these applications.When a naturally safe groundwater source is not available, or the system owner wishes to provide UVtreatment for other reasons, the following criteria shall be considered. Supplemental disinfection toprovide a residual in the water distribution system may be required by the approval authority. When UVlight treatment devices are used for non-health related purposes the UV device may provide doses lessthan indicated in the following criteria.A. CRITERIA FOR UVWATER TREATMENT DEVICES

1. UVwater treatment devices must comply with criteria approved by the reviewing authority orClass A criteria under ANSI/NSF Standard 55 - UltravioletMicrobiological Water TreatmentSystems; each UV water treatment device shall meet the following standards;a. Ultraviolet radiation at a wavelength of 253.7 nanometers shall be applied at a minimum doseof 40 millijoules per square centimeter (mJ/cm2) at the failsafe set point at the end of lamp life;b. The UV device shall be f il led with a light sensor to safely verify that UV light is being deliveredinto the reactor;c. The UV light assembly shall be insulated from direct contact with the influent water by aquartz (or high silica glass with similar optical and strength characteristics) lamp jacket tomaintain proper operating lamp temperature;d. The design and installation of the UV reactor shall ensure that the manufacturer's maximumrated flow and pressure cannot be exceeded;e. The UV assemblies shall be accessible for visual observation, cleaning and replacement ofthe lamp, lamp jackets and sensor window/lens;f. A narrow band UVmonitoring device shall be provided that is sensitive to germicidal UV light.It shall be accurately calibrated so that it indicates the true irradiance (mJ/cm2) at 253.7nanometers and be installed at the location critical for that unit. The device shall trigger anaudible alarm in the event the sensor or lamp fails or if insufficient dosage is detected as

defined in item "a" above;g. An automatic shutdown valve shall be installed in the water supply line ahead of the UV treatmentsystem that will be activated whenever the water treatment system loses power or is tripped by amonitoring device when the dosage is below its alarm point of 40 mJ/ cm 2 When power is notbeing supplied to the UV unit the valve shall be in a closed (fail-safe) posilion.h. The UV housing shall be stainless steel 304 or 316L;

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2. A f low ort ime delay mechanism wired in series with the well or service pump shall be provided topermit a sufficient time for tube warm-up per manufacturer recommendations before water flows fromthe unit upon startup. Where there are extended no-flow periods and fixtures are located a shortdistance downstream of the UV unit, consideration should be given to UV unit shutdown betweenoperating cycles to prevent heat build-up in the water due to the UV lamp:3. A sufficient number (required number plus one) of parallel UV treatment systems shall be provided toassure a continuous water supply when one unit is out of service;4. No bypasses shall be installed;5. All water from the well shall be treated. The well owner may request a variance to treat only thatportion of the water supply that is used for potable purposes provided that the daily average and peakwater use is determined and signs are posted at all non-potable water supply outlets.6. The well or booster pump(s) shall have adequate pressure capability to maintain minimum watersystem pressure after the water treatment devices;B. PRETREATMENTThe reviewing authority will determine pre and post treatment on a specific case basis depending on rawwater quality. See Section G for raw water quality limitations. If coliform bacteria or other microbiologicalorganisms are present in the untreated water, a 5 micron filter shall be provided as minimum pretreatment.C. PROCESS CONTROL WATER QUALITY MONITORING

Total coliform monitoring and other parameters required by the reviewing authority will be used toevaluate UV treatment effectiveness. The minimum monitoring frequency will be as follows:Startup and 2 weeks after start up - one raw and one treated sample.Monthly thereafter - raw and treated.Monitoring for additional parameters or total coliform on an increased frequency may be required bythe reviewing authority.

D. ONLINE MONITORING, REPLACEMENT PARTSUV light intensity of each installed unitshall be monitored continuously. Treatment units and thewater system shall automatically shutdown if the UV dosage falls below the required output of 40mJ/cm'. Water systems that have source water exceeding 5 NTU turbidity may be required toinstall an online turbidimeter ahead of the UVwater treatment device. An automatic shutdownvalve shall be installed and operated in conjunction with the turbidimeter. Each owner shall haveavailable on site at least one replacement lamp, a 5 micron replacement filter and, whereapplicable, a replacement cyst reduction filter and any other components necessary to keep thetreatment system in service.

E. SEASONAL OPERATIONSUV water treatment devices that are operated on a seasonal basis shall be inspected and cleanedprior to use at the start of each operating season. The UV water treatment system including the filtersshall be disinfected prior to placing the water treatment system back into operation. A procedure forshutting down and starting up the UV treatment system shall be developed for or by each ownerbased upon manufacturer recommendations and submitted in writing to the review authority.

F. RECORD KEEPING AND ACCESSA record shall be kept of the water quality test data, dates of lamp replacement and cleaning, a recordof when the device was shutdown and the reason for shutdown, and the dates of prefilterreplacement.

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The reviewing authority shall have access to the UV water treatment system and records.Water system owners will be required to submit operating reports and required sample results on amonthly or quarterly basis as required by the reviewing authority.

G. RAW WATER QUALITY CHARACTERISTICSThe water supply shall be analyzed for the following water quality parameters and the results shall beincluded in the UVapplication. Pretreatment is required for UV installations if the water qualityexceeds any of the following maximum limits. When an initial sample exceeds a maximum limit, acheck sample shall be taken and analyzed.ParameterUV 254nm AbsorptionDissolved IronDissolved ManganeseHardnessHydrogen sulfide (if odor is present)Iron BacteriapHSuspended SolidsTurbidityTotal ColiformE. ColiCryptosporidiumGiardia

Maximum20 percent at 1 cm0.3 mg/L0.05 mg/L120 mg/L*Non-DetectableNone6.5 to 9.510 mg/L1.0 NTU1.000/100 ML******

* A higher hardness may be acceptable to the reviewing authority .if experience with similar waterquality and reactors shows there are no treatment problems or excessive maintenance required.** These organisms may indicate that the source is either a surface water or ground water under thedirect influence of surface water and may require additional filtration pretreatment. Consult thereviewing authority for guidance.Raw water quality shall be evaluated and pretreatment equipment shall be designed to handle waterquality changes. Variable turbidity caused by rainfall events is of special concern.

Adopted April, 2003

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POLICY STATEMENTONINFRASTRUCTURE SECURITYFORPUBLICWATER SUPPLIES

Recent events in the United States and abroad have made it clear that increased security for public watersystem facilities is imperative. Review of public water systme security infrastructure and practices hasshown an industry-wide vulnerability to intentional acts of vandalism, sabotage and terrorism. Protectionfrom these types of threats must be integrated into all design considerations. Many public drinking watersystems have implemented effective security and operational changes to heip address this vulnerability,but additional efforts are needed.Security measures are needed to help ensure that public water suppliers attain an effective ievel ofsecurity. Design considerations need to address physical infrastructure security, and facilitate securityrelated operational practices and institutional controls. Because drinking water systems cannot be madeimmune to all possible attacks, the design needs to address issues of critical asset redundancy,monitoring, response and recovery. All public water supplies need to identify and address security needsin design and construction for new projects and for retrofits of eXisting drinking water systems.The following concepts and items should be considered in the design and construction of new watersystem facilities and improvements to existing water systems:1. Security shall be an integral part of drinking water system design. Facility layout shall consider criticalsystem assets and the physical needs of security for these assets. Requirements for sUbmitting,identifying and disclosing security features of the design, and the confidentiality of the submission andregulatory review should be discussed with the reviewing authority.2. The design should identify and evaluate single points of failure that could render a system unable tomeet its design basis. Redundancy arid enhanced security features should be incorporated into thedesign to eliminate single points of failure when possible, or to protect them when they cannotreasonably be eliminated.3. Consideration should be made to ensure effective response and timely replacement of criticalcomponents that are Critical components that comprise single points of failure (e.g., high volumepumps) that cannot be eliminated should be identified during design and given special consideration.damaged or destroyed. Design considerations should include component standardization, availability

of replacements and key parts, re-procurement lead times, and identification of suppliers and secureretention of component specifications and fabrication drawings. Readily replaceable componentsshould be used whenever possible and provisions shouid be made for maintaining an inventory ofcritical parts.4. Human access should be through controlled locations only. Intrusion deterrence measures (e.g.,physical barriers such as fences, window grates and security doors; traffic fiow and check-in points;effective lighting; lines of sight; etc.) should be incorporated into the facility design to protect criticalassets and security sensitive areas. Effective intrusion detection should be included in the systemdesign and operation to protect critical assets and security sensitive areas. All cameras.and alarmsinstalled for security purposes should include monitors at manned locations.5. Vehicle access should be through controlled locations only. Physical barriers such as moveable

barriers or ramps should be included in designs to keep vehicles away from criticat assets andsecurity sensitive areas. It should be impossible for any vehicle to be driven either intentionally oraccidentally into or adjacent to finished water storage or critical components without facilityinvolvement. Designated vehicle areas such as parking lots and drives should be separated fromcritical assets with adequate standoff distances to eliminate impacts to these assets from possibleexplosions of materiai in vehicles.6. Sturdy, weatherproof, locking hardware must be included in the design of access for all tanks, vaults,wells, well houses, pump houses, buildings, power stations, transformers, chemical storage, deliveryareas, chemical fill pipes, and similar facilities. Vents and overflows should be hardened through use

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7. Computer based control technologies such as SCADA must be secured from unauthorized physicalaccess and potential cyber attacks. Wireless and network based communications should beencrypted as deterrence to hijacking by unauthorized personnel. Vigorous computer access and virusprotection protocols should be built into computer control systems. Effective data recovery hardwareand operating protocols should be employed and exercised on a regular basis. All automated controlsystems shall be equipped with manual overrides to provide the option to operate manually. Theprocedures for manuai operation including a regular schedule for exercising and insuring operator'scompetence with the manual override systems shall be included in facility operation plans.8. Real time water quality monitoring with continuous recording and alarms should be considered at keylocations to provide early warning of possible intentional contamination events.9. Facilities and procedures for delivery, handling and storage of chemicals should be designed toensure that chemicals delivered to and used at the facility cannot be intentionally released, introduced

or otherwise used to debilitate a water system, its personnel, or the public. Particular attention shouldbe given to potentially harmful chemicals used in treatment processes (e.g., strong acids and bases,toxic gases and incompatible chemicals) and on maintenance chemicals that may be stored on-site(e.g., fuels, herbicides, paints, solvents).

Adopted April, 2003

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INTERIM STANDARDNITRATE REMOVALUSING SULFATE SELECTIVEANION EXCHANGE RESINFour treatment processes are generally considered acceptable for Nitrate/Nitrite removal. These are anionexchange, reverse osmosis, nanofiltration and electrodialysis. Although these treatment processes, whenproperly designed and operated will reduce the nitrate/nitrite concentration of the water to acceptablelevels, primary consideration shall be given to reducing the nitrate/nitrite levelS of the raw water througheither obtaining water from an alternate water source or through watershed management. Reverseosmosis nanofiltration or electrodialysis should be investigated when the water has high levels of sulfate orwhen the chloride content or dissolved solids concentration is of concern.Most anion exchange resins used for nitrate removal are suifate selective resins..Although nitrate selectiveresins are available, these resins typically have a lower total exchange capacity.SPECIAL CAUTIONIf a sulfate selective anion exchange resin is used beyond bed exhaustion, the resin will continue toremove sulfate from the water by exchanging the sulfate for previously removed nitrates resulting intreated water nitrate levels being much higher than raw water levels. Therefore it is extremely importantthat the system not be operated beyond design limitations.PRE-TREATMENT REQUIREMENTSAn evaluation shall be made to determine if pretreatment of the water is required if the combination of iron,manganese, and heavy metals exceeds 0.1 milligrams per liter.DESIGNAnion exchange units are typically of the pressure type, down flow design. Although a pH spike cantypically be observed shortly before bed exhaustion, automatic regeneration based on volume of watertreated should be used unless justification for alternate regeneration is submitted to and approved by thereviewing authority. A manual override shall be provided on all automatic controls. A minimum of two unitsmust be provided. The total treatment capacity must be capable of producing the maximum day waterdemand at a level below the nitrate/nitrite MCL. If a portion of the water is bypassed around the unit andblended with the treated water, the maximum blend ratio allowable must be determined based on thehighest anticipated raw water nitrate level. If a bypass is provided, a totaling meter and a proportioning orregulating device or flow regulating valves must be provided on the bypass line.EXCHANGE CAPACITYAnion exchange media will remove both nitrates and sulfate from the water being treated. The designcapacity for nitrate and sulfate removal expressed as CaCO, should not exceed 16,000 grains per cubicfoot (37g/l) when the resin is regenerated with 10 pounds of salt per cubic foot (160 g/I) of resin whenoperating at 2 to 3 gallons per minute per cubic foot (0.27 to 0.4 Umin per litre). However, if high levels ofchlorides exist in the raw water, the exchange capacity of the resin should be reduced to account for thechlorides.

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FLOW RATESThe treatment flow rate should not exceed 7 to 8 gal lons per minute per square foot of bed area (29 to 32em/minute down flow rate). The back wash flow rate should be 2 to 3 gallons per minute per square foot ofbed area (8 to 12 em/minute rise rate) with a fast rinse approximately equal to the service flow rate.FREEBOARDAdequate freeboard must be provided to accommodate the backwash flow rate of the unit.MISCELLANEOUS APPURTENANCESThe system shall be designed to include an adequate under drain and supporting gravel system, brinedistribution equipment, and cross connection control.MONITORINGWhen ever possible, the treated water nitrate/nitrite level should be monitored using continuous monitoringand recording equipment. The continuous monitoring equipment should be equipped with a high nitratelevel alarm. If continuous monitoring and recording equipment is not provided, the finished waternitrate/nitrite levels must be determined (using a test kit) no less than daily, preferably just prior toregeneration of the unit.WASTE DISPOSALGenerally, waste from the anion exchange unit should be disposed in accordance with Section 4.11.2 ofthese Standards. However, prior to any discharge, the reviewing authority must be contacted forwastewater discharge limitations or NPDES requirements.ADDITIONAL LIMITATIONSCertain types of anion exchange resins can tolerate no more than 0.05 mg/L free chlorine. When theapplied water wil l contain a chlorine residual, the anion exchange resin must be a type that is notdamaged by residual chlorine.Adopted April, 1997

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INTERIM STANDARDUSE OF CHLORAMINE DISINFECTANTFORPUBLIC WATER SUPPLIESAmmonia can be used for the conversion of chlorine in drinking water into the longer lasting but lesspowerful disinfectant chloramine, Possible advantages and disadvantages of the use of chloramine ratherthan free chlorine include:Use of chloramine may reduce total trihalomethane concentrations reaching consumers. This is becausechloramine does not form trihalomethanes on contact with natural organic matter in the water, although itmay form other by-products,Use of chloramine may reduce the need for high disinfectant concentrations to be added


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the effects on disinfectant power and corrosiveness of the water may require consideration. Ammoniagas forms alkaiine solutions which may cause local plugging by iime deposition. Where hard water isto be treated, a side stream of pre-softened water may be needed for ammonia dilution so as toreduce plugging problems.6. The use of chloramine in distribution systems which are not well maintained by flushing, swabbing andother regular routine maintenance activities can lead to local loss of disinfectant residual, increasednitrifying bacterial activity and, possibly over a period of time, to persistent high coiiform bacterialcounts which may not respond to reversion to the use of free chlorine. Early detection of nitrifying

bacteria activity may be made by checking for reduced dissolved oxygen, elevated free ammonia,elevated HPC, and elevated nitrite and nitrate levels.7. Chloramine in water is considerably more toxic to fish and other aquatic organisms than free chlorine.Consideration must therefore be given to the potential for leaks to contaminate and damage naturalwater course eco-systems. Kidney dialysis treatment can be upset by use of chloraminated water.Medical authorities, hospitals and commercial and domestic aquarium keepers should be notified sothey can arrange for precautions to be taken.Poiicy Statement Adopted April, 1997Re-Adopted as Interim Standard April, 2003

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All reports, final plans specifications, and design criteria should be submitted at least 60 days prior tothe date on which action by the reviewing authority is desired. Environmental Assessments, andpermits for construction, to take water, for waste discharges, for stream crossings, etc., may berequired from other federal, state, or local agencies. Preliminary plans and the engineer's reportshould be submitted for review prior to the preparation of final plans. No approval for construction canbe issued until final, complete, detailed plans and specifications have been submitted to the reviewingauthority and found to be satisfactory. Documents submitted for formal approval shall include but notbe limited to:

SUBMISSION OF PLANS1.0 GENERAL

PART 1

a. engineer's report, where pertinent,b. summary of the design criteria,c. operation requirements, where applicable,d. general layout,e. detailed plans,f. specifications,g. cost estimates.h. water purchase contracts between water supplies, where applicable,i. other information as required by reviewing authority.Where the Design/Build construction concept is to be utilized, special consideration must be given to:designation of a project coordinator; close coordination of design concepts and submission of piansand necessary supporting information to the reviewing authorily; allowance for project changes thatmay be required by the reviewing authority; and reasonable time for project review by the reviewingauthority.

1.1 ENGINEER'S REPORTThe engineer's report for water works improvements shall, where pertinent, present the followinginformation:1.1.1 General information,

includinga. description of the existing water works and sewerage facilities,b. identification of the municipality or area served,c. name and mailing address of the owner or official custodian.

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' - ' ' ' : ' ~ 1 ; ~ i ~ I 0 ! { f f i : : 1 { ~ 1 7 - - " - .SUBMISSION OF PLANS

1.1.2 Extent of water works system,includinga. description of the nature and extent of the area to be served,b. provisions for extending the waterworks system to include additional areas,

PART 1

c. appraisal of the future requirements for service, including existing and potential industrial,commercial, institutional, and other water supply needs.1.1.3 Justification of project

Where two or more solutions exist for providing public water supply facilities, each of which isfeasible and practicable, discuss the alternatives. Give reasons for selecting the onerecommended, including financial considerations, operational requirements, operatorqualifications, reliability, and water quality considerations.1.1.4 Soil, groundwater conditions, and foundation problems,

including a description ofa. the character of the soil through which water mains are to be laid,b. foundation conditions prevailing at sites of proposed structures,c. the approximate elevation of ground water in relation to subsurface structures.

1.1.5 Water use data,includinga. a description of the population trends as indicated by available recordS, and the estimatedpopuiation which will be served by the proposed water suppiy system or expanded system 20years in the future in five year intervals or over the useful l ife of critical structures/equipment,b. present water consumption and the projected average and maximum daily demands,including fire flow demand (see Section 1.1.6),c. present and/or estimated yield of the sources of supply,d. unusual occurrences.

1.1.6 Flow requirements,includinga. hydraulic analyses based on flow demands and pressure requirements (See Section 8.1.1)

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including1.1.7.1 Surface water sources,

a. hydrological data, stream flow and weather records,

PART 1

d. description of the watershed, noting any existing or potential sources of contamination(such as highways, railroads, chemical facilities, etc.) which may affect water quality,

c. maximum flood flow, together with approval for safety features of the spillway and damfrom the appropriate reviewing authority,

b. safe yield, including all factors that may affect it,

b. fire flows, when fire protection is provided, meeting the recommendations of the InsuranceServices Office or other similar agency for the service area involved.

Describe the proposed source or sources of water supply to be developed, the reasons for theirselection, and provide information as follows:

1.1.7 Sources of water supply

SUBMISSION OF PLANS

e. summarized quality of the raw water with special reference to fluctuations in quality,changing meteorological conditions, etc.f. source water protection issues or measures that need to be considered orimplemented.

1.1.7.2 Groundwater sources,includinga. sites considered,b. advantages of the site selected,c. elevations with respect to surroundings,d. probable character of formations through which the source is to be developed,e. geologic conditions affecting the site, such as anticipated interference betweenproposed and existing wells,f. summary of source exploration, test well depth, and method of construction; placementof liners or screen; test pumping rates and their duration; water levels and specific yield;water quality,g. sources of possible contamination such as sewers and sewerage facilities, highways,railroads, landfills, outcroppings of consolidated water-bearing formations, chemicalfacilities, waste disposal wells, etc.

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SUBMISSION OF PLANS PART 1h. wellhead protection measures being considered (see Section 3.2.3.2 and 3.2.3.3).

1.1.8 Proposed treatment processesSummarize and establish the adequacy of proposed processes and unit parameters for thetreatment of the specific water under consideration. Alternative methods of water treatmentand chemical use should be considered as a means of reducing waste handling and disposalproblems. Bench scale test, pilot studies, or demonstrations may be required to establishadequacy for some water quality standards.

1.1.9 Sewerage system availableDescribe the existing sewerage system and sewage treatment works, with special reference totheir relationship to existing or proposed water works structures which may affect the operation ofthe water supply system, or which may affect the quality of the supply.

1.1.10 Waste disposalDiscuss the various wastes from the water treatment plant, their volume, proposed treatmentand points of discharge. If discharging to a sanitary sewerage system, verify that the system,including any lift stations, is capable of handling the flow to the sewage treatment works and thatthe treatment works is capable and will accept the additional loading.

1.1.11 AutomationProvide supporting data justifying automatic equipment, including the servicing and operatortraining to be provided. Manual override must be provided for any automatic controls. Highlysophisticated automation may put proper maintenance beyond the capability of the plant operator,leading to equipment breakdowns or expensive servicing. Adequate funding must be assured formaintenance of automatic equipment.

1.1,12 Project sites,includinga. discussion of the various sites considered and advantages of the recommended ones,b. the proximity of residences, industries, and other establishments,c. any potential sources of pollution that may influence the quality of the supply or interfere witheffective operation of the water works system, such as sewage absorption systems, septictanks, privies, cesspools, sink holes, sanitary landfills, refuse and garbage dumps, etc.

1,1,13 Financing,includinga. estimated cost of integral parts of the system,b. detailed estimated annual cost of operation,

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SUBMISSION OF PLANSc. proposed methods to finance both capital charges and operating expenses.

1.1.14 Future ex1ensionsSummarize planning for future needs and services.

1.2 PLANSPlans for waterworks improvements shall, where pertinent, provide the following:1.2.1 General layout,

includinga. suitable title,b. name of municipality, or other entity or person responsible for the water supply,c. area or institution to be served,d. scale,e. north point,f. datum used,g. boundaries of the municipality or area to be served,h. date, name, and address of the designing engineer,

PART 1

i. imprint of professional engineer's seal or conformance with engineering registrationrequirements of the individual state,j. legible prints suitable for reproduction,k. location and size of existing water mains,I. location and nature of existing water works structures and appurtenances affecting theproposed improvements, noted on one sheet.

1.2.2 Detailed plans,includinga. stream crossings, providing profiles with elevations of the stream bed and the normal andextreme high and low water levels,b. profiles having a horizontal scale of not more than 100 feet to the inch and a vertical scale

of not more than 10 feet to the inch, with both scales clearly indicated,

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SUBMISSION OF PLANS PART 1c. location and size of the property to be used for the groundwater development with respectto known references such as roads, streams, section lines, or streets,d. topography and arrangement of present or planned wells or structures, with contour intervalsnot greater than two feet,e. eievations of tHe highest known fiood level, floor of the structure, upper terminal of protective

casings and outside surrounding grade, using United States Coast and Geodetic Survey,United States Geological Surveyor equivalent elevations where applicable as reference,f. plat and profile drawings of well construction, showing diameter and depth of drill holes,casing and liner diameters and depths, grouting depths, elevations and designation ofgeological formations, water levels and other details to describe the proposed wellcompletely,g. location of all existing and potential sources of pollution which may affect the water sourceor underground treated water storage facilities, .h. size, length, and materials of proposed water mains,i. location of existing or proposed streets; water sources, ponds, lakes, and drains; storm,sanitary, combined and house sewers; septic tanks, disposal fields and cesspools,j. schematic flow diagrams and hydraulic profiles showing the flow through various plant units,k. piping in sufficient detail to show flow through the plant, in