CASE STUDIES ASSESSING LOW-COST, IN-PLACE
                 TECHNOLOGIES AT SMALL WATER SYSTEMS
                              ' Prepared for
       THE ASSOCIATION OF STATE DRINKING WATER ADMINISTRATORS
                      1911 NORTH FORT MYER DRIVE
                       ARLINGTON, VIRGINIA 22209
                                  By
                   THE GREELEY-POLHEMUS GROUP, INC.
                         105 SOUTH HIGH STREET
                   WEST CHESTER, PENNSYLVANIA 19382
                                  and
                         MALCOLM PIRNIE, INC.
                       11832 ROCK LANDING DRIVE
                               SUITE 400
                     NEWPORT NEWS, VIRGINIA 23606
                               JULY 1992
REPRINTED WITH THE WRITTEN PERMISSION OF THE ASSOCIATION OF STATE
DRINKING WATER AEMINISTRATORS

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                                     ACKNOWLEDGEMENTS
         The Report Case Studies Assessing Low-Cost. In-Place Technologies at Small Water Systems was
  prepared for the Association of State Drinking Water Administrators (ASDWA). The project was directed
  by G. Wade Miller, former Executive Director ASDWA, and Vanessa M. Leiby, Executive Director ASDWA
  The project was greatly assisted by the In-Place Technology Steering Committee. The Committee members
  included:
         David Schnare, Ph.D., Assistant to the Director
         U.S. EPA Office of Ground Water and
         Drinking Water

         Donna Cirolia
         Manager, Industry and Government Relations,
         Culligan International Company

         Joseph Harrison
         Technical Director
         Water Quality Association

         Ben Smith, P.E., Acting Branch Chief
         Drinking Water Standards Division
         U.S. EPA Office of Ground Water and
         Drinking Water

         Marc  Parrotta, Environmental Engineer
         Drinking Water Standards Division
         U.S. EPA Office of Ground Water and
         Drinking Water
David Breau, P.E., Acting Manager
Drinking Water Program
Maine, Department of Human Services

Allen Hammer, P.E.
Director, Division of Water Supply Engineering
Virginia Department of Health

Dan Houck, P.E.
President
D.H. Houck Associates, Inc.

Barbara Wysock, Environmental Engineer
Technical Support Division
U.S. EPA Office  of Ground Water and
Drinking Water

Andrew Caraker
Vice President
ECOS, Inc.   .
        Funding for this project was provided by members of the Water Quality Association including:
 Culligan International Company, Northbrook, II; EcoWater Industrial Systems, Middletown, OH- Autotroi
 Corporation, Milwaukee, WI; ESSEF Corporation, Chardon, OH; Kinetico,  Incorporated, Newbury OH-
 Ametek, Sheboygan, WI; K&N Plastics, Elk Grove Village, IL; Atlantic Filter Corporation, West Palm Beach'
 FL; Trojan Technologies, London, Ontario,  Canada;  Cuno, Inc., Meridien, CT; Fleck Controls  Inc
•Brookfield, WI; Teledyne Water Pik, Fort Collins Co., Geerts Soft Water, Inc., Battle Creek, MI; Rayne of
 Santa. Cruz, Inc. Santa Cruz, CA; Urbana Soft Water Service, Urbana, OH; Structural Fibers, Elgin, IL; Water
 Inc., El Segundo, CA; Water Resources International, Phoenix, AZ; Hawkins Water Tech, Inc., Middlebury
_IN; Vetter's Inc., Washington, LA.

        This Report was prepared by The Greeley-Polhemus G roup, Inc. Assistance was provided by Malcolm
 Pirnie Inc.                                                                            J

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                 CASE STUDIES ASSESSING LOW-COST, IN-PLACE
                   TECHNOLOGIES AT SMALL WATER SYSTEMS
                                 TABLE OF CONTENTS

 Section

 ACKNOWLEDGEMENTS

 TABLE OF CONTENTS  	
 SECTION 1
 INTRODUCTION
SECTION 2
SITE SELECTION
SECTION 3
WATER SYSTEM EVALUATION
                                              	:	  i
 EXECUTIVE SUMMARY	
                                                                                  IV
                      		•.		  1
       1.1 GENERAL	
       1.2 SCOPE OF WORK	'.'.'.'.'.'.	
       1.3 ORGANIZATION OF THIS REPORT  '.'.'.'.'.'.'.'.'.'.'.'.'.	  *
      2.1 INITIAL SURVEY  	
      2.2 WATER SYSTEM SELECTION	  3

             2.2.1 Selection Process	
             2.2.2 Selected List	'.'.'.'.'.'.'.'.'.'.'.'.'.'.	    7
                             	•••	  8
      3.1  GENERAL	
                                     	  8
            3J..I Green Cove Condominiums	
            3.1.2 Pineloch Sun Beach Club	
            3.1.3 Lima Brighton Elementary School	' '   	
            3.1.4 Fruitland Domestic Water Co.          	
            3.1.5 Lost Lake Camp  	'.'.'.'.'.'.'.'.'.'.'.'.'.'.	" "	  [j
            3.1.6 Darboy Sanitary District		
            3.1.7 Readsboro Water Treatment Facility	'.'.'.'.'.	  	  p
            3.1.8 Barrick Goldstrike Mines, Inc	'.'.'.'.'.'.'.'.'.'.'.'.     	  p
            3.1.9 Taycheedah  Correctional Facility	'.'.'.'.'.'.'.'.'.	  13

      3.2 REASON FOR INSTALLATION
      3.3 TREATMENT TECHNOLOGIES .....'.'.'.'.'.	   -
                                              	 ~1 ^
            3.3.1 Pressure Filtration Units	                            ,.-
            3.3.2 Bag and Cartridge Filter Units  	'.'.'.'.'.','.'.'.'.'.'.'.	  m
            3.3.3 Ion Exchange Units	  	  .,..
            3.3.4 Reverse Osmosis Units	  •>

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       3.4  EQUIPMENT PROCUREMENT PROCESS	77. ...   22

              3.4.1  Traditional Approach	 .   23
              3.4.2  Lease Purchase	   24
              3.43  In-House Purchase  	   25

       3.5  VENDOR TREATMENT GUARANTEES  	   26
       3.6  STATE/LOCAL/ENGINEER/MANUFACTURER ROLE	   28

              3.6.1  State Role	   29
              3.6.2  Local/Third Party Role  	   29
              3.6.3  Consulting .Engineer Role	;	   30
              3.6.4  Manufacturer Role  	.-...•;•	 :r....:.-..:.-. ;-.   31
       3.7 OPERATION AND MAINTENANCE
                                                                                    31
             3.7.1 Existing Procedures	  31
             3.7.2 Suggested O&M Practices   	  35

       3.8 WATER SYSTEM COSTS	  39

SECTION 4
CONCLUSIONS	  42

SECTION S
RECOMMENDATIONS	  44

APPENDIX A
WATER SYSTEM DESCRIPTIONS	A . !
       A.I GREEN COVE CONDOMINIUM DEVELOPMENT
                                                                                  A- 1
             A.LL Installed Treatment System . . . ......	     A - 1
             A.1.2 Raw Water Intake	A . 1
             A.1.3 Low Service Pump Station	A _ j
             A.1.4 Treatment System	•           A - ">

      A.2 PINELOCH SUN BEACH CLUB	A _ 4

             A.2.1 Installed Treatment System	A - 4

      A.3 LIMA BRIGHTON ELEMENTARY SCHOOL  	A - 5

             A.3.1 Prior Water System	         A _ 5
             A.3.2 Installed Water System	         A - 5
      A.4 FRUITLAND DOMESTIC WATER COMPANY  .
                                                                                  A -6
             A.4.1 Water System	A . 6
             A.4.2 Water Treatment System .	A . 7

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        A.5 LOST LAKE CAMP	                           A  „
                                                               •	f\ - o

               A.5.1  Prior Water System	        A  g
               A.5.2  Filtration Options	'"-'  "	A * g
               A.5.3  Selected Water System	A   in

        A.6 DARBOY SANITARY DISTRICT	                        A  in
                                                               *.	A - 1U

            -  A.6.1  Existing Water System  	          A
               A.6.2  Installed Water Treatment System  	.	*.'.'.'!     A - 11

        A.7 READSBORO WATER TREATMENT FACILITY ,	. . ; . . . . . ,. : ........: .... .  .,  A . 13

               A.7.1 Existing Water System  	      "     A   ,
             .  A.7.2 Water Treatment System	'.'.'.'.'.'.'.'.'.'.'.	A - 13
        A.8  BARRICK GOLDSTRIKE MINES, INC.
                                                                                       A- 15
               A.8.1 Installed Treatment System	          A  ,fi
               A.8.2 Pretreatment System	' ' ''	A - 16
               A.8.3 Reverse Osmosis System	   	A  17
               A.8.4 Post-treatment System	^   	A - 19

       A.9 TAYCHEEDAH CORRECTIONAL FACILITY	         A . 19

               A.9.1 Installed Water System	            A  .g

TABLES

Table 1: Information Available from Owners/Operators, Manufacturers, Engineers
Table 2: Information Available from State Officials
Table 3: Water  System Profile
Table 4: Reasons for Installation of Treatment Technologies
Table 5: Treatment Technologies
Table 6: Water System Costs
                                            111

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                                       EXECUTIVE SUMMARY

          The Small Systems  Low-Cost Technology Initiative began in 1988  by the  U.S.  Environmental

  Protection  Agency (EPA) to  ensure  that  low-cost  treatment technologies  are  available and that the

  technologies are acceptable to state regulators and small water systems. In 1990, the  In-Place Technology

  Committee was formed to document that low-cost technologies are in-place at small water systems and working

  as  designed.  The Committee  included  members of EPA, the Association of State  Drinking  Water

  Administration (ASDWA) and the .Water Quality Association (WQA). ..The Committee,-working through

  ASDWA, began an investigation of several case studies of small water systems. The Report Case Studies

  Assessing Low-Cost. In-Place  Technologies at Small Water Systems pr^mc the results of investigations of

  nine small water systems that have installed low-cost technologies in an effort to comply with the requirements

  of the Safe Drinking Water Act (SDWA).

         A review of small water systems throughout the United States was performed by ASDWA, members

 of the WQA and the Water and  Wastewater Equipment Manufacturing Association (WWEMA)  and state

 regulators.  Nine small water systems were selected from this list to represent a range  of possible in-place

 treatment technologies, and a range of system sizes and ownership  types.  The selected nine small  water

 systems include:

               Green Cove Condominiums, Oak Harbor, Ohio
               Pineloch Sun Beach Club, Ronald, Washington
               Lima Brighton Elementary School, Howe, Indiana
               Fruitland Domestic Water Company, Crawford, Colorado
               Lost Lake Camp, Mount Hood National Forest, Oregon
               Darboy Sanitary District, Appleton,  Wisconsin
              • Taycheedah Correctional Facility,  Fon Du Lac, Wisconsin
               Readsboro Water Treatment Facility, Readsboro, Vermont
               Barrick Goldstrike Mines,  Inc., Elko, Nevada

        The nine systems represent different  installed  treatment technologies,  different ownership types,

several types of operation and maintenance strategies, and different approaches to improving the quality of

drinking water. Four systems.iailized.pressure.ffltration unjts;-two-systems utilized bag and cartridge nitration

units; two utilized ion exchange water  softeners; and two utilized reverse osmosis units. Note the Barrick

Goldstrike facility utilized both multi-media filters and a reverse osmosis unit. The water systems ranged in
                                                IV

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  size from approximately 100 connections up to 800 connections.  Six systems are community water systems,




  two are non-transient non-community water systems and one is a transient non-community water system. Table




  I presents a profile of the water system including the system location, number of connections, treatment




  technology, ancillary features  constructed  as part of the  installation, total project cost and treatment



  technology cost.




         The type of treatment technology and the extent of improvements installed at the small water systems




  were dependent on the reason  for installation  and the financial strength of owner.  Systems'that were only




  improving  their treatment process to  meet SDWA requirements,  generally installed only the treatment




  technology and few other system improvements.  Systems that were installing drinking water systems for new




 or expanded communities provided more extensive improvements in addition to the treatment technology.




 These latter systems also tended to be  more financially secure, or as in the case of the Readsboro system,




 received Federal and state grants for a substantial portion of the improvement cost.




         Five of the systems investigated (Green  Cove, Darboy, Readsboro, Barrick  and Taycheedah) made




 significant improvements to the water system in addition to the installation of the new treatment technology.




 The additional improvements include substantial water plant buildings (as opposed to concrete block or.




 wooden houses),  new  groundwater wells,  transmission/distribution and  storage facilities,  and  other



 miscellaneous facilities. Each of these systems had  the financial strength, either internally or with Federal/state*




 assistance, to purchase these facilities.  The  Green Cove water system was  installed for a new residential




 development and the Darboy system was installed for  expansion of .residential development.  The Barrick




 system was installed as part of a multi-million  dollar expansion of a gold mine.  The state correctional agency




 supported the improvements to  the Taycheedah  facility.  Readsboro, which  internally does not have  the




 required financial strength, was able to purchase  and install the required facilities with the support of Federal




 and state grants and loans.   In contrast, the other  four facilities were  existing water systems that apparently-




 required only the addition  of a treatment process to remove  a  specific contaminant.  These treatment




 technologies were installed within the existing system with minimal other improvements performed. The Lima




Brighton and Lost  Lake systems were non-transient non-community and transient  non-community water

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 systems, respectively, and required limited improvements.  In both cases the improvements were purchased


 directly by the owner (Lakeland School Corporation and the U.S. Forest Service, respectively). The.Pineloch


 and Fruitland Domestic water systems financed the improvements internally and therefore installed only the


 facilities required to remove the specific contaminants.


         In general, all of the water systems meet the goal of improving the quality of drinking water. The


 treatment technologies installed at the water systems are .capable of reducing the level of the. contaminants


 of concern to below state standards according to the results of finished water quality analysis and discussions


 with state personnel.  The three Culligan Multi-Tech1 pressure filtration systems are producing acceptable


 finished water quality. Improvements to  the operation of two of the systems (Readsboro and Barrick) could


 be possible through operator training and changes in chemical additions. The HSI Canada system at Pineloch


 is capable of producing  acceptable water  quality,  according to the system owner and the manufacturer.


 However, the system was having mechanical problems with one of the two filter units during the investigation


 which resulted in high sulfide levels in the finished water since one  of the units  was not being backwashed.


        The  Fruitland Domestic and Lost Lake Camp water systems utilize bag and cartridge filtration units


 to treat the  surface water sources.  The Fruitland Domestic system utilizes  Filter Specialists,  Inc. and


 Brunswick Technetics filter units and the Lost Lake Camp system utilizes CUNO cartridge and 3M bag filters.


 Both systems based their selection of the technology on the results of research performed at  Colorado State


 University, which indicated that the technology was appropriate for surface water sources.  The performance


 of the two systems is related to the quality of raw water entering the system.  Raw water turbidity levels at the


 Fruitland Domestic system range from 1 to 5 NTU during normal streamflow months and range from 8 to 10


 NTU during  high streamflow months; whereas raw water turbidity at  Lost Lake Camp are consistently below


 1.0 NTU. The results of finished water quality analyses obtained for  the Fruitland Domestic system  for 1991


 indicate that monthly average turbidity levels ranged from approximately 0.3 to 0.4 NTU from August through


 February and 0.6 to 1.1 •NTU-from March through'June:  'In'May 1991 the water system was in violation of
   "CULLIGAN" is a registered trademark of Culligan International Company. "Multi-Tech" is a trademark of Culligan Internation:il
Company.
                                                 v:

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  Colorado's turbidity standard of less than 1.0 MTU and in June the turbidity level approached the standard.
  Operation and maintenance procedures used by the water system may have contributed to the violation of
  turbidity levels.                                                  ,                             ,
         The Oregon Health Division considers that the Lost Lake Camp water system meets water quality
  requirements based on the results of water quality analyses, performance of the water system and certification
  from the National Sanitation Foundation, Colorado State University and the Colorado Department of Health
  that the bag. filters are acceptable for giardia removal.
         The Darboy and Taycheedah water systems installed Tonka Water Treatment and System Mario ion-
 exchange units, respectively, to reduce  levels  of radium  226 and 228 from the incoming raw water.   Both
 systems are producing acceptable finished water quality according to the results of water quality analyses.
         The two reverse osmosis units at the Lima Brighton Elementary School (Water Factory Systems) and
 the Barrick Goldstrike Mines (Culligan) are also successfully removing high levels of nitrates and arsenic
 according to the finished water quality analyses.
         The approach  used by  the  water  systems for the procurement  of the  treatment technology was
 dependent primarily upon the extent of required improvements and the ability and knowledge  of the owner.
 The systems that required significant additional improvements utilized a consulting engineer to develop plans,'"
 specifications and  bid documents to select and award contracts for installation of the required facilities.  The
 Green Cove, Pineloch, Darboy,  Readsboro, Barrick Goldstrike and Taycheedah water systems utilized this
 approach.  In contrast, the Lost Lake Camp water system utilized a "lease purchase" approach, developed and
 administered internally  by the Forest Service.   The Lima  Brighton and Fruitland Domestic water systems
 utilized an  "in-house purchase"  approach  whereby the system owners working with assistance from state
 regulators negotiated directly with system suppliers/manufacturers for the purchase and installation of the
 treatment technologies.
        Guarantees on  the performance of the treatment equipment were required, by all, water systems
according to the plant operators/except the Fruitland Domestic system.  The extent of the guarantees ranged
                                                VII

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 from a basic one-year parts and labor coverage to more sophisticated coverage of equipment performance and

 serviceability.

        Table I presents a summary of the available information on the total project cost and the treatment

 technology cost for each of the nine water systems. Direct comparison of all the values shown is not possible

 because the available information was not provided on a common basis.  Estimates were made for some of

 the costs to try to achieve a level basis for evaluation.  The costs shown indicate that, in general, treatment

 technologies can be installed for 'S200 per connection or less.  However, if total project .costs are considered,

 the cost per connection ranges from S50 to 58,220. These total project costs are not always considered in the

 operation and  maintenance costs for these facilities since  project costs may be incorporated  into  the

 development infrastructure costs (i.e., Green Cove), paid through capital funds (i.e., Lima Brighton, Lost Lake

 Camp, Barrick Goldstrike and Taycheedah) or  substantially offset by Federal and/or  state grants  (i.e..

 Readsboro, Fruitland, Darboy). The total project costs will have to be considered for communities and water

systems that can not take advantage of these alternative financing arrangements.

       The conclusions of the study are as follows:

       1. The type of treatment  technology and the extent of improvements installed at the water
       system were dependent on the reason for installation and financial strength of the owner.
       Systems that were responding to requirements of the SDWA,  generally installed only the
       treatment  technology.   Systems  that were installed  for new  or  expanding communities
       provided more extensive improvements in addition to the treatment technology. These latter
       systems also had greater financial strength to absorb the cost of improvements.

       2.  Water systems  need adequate facilities,  qualified operators,  technical assistance and
       adequate funding to meet requirements of the SDWA. Performance of the nine systems, even
       with adequate facilities, was impacted by  the level of operator training and qualifications.
       Better qualified operators were able  to  adequately operate  the  facilities and recognize
       problems and assess possible solutions.  Less qualified operators may be capable of operating
       the system but appeared- to lack the ability to identify and find solutions to water system
       problems.  The impacts on the  finished water quality were most apparent for systems with
       changing raw water quality.

       3.  Three techniques were utilized by the water system to evaluate, select and procure the
       appropriate treatment technology. The selected technique was dependent primarily upon the
       extent of required improvements and ability of the owner.-Systems that required significant
       improvements in addition  to the treatment technology utilized the "traditional  approach",
       relying on a consulting engineer to develop plans, specifications and bid documents to select
       and award installation contracts. Systems that installed only the treatment technology utilized
       the internally developed "lease purchase" approach or an "in-house purchase" approach.  Each
                                               VIll

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 approach was appropriate for the facility to accomplish the required procurement. However,
 the latter two approaches placed greater responsibility on the water system owners.

 4. Guarantees on the performance of the treatment equipment were required by all the water
 systems except Fruitland Domestic. The extent of guarantees ranged from basic one-year parts
 and labor guarantees, to equipment performance and serviceability guarantees. Some systems
 with engineering plans and specifications  identified more restrictive guarantees on system
 performance  over time and individual components.

 5. The relationship among the owners, state officials, engineers and manufacturers and their
 roles in project development was dependent on the size and complexity of the proposed
 improvements.  Water systems that installed significant improvements relied on consulting
 engineers to  evaluate alternatives and develop plans,  specifications and  bid documents.
 Responsibility for technical effectiveness and system performance rested with the consulting
 engineers in this case. Water systems that installed only the treatment technology relied more
 heavily on state  officials and suppliers/manufacturers for alternatives evaluation, process
 selection and  performance. In this case, responsibility for technical effectiveness shifted to
 state officials  and manufacturers, at least that was believed by the owners.

 6.  Qualified water system operators are required to operate systems as well as to identify
 problems and  assess possible solutions. Problems not identified (i.e., washing out bag filters')
 will not be fixed unless operators are qualified and can recognize the problems. Operators
 require technical assistance on a periodic basis to properly operate and maintain the facilities.

 7.  Low-Cost,  In-Place Treatment Technologies can  be installed for S200 per connection or
 less according to  the  costs identified for the nine systems.  However, the total cost for all
 required system improvements can be much greater  depending on the condition and design
 of the existing facilities. The total project costs have to be considered by communities and
water systems  m assessing the feasibility and approach to installing system improvements
                                        IX

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                                             SECTION 1
                                          INTRODUCTION

  1.1     GENERAL

         In 1988, the U.S. Environmental Protection Agency (EPA) began a Small Systems  Low-Cost

  Technology Initiative with a mission to ensure that (a) low-cost technologies are available, and (b) the states

  and public water systems will accept these technologies. In 1990, the Low-Cost Technology Initiative began

  a  public/private  partnership  venture  in  which  the  EPA, the  Association  of  State  Drinking Water

  Administrators (ASDWA), and members  of  the  Water Quality Association (WQA) joined  together to

 document that low-cost technologies are in-place and working as designed.             ;

        As part of this effort, ASDWA requested proposals to conduct a number of case studies of small water

 systems that have installed low-cost technologies in an effort to comply with  the requirements  of the Safe

 Drinking Water Act (SDWA).  In August 1991, The Greeley-Polhemus Group, Inc. (GPG), entered into an

 agreement with ASDWA to conduct several case studies of small water systems.  GPG was supported by

 Malcolm  Pirnie, Inc. in this effort.   The intent of this effort was to investigate and document the use of

 treatment technologies in an attempt to identify effective, economical and efficient methods of solving small

 water system problems. The results of the investigation (data and case study reports) are intended to assist'

 state regulators in the evaluation and approval of thesejechnologies in their states.

 1.2     SCOPE OF WORK

        The Scope of Work involved the investigation of small water systems that have installed  low-cost

 treatment technologies to. achieve compliance with  the SDWA. The intent was to document  the technical

 performance and the costs of each installation.  The work efforts included an  investigation of the selected

 small  water systems, assessment of the  treatment  technology, including the  operation and  maintenance

 requirements, the performance of the systems - specifically their ability to meet SDWA requirements - and

 the costs associated with installation  and  long-term operation.  The work efforts also addressed the barriers

 that were overcome to install the technology; the procurement process used; treatment guarantees provided

by the supplier; and the interaction with state and local officials and others.

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        The work plan included (1) the identification and confirmation of appropriate sites that were willing



 to participate in the investigation; (2) the development and distribution of a questionnaire to identify the types




 of information needed for the case studies; (3) on-site visits to meet with water system owners/operators and



 others (state regulators, manufacturers,  engineers,  etc.)  if available, to discuss the operation of the water



 system; (4)  development of case study reports that  describe the  results  of  the investigations;  and (5)



 development of this final report to compile the case study findings and highlight the strengths and weaknesses



 of the treatment technologies and their use at small water systems.          	 '



 1.3     ORGANIZATION OF THIS REPORT




        This report consists of five  sections and an  appendix.  Section 1 discusses the purpose of the work.



Section 2 presents the site selection process used to select the nine small water systems to be investigated.



Section 3 presents the evaluation of the selected small water systems.  Section 3 focuses on the treatment



technology, vendor treatment guarantees, treatment efficiency, relationship of the system to state, local



government, consulting  engineers,  suppliers  and  other interested parties, operation and  maintenance



requirements and capital and operating costs.




        The conclusions of the investigations are presented in Section 4 and recommendations are presented



in Section 5. Appendix A contains  a brief description of the small water systems in the study  including the



facilities  and water quality  prior to  improvements, the selected treatment technology and  the date of



installation.

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                                            SECTION 2
                                         SITE SELECTION

 2.1     INITIAL SURVEY

         The In-Place Technology Committee is one of five committees that comprise the Low-Cost Small

 System  Treatment Technology Initiative.   The  committee was  formed to  develop  data  on treatment

 technologies that have been installed for small systems.  The Committee developed a questionnaire on small

 water system treatment technologies that was distributed to all the states. The survey was designed to obtain

 information from states on small system treatment technologies and to document the efficacy and costs of the

 treatment as well as why particular treatment systems were selected.

        The states also submitted lists of successful small water systems that were working effectively and lists

 of small water systems that did not perform adequately.  The Water Quality Association (WQA) and  the

 Water and Wastewater Equipment Manufacturing Association (WWEMA) gathered additional information

 from their members on small water systems. Based on the list of successful sites provided by the states and

 information from WQA and WWEMA, the Committee selected potential sites for this study.

 2.2     WATER SYSTEM SELECTION

        GPG met with members of the Committee at the start of project activities to discuss the scope and'

 objectives of the project and to review the sites selected for evaluation and the selection process. The results

 of that meeting included the identification of the following water systems~for possible, inclusion in this study:

        I-      Gfeen C°ve Condominiums, Oak Harbor, Ohio
        2.      Pmeloch Sun Beach Club, Ronald, Washington
        3.      Lake Tuck Water System, Bellevue, Washington
        4.    "• Lima Brighton Elementary School, Howe, Indiana
        5.      Fruitland Domestic Water Company, Crawford, Colorado
        6.      Lost Lake Camp, Mount Hood National Forest, Oregon
        7.      St. John the Baptist Church and School, Fond Du Lac, Wisconsin
        8.      Darboy Sanitary District, Appleton, Wisconsin
       9.      Taycheedah, Fond Du Lac, Wisconsin
        10.     Readsboro Water Treatment Facility, Readsboro, Vermont
        11.     Barrick Goldstrike Mines, Inc., Elko, Nevada

   v                                                                                           	

       The  purpose of Task 2 of the Project was to confirm the appropriateness of the selected sites to meet

the objectives of this Project and to confirm the availability of data needed to assess the potential applicability

-------
 of the low-cost technology to provide solutions to other small water systems.  "Appropriateness" was defined




 to include (1) the willingness of the water system owners and operators to provide information and assist in




 evaluating the system, (2) the availability of before and after water quality and operations data for assessing




 the effectiveness of low-cost technologies, and (3) to the extent possible, provide a variety of situations and



 problems that were successfully addressed.



 2.2,1   Selection Process




        State regulators responsible for the water systems were contacted to provide background information



 and  identify the availability of water quality data, sanitary surveys, plan review reports, and general water



 system data (plans and specifications of installed treatment technology).  The discussions were also used to




 obtain the state regulators' assessment of the water system and the owner/operator, the appropriateness of the




 system for inclusion in the Project, and the performance of the equipment to meet design specifications.




        The owners/operators of the water systems were contacted to identify their willingness to participate




 in the project, the availability of water quality and system design data and analysis, and any restrictions to its



 use,  and to discuss the water system in general.  The manufacturers of the treatment units and the system



 design engineers were  also contacted, if known, to identify availability of information and willingness to



 participate in this Project. In some cases, the names of the manufacturers, installers or other design engineers



were not readily available, but were identified after a more detailed review of system files.




        The work plan for  this  Project was explained to each of the potential  participants to describe the




 timing and amount of assistance that would be required.  The water system owners/operators were told that




a letter and questionnaire'would be distributed to explain the Project and identify the types of information




 needed for evaluation,  and  that' site visits would be made to each facility to discuss system operation and




 performance, inspect the system and to  collect additional data.  All of the water system owners/operators




indicated their willingness to participate  in the site visits, subject to approval from their Boards, if required.




        The results of the  telephone contacts  to the owner/operators,  state regulators, manufacturers,, and



engineers are summarized in Tables 1 and 2.

-------




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-------
 2.2.2   Selected List

        Based on the results of the initial investigations, the following water systems were recommended for

 inclusion in the study:

                Green Cove Condominiums
                Pineloch Sun Beach Club
                Lima Brighton Elementary School
                Fruitland Domestic Water Company
                Lost Lake Camp
                Darboy Sanitary District
               Taycheedah Correctional Facility                        	
                Readsboro Water Treatment Facility
               Barrick Goldstrike  Mines, Inc.


        The Lake Tuck  Water System and the St. John the Baptist Church and School were not recommended

due  to  operational problems at  the time of survey  and the limited amount of available information

documenting the systems.

-------
                                             SECTION 3
                                   WATER SYSTEM EVALUATION

 3.1     GENERAL

        Nine small water systems were selected for evaluation as part of the study to assess Low-Cost, In-Place

 Technologies at small water systems. The nine systems represent different installed treatment technologies,

 different ownership types, several types of operation and maintenance strategies, and different approaches to

 improving the quality of drinking water.

        The following paragraphs present a summary profile of each of the water systems including the size

 and location of t'he water system, principal players, installed technology together with any required ancillary

 features, operation and maintenance (O&M) responsibilities, and the approach used to obtain the technology.

 Table 3 summarizes  this information. The costs of each of the systems are presented later in this  Section.

 Appendix A presents a more detailed description of each of the water systems.

 3.1.1    Green Cove  Condominiums

        The Green Cove water system is a community water system that serves the potable water needs of the

 750-unit recreational resort located on the shore of Lake Erie near Oak Harbor, OH. The water system was

 installed as part of the condominium development and was designed to reduce the levels of turbiditv, bacteria

 and giardia.  The installed facilities include a raw water intake, low service  pump station,  pressurized

 clarification and filtration system,  granular-activated carbon  (GAC)  filter, disinfection system,  storage

 tank/clearwells and distribution  system.  The  Culligan Multi-Tech clarification and filtration system was

 installed to reduce turbidity, bacteria and giardia.  The GAC filters were installed to remove objectionable

 tastes and odors and to remove benzene which may occur in the raw water since the intake is located in a  boat

 channel for the condominium development.

        The system was designed by a consulting engineer with input from the owner and state regulators.

 Plans, specs and bid  documents  were prepared.  The  system is operated,by. part-time .certified operators.

employed  by the Condominium Group.  Culligan and the engineer assist with maintenance on an as needed

basis.

-------



•••
ROFILE
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WATER SYSTEM
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ANCILLARY
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TREATMENT
TECHNOLOGY
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clearwclls.transmissions
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Pressure clarifier, depth
filler and GAC filler,
disinfeclion

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Howe, IN
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Lima Brighton
Memenliiry School

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Appleton, Wl
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Darboy Sanitary
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filler disinfeclion

144
(400 people)

Readsboro, VT
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EIko, NV
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urrick (ioidstrlke
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-------
 3.1.2    Pineloch Sun Beach Club




         The Pineloch Sun Beach Club water system is a community water system that serves the potable water




 needs of the 400-unit recreational community located in Ronald, Washington. The water system was installed




 to reduce high levels of iron, manganese and sulfide in the raw water, which is obtained from an old coal mine




 shaft .near the water system. The water system currently serves the needs of 10-18 full-time cabins and about




 210 part-time occupancy cabins. The installed treatment system includes an HSI Canada, multi-media pressure



 filter with ion exchange media and chlorination.




         The system is operated  by the Club manager who performs daily checks of system operation. The



 operator is not certified, as state certification is not yet required.



 3.13    Lima Brighton Elementary School




         The Lima Brighton Elementary School water system is a non-transient non-community water system




 that serves the drinking water needs of the students and staff of the elementary school.  The water system was




 installed to reduce the levels of nitrates from the existing groundwater supply.  The installed system is a




 packaged Water Factory Systems HP-400 Reverse Osmosis Treatment System designed  to produce 250 to 280




 gallons per day.  The packaged RO unit was connected to the existing potable water facilities with only minor.



 additional piping required.




        The owner solicited proposals from suppliers/manufacturers for equipment suitable for the reduction




 of the levels of nitrates. Hawkins Water Tech, Inc. was selected  based on cost and a performance  guarantee



 that the level of nitrates would be reduced to less than the Maximum  Contaminant Level (MCL).




        The system is operated by school employees.  Hawkins  Water Tech, under an annual maintenance



 contract, changes the prefilters, p'H control cartridge, GAC filters and sanitizes the system.



 3.1.4   Fruitland Domestic Water Co.




        The Fruitland Domestic -Water  Company is a community water system  serving approximately 100




 customers in the area surrounding Crawford, Colorado.  The  system was  installed  to  remove  turbidity,




 bacteriological contamination and giardia. The installed system includes Filter Specialists, Inc. filter housings




with 10- and 5- micron bag filters, followed by Brunswick Technetics  filter units with a 1-micron cartridge






                                                10

-------
  filter. Modification of the chlorine system was also performed at the time of the filter installation.  The filters
  were purchased by the water company and installed directly by the homeowners (also water system owners)
  The filters were installed along the existing transmission line route, about 10 miles downstream of the water
  intake gallery and about 8 to 10 miles upstream of most of the water users.
         The system is operated and maintained by a water system operator currently certified by the state with
  a D license.  In 1992, this level of certification is required to  be upgraded to a C license. The operator is
  assisted by other water system owners as needed to maintain the system.            -	
 3.1.5    Lost  Lake Camp
         The Lost  Lake Camp water system is a transient non-community water system that serves the potable
 water needs of the campground located in ML Hood National Forest, near Hood River, Oregon. The system
 was installed to  meet the Surface Water Treatment Rule (SWTR) requirements of the State of Oregon.  The
 installed facilities  include CUNO 25- or 5-micron prefilter cartridge  filters, and a 3M 3.5-micron final bag
 filter. The system is a skid-mounted self-contained filtration plant designed for the removal of turbidity and
 giardia cysts.
        The Engineering Department of the Forest Service (owner) performed the evaluation of treatment
 alternatives and  selected  the recommended treatment system. The water system is operated and maintained
 by the campground operator, under contract to the Forest Service.
 3.1.6   Darbov  Sanitary District
        The Darboy Sanitary District Water System is a community wafer system serving approximately 2,000
 people in the  vicinity of  Appleton, Wisconsin. The new facilities were installed to meet the needs of the
 expanding population.  The water system includes a new pump station and groundwater well pump and Tonka
 Water Treatment Company zeolite softeners, and modified chlorination equipment at the previously existing
water treatment  facilities.  The treatment system was installed to reduce raw water hardness and combined
radium 226 and 228 .contamination.  ••••
        The system was designed by a  consulting engineer with input  from the owner and state regulators.
Plans, specs and bid documents were prepared.  The system is operated by a full-time operator employed by
                                                11

-------
 the Sanitary District  The operator is state certified for groundwater systems, distribution system and the



 zeolite treatment process. Routine maintenance of the system is performed by the plant operator and support



 personnel of the District



 3.1.7   Readsboro Water Treatment Facility



        The Readsboro water system is a community water system that serves approximately 400 people (144



 connections) in the town of Readsboro, Vermont  The water system was installed to meet the filtration



 requirements  of the SWTR.   The  installed facilities  include the  water  treatment  plant and  treatment



 equipment, 275,000-gallon storage tank, and transmission mains. Ancillary facilities, which were also required,



 include an access  road, sewer line extension, bridge and water meters.  The water treatment equipment



 includes booster pumps, chemical addition,  pressure clarification and  filtration filters and chlorination.



 Finished water is stored in the 275,000-gallon storage tank.



        The system was designed by  a consulting engineer with input from the owner and state regulators.



 Plans, specs and bid documents were prepared.  The water system  is operated by one full-time operator



 employed by the town.  The operator is also responsible  for operation of the town's wastewater  treatment



 system.



 3.1.8    Barrick Goldstrike Mines. Inc.




        The Barrick Goldstrike water system is a non-transient non-community water system that serves the



 potable water needs of the Mine's 1,100 employees. The water system was installed to reduce levels of arsenic,



 turbidity and silt-density index from-the existing groundwater supply.  Prior to installation of the new water



system, the company used bottled water for its potable water needs.  Previous owners of the mine used the



groundwater well for water supply.




        The water system installed at the Barrick Mine includes a pretreatment system consisting of a Culligan



Multi-Tech system with alum and polymer feeders, a polymer trap, a reverse osmosis system,  and a  post-



treatment system consisting'of a forced draft decarbonator and chlorine and polyphosphate feeders.   The



treatment system was designed, manufactured, supplied and tested by Culligan International Company.

-------
            A local consulting engineer from Nevada assisted in the permit approval process. Barrick's consulting
    engineer for  the  mine expansion contract assisted in the identification and  selection of the .treatment
    equipment and the selection of Culligan for supplying and installing the equipment.
            The treatment system is  operated by one full-time operator employed by the Barrick Mines.  The
    operator is also responsible for operation of the mine's domestic wastewater treatment system. The operator
    is not .state certified for the water plant, as this is not yet required by the State of Nevada for this facility.
    3.1.9   Taycheedah Correctional Facility            •      -                 	  ,,...,,  ;
           The Taycheedah water system is a community water system serving the potable water needs of 375
    inmates  and staff  of the correctional facility located near Fon du Lac, Wisconsin.  A System  Mario ion
    exchange water treatment system was installed to reduce the levels of radium.  The water supply is obtained
    from two groundwater  wells.
           The water system was designed  by a consulting  engineer with input from the owner and the state
   drinking water personnel.  Plans, specifications and bid documents were  prepared for the purchase and
   installation of the treatment equipment.  A mechanical contractor purchased and installed the equipment in
   an existing building. The plant is operated and maintained by the correctional facility maintenance personnel.
   The mechanical contractor provides assistance as needed, with support from the equipment supplier.
   3-2      REASON FOR INSTALLATION
          The type of treatment technology and the extent of improvements installed at the small water systems
•  ' were dependent on the  reason for. installation and the financial strength of  owner. Systems that were only
   improving their treatment process to meet SDWA requirements,  generally installed only the treatment
   technology and few other system improvements. Systems that were installing drinking water systems for new
   or expanded communities provided more extensive improvements in addition to the treatment technology.
   These latter systems also tended to be more financially secure, or as in the case of the Readsboro system.
   received  Federal and state grants for-a«ubstaniial»portion-of the improvement cost.
          Table 4 presents  the  reasons for installation for each  of the nine water systems and comments
  describing the decision process.
                                                  13

-------
ALLATION OF TREATMENT TECHNOLOGIES
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Green Cove was a new housing development which required water supply. ITie state required that SDWA
rcgulalions be met or permits would nol be issued and therefore the development could not proceed. The
developer selected a technology and complete water system (intake to water tap) that met requirements.
Cost of system was incorporated into infrastructure, cost of the dcvclop'menl.






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Pincloch was an existing communily water system that wanted to improve water quality and be "one-step
ahead" of regulations. Iron and manganese were low priority pollulanls according to stale. Improvements
limited to inslallalion of new Irealmeni process. Improvcmenis lo water source piping or waste irealment
were not performed. Improvements purchased by homeowners through monthly fees.



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Owner was concerned aboui nilrales in school's drinking waler supply. Installed treatment system
specifically to remove nilrales. Equipment was installed lo treat only water for drinking fountains and
kitchen use. System cost paid by Ihc school.


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Bag and cartridge fillers installed within an existing transmission and distribulion system. Homeowners
recognized need for treatment improvements due to giardiasis outbreak. Ixick of financial strength of
homeowners and system limited the extent of improvements. ^Improvements supported by FmHA financial
assistance.


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Extensive water system improvements made relative lo size of customer base. New facililies installed
included piping, treatment plant and equipment, storage lank plus access road, bridge and waste disposal.
Project heavily supported by FmHA and stale grants and loans. Without assistance, improvements
probably would nol have been performed.



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Water Irealment facilities installed as part of a multi-million dollar expansion of gold mine by new mine
owner. Owner concerned about employees health and safely as well as corporate liability associated with
contaminated water. The Company had heard rumors that the] previously used bottled waler may have
been obtained from a conlaminaled source. Company installed its own treatment facilities at Company
cost.




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Slate agency, concerned alxiul health and safely of inmales and staff as we!! as iiability, installed treatment
system lo reduce high levels of radium from existing ground wsiier source. Improvemenis included a new
well and transmission piping and w.-iier Irealmeni equipment. Costs paid directly by (he Correclional
Facility.


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         Five of the systems investigated (Green Cove, Darboy, Readsboro, Barrick and Taycheedah) made




  significant improvements to the water system in addition to the installation of the new treatment technology.




  The additional improvements  include substantial  water  plant buildings  (as opposed to concrete block or




  wooden  houses), hew  groundwater  wells, transmission/distribution and storage  facilities, and  other




  miscellaneous facilities. Each of these systems had the financial strength, either internally or with Federal/state




  assistance, to  purchase these facilities.  The Green Cove water system was installed for a new residential




  development and the Darboy system was installed for expansion of residential development.  The Barrick




  system was installed as part of a multi-million dollar expansion of a gold mine. The state correctional agency




  supported  the improvements to the Taycheedah facility. ' Readsboro, which internally does not  have the




  required financial strength, was  able to purchase and install the required facilities with the support of Federal



 and state grants and loans.




        In  contrast,  the other four facilities were existing water systems  that apparently required only the




 addition of a treatment process to remove a specific contaminant. These treatment technologies were installed




 within the existing system with minimal other improvements performed. The Lima Brighton and Lost Lake




 systems were non-transient non-community and transient non-community water systems, respectively, and



 required limited improvements.  Note that the Lima Brighton system is essentially a point of entry system for




 the school.  The Pineloch and Fruitland Domestic water systems financed the improvements  internally and



 therefore installed only the facilities required to remove the specific contaminants.



 3-3     TREATMENT TECHNOLOGIES




        Four different treatment technologies were utilized  by the nine small water systems investigated in




 this study.  Four of the nine small water systems utilized pressure filtration units. Two systems utilized bag




 and cartridge filtration units;  two systems utilized ion exchange water softeners; and two systems utilized




 reverse osmosis units.  Notg the  Barrick facility utilized both multi-media filters and a  reverse osmosis  unit.




 A discussion of the performance of each of these units is presented  in the following  paragraphs.  Table 5




 presents a   listing  of  the water systems  and  the  associated  treatment  technologies together with  the



manufacturer, contaminant of concern, design flow and overall assessment  of system  performance.
                                                 15

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         The evaluation of the performance of these systems is based on the review of available water quality




 analyses, discussions with water plant operators and state personnel, and observations made during the site




 visits.  As such, the observations presented below are initial indications of the performance of the systems or




 suggested operational changes that may have to be modified as a result of further analysis and review.



 3.3.1    Pressure Filtration Units




         Green Cove, Readsboro and Barrick water systems installed the Culligan Multi-Tech systems with




 clarification and depth filtration units.  The Green Cove system also utilizes a GAC filter and the Barrick




 system utilizes a reverse osmosis  unit (discussed later).  The Pineloch water system installed a HSI Canada




 multi-media filter. The Green Cove, Readsboro and Pineloch systems utilize two process trains operating in




 parallel.  The Barrick system is a single process train.  Design flow for the treatment units are as follows:




 Green  Cove -  2  at  115 gallons per minute (gpm); Readsboro - 2 at  35 gpm; Barrick  -  1 at 90. gpm; and



 Pineloch - 2 at 75 gpm.




        The three Culligan units appear to be operating as designed, producing finished water that meets state




 requirements, based on discussions with the owners/operators and review of the finished water quality analyses.




 The Green Cove system appears to be operating with the least problems. This can be attributed to the desien



 of the system as well as  its operators. The system is operated by part-time operators, under contract with the




 condominium complex.  These  part-time operators are also full-time  operators of larger water treatment




 facilities in the area and are state certified as  Class II water plant operators at the Green Cove facility.




 Following an initial break-in period where chemical dosages were adjusted', the plant has consistently produced




 adequate finished water quality based on the results of the water quality analysis.  The operators are currently




 investigating high turbidity levels as measured in the finished water clearwells. Monthly average turbidity levels"




 for 1991 ranged from 0.26 to 0.43 NTU, as measured in the clearwells. In contrast, turbidity levels in the water




after the Multi-Tech filtration process have been measured in the 0.1 to 0.2 NTU range.  The higher levels




are believed to  be the- results of uncoated concrete block baffles which were installed in the clearwells after




initial construction.  An investigation of alternative sealants for the concrete block baffles is a process to try



to further reduce  turbidity in the finished w;uer.
                                                . 17

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         The Readsboro water treatment system provides the required filtration to remove the turbidity and




 bacteria to below recommended limits. The system is currently having difficulty meeting the disinfection and



 disinfection by-product requirements in the distribution system.




         Review of system operation and chemical additions indicate that current corrosion control practices




 would be improved by discontinuing  use  of the polyphosphate corrosion inhibitor and switching to  an




 orthophosphate. This is because of the low hardness and alkalinity levels in the finished water.  The best




 corrosion control protection for this type of water is an orthophosphate that may also reduce the potential



 of lead and copper leaching into the drinking water from household plumbing.




        Use of an alternate coagulant should also be considered in order to optimize natural organic material



 removal.  This is needed to lower the potential trihalomethane formation and allow proper chlorine levels to




 be maintained to protect against microbial  contamination in the distribution system.  Alum, ferric chloride




 and polyaluminum chloride (PAC) used at the proper coagulation pH will typically provide effective turbidity



 and organic material removals.




        The  above described problems  are operator-related  rather  than  a deficiency in  the  treatment



 equipment. Additional training of the operator and additional working knowledge of the system should help.



 to improve the performance of the plant.




        The operation and performance of the  Barrick water system is discussed in Section 3.3.4, Reverse



 Osmosis  Units.




       The Pin.e"loch water system was having mechanical problems with one of the two filter units at the time




 of the site visit.  The system operator indicated that a spacer washer on the backwash timing mechanism broke




 during operation which prevented the filter unit from being backwashed. At the time of the site visit, the unit




 had  been  out  of operation for  about  two  months.   The replacement  part was  on order  with the




supplier/manufacturer however, apparent problems between the owner, supplier and manufacturer delayed the




delivery of the replacement part. Information from the supplier/manufacturer was not available to assess the



reasons for the problems.
                                                18

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         Prior to failure of the backwash cycle, the unit had apparently been operating adequately producing




 water quality meeting state standards. After failure, the operator was apparently running the two parallel filter




 units in a series operation which resulted in higher sulfide levels in the finished water since the broken unit




 was not being backwashed. The operator indicated that both units were operated to equalize the pressure on




 both tanks to prevent other damage to the.system. The higher sulfide levels were identified by taste and smell.




 Water quality analysis of the finished drinking water were not available for this period.




         Operation of only the "good" filter unit during this period may have been possible since water demand



 was low during the off-season. The operator, however, did not utilize this operating scheme.



 3.3.2    Bag and Cartridge Filter Units




        The Fruitland Domestic and Lost Lake Camp water systems utilize bag and cartridge.filtration units



 to treat the surface water sources. Both systems were installed to remove turbidity, bacteria and giardia. The




 raw water source conditions for the two systems are very different which impacts the performance of the filter




 units.  The Fruitland Domestic raw water source is Crystal Creek, a mountain stream in Western  Colorado.




 The stream  is subject to significant changes in turbidity levels due to changes in runoff conditions.  During




 heavy runoff months, April, May and June, raw water turbidity levels can range from 8 to 10 NTU.  During



 other months, the raw water turbidity levels range from 1 to 5 NTU.




        The Lost Lake Camp raw~water source is Lost Lake, a mountain lake 167 feet deep and located 3,100



 feet above sea level.  Turbidity levels in the raw water are consistently below 1.0 NTU.




     ;  Both systems  based their selection of the bag and cartridge technology on the results of research




 performed at Colorado State University by Dr. Charles Hibler.  The results indicated that the technology was



 appropriate for treatment of surface water sources.




        The results of finished water quality analysis obtained for the Fruitland Domestic system for 1991




indicate that monthly average turbidity levels ranged from approximately 0.3 to 0.4 NTU from August through




February and 0.6 to 1.1'NTU from March through June.  In May, 1991, the water system was in violation of




the state's turbidity standard of less than 1.0 NTU, and in June the turbidity level approached the  standard.
                                                19

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        Sufficient data was not available during the investigation to determine if the system is in compliance



 with the-SWTR.  Turbidity removal by the bag and cartridge filter system was reported to be "high" but there



 was no reference to removal of giardia cyst-sized particles. The state regulators indicated that a particle size



 analysis on the treatment system will be performed in the near future, although no specific time was identified.



 While it appears that the system may be meeting existing turbidity standards (for most months) the system may



 not be capable of meeting future filtration requirements.



        The Oregon Health Division considers  that the Lost Lake. Camp water system meets water quality



 requirements based on the results of water quality analyses, the overall performance of the water system and



 the certification, from the National Sanitation Foundation (NSF), Colorado State University and the Colorado



 Department of Health that the bag filters are acceptable for giardia removal. The state gave the water systems



 credit for 2 log removal through the filters based on certification from NSF that the bag filter was capable of



 removing giardia sized paricles.  The existing chlorination system with detention time  provided the third log,



 99.9%, removal/ inactivation as  required by the SWTR.



 3.33   Ion Exchange Units



        The Darboy and Taycheedah water systems installed ion exchange units to reduce levels of radium 226



 and 228 from the  incoming raw water. The Darboy water system installed Tonka Water Treatment Company



 zeolite water softeners. The two zeolite  softeners operate in parallel and produce 484 gpm of treated water.



 The softened water is blended with 66 gpm of-"untreated water to reduce its aggressiveness. The Darboy water



 system reduces the contaminants of concern, sulfate, iron and radium, and the aesthetic concerns of hardness



 and total dissolved solids to below the recommended limits.  The water quality analyses  indicated that iron



 has been reduced  to 0.23 milligrams/liter (mg/1) from 0.59 mg/1 and that combined radium 226 and 228 levels



 have been reduced to less than 1.0 pico curies per liter (pCi/1) from a rolling average of 5.4 pCi/1. The zeolite



softeners may  be slightly undersized or overloaded for the raw water quality and flows, but have performed



adequately with more frequent  backwash and brine regeneration.  To date, no significant operational or



maintenance problems have been reported.
                                                20

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          The Taycheedah water system installed two System Mario ion exchange units, operating in parallel.
  The system is working as designed according to the plant operator. The treatment units reduce radium levels
  in the raw water of 19-20 pCi/1 to less than 1 pCi/1 in the finished water. The finished water meets the state's
  drinking water standards according to the plant operator.  The only reported problem is with the timing on
  some  of the  meters, however the system installer is currently  providing service with support from the
  equipment supplier to solve this problem.
  3.3.4    Reverse Osmosis Units                                        .     • . f •            . -
          The Lima Brighton Elementary School and the Barrick Goldstrike Mine water systems both use
  reverse osmosis technology for treatment of raw water. The two systems, however, are very different in size
  and  design characteristics. The Lima Brighton water system is essentially a point of entry treatment unit
  providing 250-280 gallons per day (gpd) of treated water,  whereas the Barrick water system is designed to
  provide 56 gpm or 80,000 gpd of treated water.
         The Lima Brighton water  treatment  unit is a  Water Factory Systems HP-400 Reverse Osmosis
 Treatment System. The HP-400 packaged system includes a 5-micron cartridge prefilter, the reverse osmosis
 (RO) unit, a pH control filter adding calcite to control corrosivity and a GAC filter.  The water system also
 includes storage and repressurization tanks  and post-treatment GAC filters at each point of use (5 sites) in
.-the school. The system is designed to reduce nitrate levels in the.raw water from approximately 14 mg/1 to
 less than 1.0 mg/1 in the finished water. Results of water quality analyses performed after installation of the
 unit  indicate that-the nitrate level in  the finished water was reduced  to less than 1.0 mg/1, meeting  state
 requirements. -   '             •
        Technical review of the treatment system has raised some questions pertaining to the need for the
 GAC filter at the RO unit and  the GAC  filters  located at the different points of use. The GAC filter at the
 RO unit  was installed to control organics passing through the RO membranes. Since it is unlikely that
 organics will pass through the RO-membranevthe-GAC-filter may not be required. The point of use GAC
 filters are also not required and may adversely affect the microbial  quality of the drinking water.  Microbial
 growth in the GAC filters and the system was reported to be controlled through an annual disinfection of the
                                                 21

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 system  The system is flushed annually with chlorine dioxide at the start of the school year to clear microbial




 growth from the system. However, because no disinfectant residual is maintained during the school year, the




 microbial contamination can occur between chlorine dioxide flushing periods.  If the GAC filters.remain in




 service, it is recommended that they be replaced monthly to prevent microbial growth in the filters.




        RO units produce a very corrosive product water. Blending a percentage of the feedwater with the




 RO unit effluent should be considered to add stability to the product water stream and reduce the potential




 of corrosion by-products such as lead and copper from entering the drinking water.  The amount by-passed



 would be limited by the blended water's level of nitrates or other water quality concerns.



        The Barrick Goldstrike water treatment facilities include a Multi-Tech System with Alum and Polymer




 Feeders, a Polymer Trap, Acid and Antiscalant Feed Systems, a KP-90 Reverse Osmosis System and a Forced




 Draft Type Decarbonator. The system  is  designed to reduce the levels of arsenic, turbidity, and silt density




 index from the existing groundwater supply and produce 56 gpm of treated drinking water.  The results  of




 water quality analyses indicate that the system is working and producing finished water that meets the state's




 drinking water standards. Arsenic was reduced to approximately 0.022 mg/1 after installation from 0.084 before




 installation. Turbidity has been reduced to approximately 0.1NTU from 1.2 to 1.5 NTU.  The water system




 operator indicated that the system is operating well with no major  maintenance required to date.




        The Alum and Polymer Feed Systems, Multi-Tech Filtration System arid Water Softener 5>ystem was




 installed because the owner wanted identical systems for both the drinking water and boiler feed water systems




 for ease of operator maintenance.




        Corrosion control.for lead and copper could be improved by switching to zinc orthophosphate instead




 of polyphosphate and blend feedwater with the  RO permeate to increase product water stability.




       The unit is also achieving  only 89 percent salt rejection which is considered low for this type of



 membrane.




3"*     EOUIPMENT.PRQCUREMENT  PROCESS




       Three different approaches were utilized by the nine water systems for the evaluation, selection and




procurement of the treatment technology. The selection of the appropriate approach was dependent primarily






                                                22

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  upon the extent of required improvements arid the ability and knowledge of the owner. The systems that




  required significant improvements in addition to the treatment technology utilized the "traditional approach "




  reiving on a consulting engineer to develop plans, specs and bid documents to select and award contracts for




  installation of the required facilities.  The Green Cove, Pineloch, Darboy, Readsboro, Barrick Goldstrike and




  Taycheedah water systems  utilized this approach.  In contrast, the Lost Lake Camp water system utilized a




  "lease purchase" approach,  developed and administered internally by the Forest Service. The Lima Brighton




  and Fruitland Domestic water systems utilized an  "in-house purchase" approach whereby the system owners




  working with assistance from state regulators negotiated directly with system suppliers/manufacturers for the



  purchase and installation of the treatment technologies.



 3.4.1   Traditional Approach




        The traditional approach for  the selection and procurement of water treatment facilities is where the




 water system owner engages the services of a consulting engineer with  input from state regulatory officials to



 procure water treatment facilities.                                                    .




        The consulting engineer evaluates  the water needs of the water system and recommends expansion



 or system  improvements.  Alternative water supplies and  treatment  options are  evaluated based on cost,



 treatment  requirements, and equipment performance.   Final selection  criteria  for the water treatment




 equipment are generally based on capital cost and treatment effectiveness.  Bench scale or pilot tests may be




 conducted  prior to selection of the treatment equipment to evaluate equipment performance.  The engineer




 prepares contract documents, including plans and specifications, for the purchase and installation of the new.




 equipment and treatment plant facilities.  Bids are  requested from contractors for the equipment and other




 facilities as needed.  Award of the contracts is generally based on low-bid and  technical acceptance.




        As previously stated, Green Cove, Darboy, Pineloch, Readsboro, Barrick Goldstrike and Taycheedah



water systems utilized this approach.  In each case,  there were required system improvements in addition to




the treatment technology, which required the services of a consulting engineer to evaluate and design.




        Contract documents  for the Darboy and Readsboro water systems permitted the mechanical contractor



to submit an alternate bid for alternative treatment equipment that met  the performance requirements of the
                                              '  23

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 contract.  In both cases, the winning contractor  utilized alternative equipment proposals to develop the




 winning bid. It is not known if the contract documents for the other systems permitted the use of alternative



 equipment proposals.




         The traditional procurement approach utilized by the six water systems was successful and appropriate.




 Use of an alternative approach may not have been possible due to the complexity of the improvements made •



 to the systems.




 3.4.2    Lease Purchase




         The Forest Service utilized a lease  purchase arrangement for the procurement of water treatment



 facilities for the Lost Lake Camp.  The Forest Service requested quotations from three suppliers of water



 filtration equipment to supply and install water filters for a  pilot test to evaluate the performance of the




 proposed equipment. The Forest Service utilized a performance specification to identify the requirements of




 the pilot test. The water system was required to be National Sanitation Foundation approved and be capable




 of filtering at least 1-micron sized-particles for giardia cyst  removal.  The filtration technology was  not




 specified, allowing each company to propose its own filter.  A lease arrangement was specified, whereby the




 Forest Service would lease the equipment for the four month campground season.  The proposals were




 evaluated based on technical acceptability, least rental cost and conformance to existing site evaluations. Based



 on the results of this selection process, the Forest Service selected one of the companies to install bag and




 cartridge filters for the four month season. The equipment met the selection criteria and had the least rental



 cost.           .'




        The pilot test was actually a full scale treatment test of actual equipment to be installed at the Camp.




 Marvin Company, Inc. was selected to install a skid-mounted cartridge/bag filter system because of its technical




 acceptability and lower lease costs.  The pilot  test was based  on a lease arrangement where the treatment




equipment was rented from the manufacturer/supplier for the four month test  period. Following completion




of the pilot test and evaluation of the results,  including finished water quality, operation and  maintenance




requirements and overall  system  performance, the  Forest  Service entered into negotiations  with  Marvin



Company, Inc. for the purchase and final installation of the  equipment.






                                      .           24  '

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          The lease proposal provided three options to obtain a credit for a portion of lease cost based on the
  amount of time the equipment was leased from the supplier.  If the equipment was leased for four months,
  35 percent of the lease cost was applied as a credit to the purchase price.  If the equipment was leased for six
  or twelve months, the credit applied to the purchase price was 50 percent and 80 percent, respectively. These
  credits did not apply to the freight or installation charges.
  3.4.3    In-House Purchase
         The Lima Brighton Elementary School System worked directly with representatives of EPA and water
  treatment equipment suppliers to evaluate and design a treatment unit for the school. Following notification
  in November 1988 from EPA of a nitrate problem in the raw water supply, school officials contacted several
 equipment suppliers to identify possible solutions.  In January 1989, Hawkins Water Tech, Inc. submitted a
 preliminary proposal to the school identifying two treatment alternatives and their associated costs.  Reverse
 osmosis treatment was recommended because of its lower operational cost.
         In April 1990, the school requested formal proposals from equipment suppliers for the installation
 of a water .treatment system.  The request was based on a performance specification for the reduction of
 nitrates to below the established MCL. No formal bid documents were prepared for the procurement.  The.
 suppliers were requested to submit proposals for equipment that would meet the performance specification.
 A performance guarantee was required from the supplier to guarantee acceptable treatment of the raw water
        Hawkins Water Tech, Inc. submitted a proposal containing two options for nitrate removal at the
 school. Option  1 was an anion resin exchange system.  The option included an automatic twin tank system
 and a manual single tank'system.  The costs for these systems were approximately 55,700 for the automatic
 system and S3.550 for the manual.  The second option was the HP-400 Reverse Osmosis system which had a
 cost of approximately 53,600.  Operational costs for the manual anion exchange system were estimated to be
 S40 per month versus a cost of 560 - 580 per year for the RO system. The installation cost for both systems
 was estimated to be S2;175.
        Representatives of the school evaluated the proposals and awarded the contract to Hawkins Water
Tech, Inc. for the installation of the HP-400 Reverse Osmosis System.
                                                25

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        The Fruitland Domestic Water Company utilized selection criteria for the water treatment system that

 were based on capital cost, simplicity of design and ease of operation.  No specific bench scale or pilot test

 was conducted prior to selection of the treatment process.  Research by Colorado State University into the

 applicability  of  bag filters for surface water filtration was used  to evaluate the  appropriateness of the
                     *.          %               •
 technology for the Fruitland water system.

        The treatment equipment was purchased by the Fruitland Domestic Water Company using a loan from

 FmHA.  The loan was an extension of a previous grant and  loan package obtained from FmHA for the

 original installation of the intake gallery, chlorinator and transmission and distribution piping.

        The  treatment system was supplied by  Chief Equipment  Corporation, Denver,  Colorado and

 manufactured by Filter Specialists, Inc., Michigan City, Indiana and Brunswick Technetics Filterite, Timonium,

 Maryland.  The system was installed -by the Fruitland water system owners.

 3.5     VENDOR TREATMENT GUARANTEES

        Guarantees on the performance of the treatment equipment were required by all water systems

 according to the plant operators, except the Fruitland Domestic system, as discussed below. The extent of the

 guarantees  ranged from a basic one-year parts and labor coverage to more sophisticated coverage of equipment

 performance and serviceability.
                                                  •         •                              -*
        The performance guarantee provided by Hawkins Water Tech, Inc. for nitrate reduction at the Lima

 Brighton Elementary School was as follows:

               The Water Factory Reverse Osmosis HP-400 System will reduce the level of nitrate
        to below 10 ppm (as N). 10 ppm is the present Environmental Protection Agency maximum
        contaminant level  (MCL).   Upon  failure by  Hawkins Water Tech, Inc.  to meet this
        performance guarantee, Lakeland School Corporation has the option to request return of the
        money paid for the system.  Hawkins Water Tech, Inc. will  comply with the request. Both
        parties have the option of using an independent certified laboratory to verify actual  nitrate
        reduction.

        Water Factory Systems, the equipment manufacturer, provided a one-year limited warranty on the

water treatment system. 'The warranty'covered the entire system for a period of one year from the date of

installation or 60 days from the factory shipping date, whichever was first.  Replacement of the RO membrane
                                               26

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 was covered in full for the first 90 days.  For the period from the fourth to the twelfth month, the owner was

 required to pay 1/12 of the current suggested retail price for each month the RO unit was in service.

        The contract documents for the Darboy required a one-year parts and labor guarantee be provided

 on the treatment equipment. According to the bid specification, the equipment supplier was to guarantee that

 the softener system would provide the specified quantity of soft water at the identified flow rate;  that the

 effluent from the softener show zero hardness; that the turbidity or color would not increase by reason of

 flowing through the softener; and that no iron exchange material would be washed out of the system during

 any softening cycle at maximum flow rates.  The supplier was also required to guarantee that the loss of ion

 exchange material volume due to attrition would not exceed 3 percent per year for a period of three years.

 The agreement required the supplier to replace any defective materials or equipment  at no charge to the

Sanitary District for a period of one year from the date of final acceptance of the equipment.  The treatment

system warranty agreement specified items  requiring  routine maintenance.   A performance  bond was also

required for installation of the water  treatment facilities.

       The contract documents for the Readsboro water system specified the following guarantee:

               The  contractor shall guarantee all materials and  equipment furnished and work
       performed  for a period of one  year  from  the date of substantial completion or final
       completion of the project or specified part, as appropriate.  The contractor warrants and
       guarantees for a period of one  year  from  the date of substantial completion or final
       completion of the project or specified part, as appropriate, that the completed project is free
       from all defects due to faulty materials or workmanship and the contractor shall promptly
       make such corrections as may be necessary by reason of such defects including the repairs of
       any damage to other parts of the  project resulting from such defects. The owner will give
       notice of observed defects with reasonable promptness. In the event that the contractor
       should fail to make such repairs, adjustments, or other work that may be made necessary by
       such defects, the owner may do so and charge the contractor the cost thereby incurred  The
       performance bond  shall remain in full force and effect through the guarantee period.

               Contractor warrants and  guarantees to Owner and Engineer that all materials and
       equipment will be new  unless otherwise specified and that all work will be of good quality
       and  free from faults  or defects and in accordance with  the requirements  of the contract
       documents and of any inspections, tests or approvals. All unsatisfactory work, all faulty or
       defective work, and all work not conforming to the requirements of the contract documents
       at  the time of-acceptance-thereof-or of such  inspections, tests or approvals shall be
       considered defective.  Notice of all defects will be given to  contractor.  All defective work
       whether or not in place, may be rejected, corrected or accepted as determined by engineer.'

               Contractor warrants and guarantees that  title to all work materials and equipment
       covered by an application for payment, whether incorporated in the project or not, will pass
                                               27

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         to owner upon the receipt of such payment by contractor, free and clear of all liens, claims,
         security interests  or encumbrances, hereinafter referred  to as Liens;" and  that no  work,
         materials or equipment covered by an application for payment will have been acquired by
         contractor; or by any other person performing the work at the site or furnishing materials and
         equipment for the project, subject to an agreement under which an interest therein  or an
         encumbrance thereon is retained by the seller or otherwise imposed by contractor or such
         other person.

     .   The Forest Service utilized the results of the pilot test and  certification from the National Sanitation

 Foundation, Colorado State University and the Colorado Department of Health as evidence that the proposed

 bag and cartridge filtration system would work effectively. In addition, the equipment'suppiier was required

 to provide a one-year parts and labor warranty.

         The Fruitland Domestic Water Company also  relied on the results of the Colorado State University

 research and input from the State Drinking Water personnel as evidence that the bag and cartridge filters were

 appropriate for their water system.  No other treatment system guarantees or warranties were provided with

 the equipment, according to the system owners.  No performance bonding was required since  the owners

 installed the equipment and constructed the filter house themselves.

        Detailed information on guarantees for the Green Cove,  Barrick, Taycheedah and Pineloch water

 systems was not provided; however, the operators indicated that standard one-year parts and labor guarantees

 were required.

 3.6     STATE/LOCAUENGINEER/MANUFACTURER  ROLE

        Installation of the treatment technologies at the nine small  water systems required different levels of

 participation and assistance from the  owners, operators, state officials, consulting engineers, manufacturers

 and contractors.  The level  of involvement of each of the players was dependent on the complexity of the

 proposed improvements, the abilities of the owner/operator, and the level of financial commitment available

 for system improvements. Water systems that installed additional (complex) improvements (i.e., storage tanks.

 pipelines, roads, groundwater wells, etc.) utilized consulting engineers to evaluate alternatives  and develop

 plans, specs and  bid documents-for  procurement.  Responsibility for technical effectiveness rested with the

consulting engineers in these cases.  Water systems that installed only the treatment technology relied more

heavily on state officials and manufacturers to complete system installation.  In this case responsibility for
                                                28

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  technical effectiveness shifted to state officials and manufacturers, at least that was believed by the owners that
  utilized this approach.
  3.6.1   State Role
         In all cases, the state was responsible for providing assistance to water system owners and review and
  approval of the proposed improvements to the water system. In some cases the state officials exceeded this
  responsibility and provided greater assistance towatersystern owners through the identification and evaluation
  of alternative improvement technologies.  This approach was used by the Lima Brighton and Fruitland
  Domestic water systems  that relied on state officials  for assistance in  the.identification and evaluation of
 alternatives.  In  both cases,  the  owners were working by themselves  without the assistance of a consulting
 engineer. (Note: the Fruitland Domestic water system utilized an engineer to submit the permit application).
 State and EPA officials identified treatment options and other water source alternatives for the Lima Brighton
 system.  This evaluation was useful and provided a basis for the owners to begin the manufacturer selection
 and negotiation process.  The Fruitland Domestic water system relied on approvals from the state drinking
 water personnel that the bag and cartridge filter were appropriate for giardia cyst removal from surface water
 supplies.
        In the Green Cove  and Lost Lake  cases, state officials gave tentative approval of the treatment
 technology subject to adequate performance of the system  during actual operation. Ohio officials required
 full-time monitoring of the Multi-Tech system at Green Cove even though the system is theoretically designed
 to operate by itself. After further review of system performance, Ohio may permit automatic operation of the
 unit.
        The  extent of state  involvement in the installation of treatment technologies  in the other water
systems appeared to be limited to  the normal review process. In each of these cases a consulting engineer was
involved and  project development followed the "traditional  approach"  as,previously discussed.
3.6.2    Ixx:al/Third  Party Role
        Research efforts  at  Colorado State  University and certification from  the National Sanitation
Foundation were relied upon for the selection of the bag and cartridge filters.  The research evaluated the use
                                                 29

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 of bag filters for turbidity and bacteriological contamination control, specifically giardia sized particles, for



 surface water supplies.  The results of the research indicated that the technology was appropriate to remove



 turbidity, particulates and bacteriological contaminations from raw surface water, according to the contacted



 state officials and water system owners.  The selection of this technology for these systems was based on the



 research and approval from state drinking water personnel.



 3.6.3   Consulting Engineer Role



        Consulting engineers were used by most of the water systems evaluated in this study. Only the Lima



 Brighton, Fruitland Domestic and Lost Lake Camp facilities were installed without significant support by a



 consulting engineer. The Fruitland Domestic water system required a consulting engineer to sign and seal



 drawings for the intake facilities and treatment process although the services appeared to be limited.  While



 the Forest Service did not use a consulting engineer for improvements at the Lost Lake Camp, it did rely on



 engineers in the Service's Engineering Department to perform alternatives evaluation, system selection, design



 and layout, contract documents preparation, and construction and installation oversight.



        Consulting engineers were used by the Green Cove, Pineloch, Darboy, Readsboro, Barrick Goldstrike



 and Taycheedah water systems. The typical  services included the evaluation of water supply alternatives,



 evaluation of treatment technologies, preparation of design plans, specifications and contract documents,



 review and field monitoring during construction and installation, start-up services and preparation of operation



 and maintenance manuals. The extent of improvements installed at the Green Cove, Darboy, Readsboro.



 Barrick Goldstrike and Taycheedah systems required  the services of a consulting  engineer. The level of



 engineering services for each of the systems varied depending upon the needs of the owners and the project.



 The engineering services described above were performed by the consulting engineers for the Green Cove,



 Darboy and Readsboro water systems, according to the system owners. The extent of engineer involvement



 in the Pineloch, Barrick Goldstrike and Taycheedah was not identified due to  limited information provided



 by system owners. • However  it appears-that -most of the services described above were performed for .the



Barrick Goldstrike and Taycheedah systems, whereas an abbreviated scope of services  may  ha%-e  been



performed for the Pineloch water system since only the treatment technology was installed.
                                                30

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  3.6.4    Manufacturer Role                                                            	
          The manufacturers were responsible for the evaluation, design,  fabrication and in some  cases
  installation of the selected treatment technologies.  In cases where  the manufacturers did not install the
  equipment, the equipment suppliers working with assistance from the manufacturers, installed the equipment.
          In most cases the manufacturer/supplier was not involved in the permit approval process.  Two
  notable exceptions to this are the Green Cove and Lima Brighton water systems. The owners and engineers
  of the Green Cove water system were assisted by Culligan .representatives in the .permit approval process.
  Culligan provided documentation on the tested performance of the Multi-Tech filtration process and  helped
  convince the State of Ohio of the appropriateness of the Multi-Tech technology for the Green Cove system.
  The owners of the Lima Brighton water system also were assisted by the equipment supplier in the evaluation
  of treatment alternatives and selection of the appropriate technology for the school.
         Manufacturers of the equipment for the other water systems also provided documentation on system
 performance to the owners and consulting engineers however their role in the permit approval process was
 reduced.
 3-7      OPERATION AND MAINTENANCE
 3.7.1    Existing Procedures
        The extent of operation  and maintenance practices varied at each of the nine water systems. The-
 practices differed due  to treatment technology, type of water system and sophistication of operation, abilities
 of the operator and state' requirements. The larger'systems at Green Cove, Darboy, Readsboro, Barrick and
 Tavcheedah generally  had. more defined O&M practices thafwere performed by more qualified personnel.
        Ohio drinking water personnel required the highest level of operator certification,  of the systems
 investigated, and full-time monitoring of the water system during operation. Consequently, the Green Cove
 system appears to be one of the better  systems  investigated.  All  operations at the plant are manually
 controlled, however, the Multi-Tech, system ^equipped with an automatic controller.- To fill the clearwells
with  finished water.the operator starts the chemical feed systems and the Multi-Tech system.  After filling the
clearwells the operator shuts down the system.  Manual operation  of the system and monitoring during
                                                31

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 operation is required by the Ohio EPA. Backwashing the system is performed when the pressure differential

 or headless across the filters exceeds 10 psi.  Generally the system is backwashed every 15 to 20 hours of

 operation.  Currently the operator initiates and monitors and backwash cycle.

         The Readsboro system is operated by one full-time operator employed by the town.  The operator

 is also responsible for operation of the town's wastewater treatment system.  A part-time assistant operator

 is available to operate the system as needed.  The operator is not state certified for the treatment  system as

 Vermont has not instituted a certification process.  The operator is certified for the wastewater  treatment

 plant. Maintenance of the system is generally performed by the operator with assistance from the town's utility

 personnel (4 total) as needed. The operation and maintenance requirements are specified in an O&M Manual

 prepared for the water system. The water system is backwashed or cleaned prior to each water treatment run.

 Production runs vary from 15,000 to 20,000 gallons to a maximum of 190,000 gallons.  The Readsboro water

 system, while currently meeting, water quality standards, is having operational problems with chlorine  additions

 and chlorine residuals.  The consulting engineer that designed the Readsboro facility is not under contract,

 which makes it more difficult for the operator to receive technical assistance. Funding at the Readsboro plant

 also appears to be a  greater problem than at the other systems.

        The Barrick Goldstrike system also is currently meeting water quality standards.  The  system is

 monitored full-time, however the operator is not state-certified.  Maintenance of the system is  generally

 performed by the operator with assistance  from  other  Mine personnel, as  needed.  The operation and

 maintenance requirements are 'specified in an O&M Manual prepared for the  water system.' The normal

 operating parameters of the system are specified  in the Manual. The operator is required to check the

 feedwater supply for  the system periodically to determine whether adjustments to the treatment parameters

are required.  The  O&M  Manual  identifies normal maintenance requirements of the system.   Normal

maintenance includes replacing filter elements as needed, lubrication and alignment checks for the pumps and

valves, and inspectionof jhe overall system. The daily maintenance check-list specified in the Manual  includes:

        1.   Prefilter Pressure Differential
        2.  Silt Index Text Results (SDI)
        3.   Record all information on RO Operating Data  Sheets

-------
          4.  Run unit for 15 minutes if not in use (to control bacterial growth by rinsing
             out stagnant water).


          Evaluation of the performance of the Pineloch water system is limited due to the lack of available

  information and the breakdown of one of the two filter units during the study. Normal O&M practices at the

  Pineloch facility include daily checks of the system and chlorine additions. The system does not have an O&M

  manual available on-site.  Normal O&M is performed by the system operator.  The system does not have a

  formal maintenance agreement in place.


         The Fruitland Domestic water system operator is currently certified by the State  with a D license.

  In 1992 the level of certification is required to be upgraded to a C license. Normal operation and maintenance

 services include a twice weekly or as needed check of the system components, including the bag and cartridge

 filters. The bag filters are backwashed or cleaned  twice a week under normal operation.  Higher turbidity

 levels during spring floods or high water events may require more frequent cleaning of the filters. The filter

 cleaning procedure normally involves removal of the 10- and 5-micron filters from the system and backwashing

 the filters. The 1-micron cartridges are backwashed in place.  The 10- and 5-micron  bag filters are generally

 replaced once a year.  The  1-micron cartridge filter is generally replaced every three months.  (Note: more

 frequent replacement of the bag and cartridge filters is recommended, see Section 3.7.2.)  Normal operation

 and maintenance of the system is limited since there are no pumps or meters.  Water flows by gravity from

 the source to the  customer,  negating the need for pumps.  Occasional maintenance of the doles (flow

 controllers), installed on the customers lines, is.required to maintain water flow to the customers.

  .     .The operation of the Lost Lake Camp water system is manual. The campground operator, on a daily

 basis when the campground is open, checks the level of the finished water storage tank, to identify the total

 water available to the campground.  If additional finished water is required, the operator manually turns the

 generator and pumps on, and initiates the water filtration process. The operator performs the necessary water

 quality tests and records system data.  Following .the filling QfJhe5torage.iank.-the operator manually turns

 off the generator and pumps. When the system is on. it operates continuously with no operator effort required

other than periodic checking of the filer replacement status gauges.  Should filter changeout be necessary, the

system is shutdown and a new set installed.  The system is then restarted with very little effort and no


                                                33

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 adjustments to make.  Chlorine injection is'provided by the injection pumps when generated power is being



 supplied to the main system feed pumps. Whenever the main system feed pumps are in operation the chlorine



 feed pumps are also in operation to assure adequate system disinfection residual.



         When the system is in operation, the operator checks  the differential pressure across each filter



 housing as indicated on the respective gauges. When the differential pressure reaches 30 pounds per square



 inch (psi),  the filter should be replaced, according to the equipment supplier.  During actual pilot test



 operation, the filters were replaced when the gauges indicated 10 to 20 psi which may account for the high



 filter use during the test.  Daily checks are made of the chlorine solution level in the mix tank.  Additional



 solution is added as necessary.  The piping and tubing connections are also periodically inspected to identify



 leaks or areas where repair is needed.




        The Darboy water system is operated by a certified operator and supported by the District's consulting



 engineer.  The operator  is state certified  for groundwater systems,  distribution systems and the  zeolite



 treatment process. The operation and maintenance requirements are specified in an O&M Manual prepared



 for the water system. The water system is backwashed or cleaned after treatment of 135,000 gallons of water.



 The operator is not required to initiate backwashing since the system is automated with an in-line meter and



 system controller which monitors total water treated per cycle and initiates the backwash cycle.  Chemicals



 required for treatment include approximately 35,000 Ibs. of salt  per month and approximately 50  Ibs. of



 chlorine gas per month.  The equipment performance is monitored by flow meters and a telemetry system.



 Water quality parameters  are monitored by the Wisconsin Department of Natural Resources. Daily water



 quality analyses include hardness of the raw water, and hardness, pH and chlorine residual of the finished



 water.  The salt content of the brine solution is also monitored on a daily basis. Routine maintenance of the



system is performed by the plant operator and support personnel of the District. To date,  no significant



operational of maintenance problems have occurred.




        The Taycheedah facility is producing adequate water quality according to. the plant operator.  Specific



information on the,O&M  practices of the system, however, was not provided by the owner.
                                                34

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                                                    is
         The Lima Brighton water system is operated  by representatives of the school.  The system i
 maintained by the equipment  manufacturer under an annual maintenance contract.  Normal operational
 procedures for the system include weekly tests of the total dissolved solids (TDS) monitor, monthly Hushing
 of impurities from the  RO membrane and periodic monitoring of the filter  housings.  The water system
 supplier performs  filter replacement .and sanitizes the system under the annual maintenance contract.
 3.7.2    Suggested O&M Practices
         General operation  and maintenance requirements  and guidance is  provided.for the treatment
 technologies surveyed.
 Pressure Filter Units
         The performance of pressure filters should be monitored  frequently (or continuously if possible).
 Turbidimeters are available that can continuously measure the turbidity of the water filtered. Turbidity can
 also be measured regularly with "grab" samples and a  bench turbidimeter.  Turbidity measurement by grab
 sample is recommended every two to four hours. A sudden rise in turbidity, a turbidity "breakthrough" event,
 or an increase over a set turbidity limit, usually 0.5 turbidity units, indicates the need to backwash the filter.
 The filter is then backwashed with filtered water until clean (virtually clean if observation of backwash water
 is possible).
        Pressure filters must also be~monitored for the gradual development of headless through the  filter
 media.  Differential pressure gauges, or influent and  effluent pressure gauges, are normally installed on
 pressure filters to indicate headloss.  Filters should be backwashed-at a headless 
-------
         3. Regular backwashing. Keep records of backwash frequency and duration for each filter




         as well as headless and turbidity before and after a backwash. Be sure that the backwash rate




.  .       is sufficient to expand the media and flush out accumulated dirt.  Open the backwash valve




         slowly.




         4. Inspect the media regularly (at least once a year). Open the pressure filter and visually



         inspect  the media for loss of media (measure from top), mudball formation (inadequate




         backwash), caking, surface cracks, mounding, or unevenness.  Remove any  mudballs  and




         replace or add media as necessary. Mounds may indicate under drain problems to inspect and



         repair.




         5. Any pressure pumps, backwash  pumps, or additional equipment such as an air scour




         backwash assist must be maintained according to manufacturer's recommendations. Regular




         lubrication, checks of packing condition, and bearing noise or temperature observations are



         essential.




         6. Inspect and calibrate any gauges,  flow controllers or instrumentation on a regular basis.



         Repair or replace as necessary.



 Bag and Cartridge Filter Units




         Bag and cartridge filters can also be monitored for turbidity breakthrough and headloss (pressure drop




 or pressure differential).  Sudden turbidity increases or gradual turbidity increase over a preset limit indicates




 that the cartridge filter needs to be replaced and/or the bag filters should be backwashed or replaced depending




 on manufacturer's recommendations.  Turbidity of the filtered water can be measured continuously or with



 regular grab samples (every two to four hours).




         An increase of differential pressure (pressure,drop) from inlet to outlet indicates  that the cartridge



 filter is becoming  overloaded  with filtered material.  A filter inspection or replacement should take  place




 whenever a cartridge filter differential pressure increases 5 units from the initial differential pressure recorded




 when the filters are first put into service (inlet pressure - outlet pressure = initial differential pressure 4-5).



 Record pressure differential information daily.






                                                  36

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or
          The 10- and 5-micron size bag filters should be backwashed at least twice a week or more frequently

  if turbidity increases over 0.5 turbidity units. Each filter of that size should be replaced every three months

  of continuous use.  In addition, the filters should also be replaced when a pressure differential of 30 psi is

  measured across the filter.

      .    Filters smaller than  the 5-micron.size should be similarly monitored and replaced after one month

  of continuous use.

         Any gauge, instrumentation, or associated equipment should be inspected, calibrated, and maintained

  on a regular basis.

  Ion Exchange

         For ion exchange systems, the primary O&M requirement is periodic regeneration of the resin. With

 continued use, the resin capacity will also be reduced because resin effectiveness is never completely recovered

 by regeneration. When the capacity  becomes too low, the resin can be washed with either a strong acid

 base solution or it  can be replaced.  Replacement is often the more feasible option.

         Other operational concerns include suspended solids, manganese, and  iron. Control of suspended

 solids may require prefiltration. Iron and manganese can enter the resin bed as  soluble salt that oxidize into

 a deposit that  must be removed for the  beds to  remain operational.  Water  temperature should  also be

 monitored.  Each of these concerns should be adjusted when possible to meet the following guidelines:

                Iron            <5 mg/L
                Manganese     < 1 mg/L
       :        Turbidity      .  <5 NTUs
               Temperature    <140°F

        Concentrated brine used for resin regeneration must be disposed of properly.

        Product water may be corrosive enough to  require the addition of a corrosion inhibitor to avoid

elevated levels of copper, iron, or lead leached from household plumbing and/or shortening the life of the

plumbing fixtures.
                                                      4

        Anion exchange units  should be monitored for nitrates in  the effluent.  With most anion exchanges,

sulfate is preferred  over  nitrate which  reduces the nitrate  capacity of the  resin.   With  high  sulfaie

concentration previously exchanged, nitrate ions can be released back into  the finished water.

                                                37

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        Any associated equipment such as instrumentation and pumps should be inspected and maintained

at least as regularly as recommended in manufacturer's guidelines.

        High levels of organic material can also foul the resins.

Reverse Osmosis Units

        Typical RO plant operation includes the following items:

        1. Cartridge filters should be replaced whenever the pressure drop across the filter reaches

        15 psi.    '                                                  :	'

       2. Check chemical feeding equipment and adjust the feed rate to the desired dose (usually

       2 to 5 mg/L).

       3. Adjust feed and concentrate flow to establish the desired feed pressure and recovery rate.

       4. Check and record the differential pressure across  each stage of the RO unit.  When  the

       pressure increases, fouling is indicated and the membranes may require cleaning.

       Specific parameters to monitor include the following:

       1. Feedwater temperature and pH should be monitored on a regular basis as these will effect

       system performance.

       2.  Conductivity of the feed, permeate, and concentrate water should  be  done daily to

       determine any changes in membrane salt rejection properties.

       3.  Pressure of the feedwater and at the end of each membrane stage should be  measured

       daily. Changes in the pressure differences between stages indicate fouling or plugging of the

       membranes. The permeate discharge should also be measured and maintained less than  20

       psi to prevent damage to the membrane.

       4. Feedwater, concentrate and permeate flows should be monitored to ensure proper system

       recoveries are maintained.
                                             »
       5.  Associated  equipment.  Maintain and calibrate  any  pressure, flow,  and conductivity

       meters/gauges as well  as feedwater pumps at least  per manufacturer's guidelines.
                                               38

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         Product water may. be corrosive and require the addition of a corrosion inhibitor, to prevent corrosion
 in the distribution system.                                                                  .
 3.8     WATER SYSTEM COSTS
         Table 6 presents a summary of the available information on water system costs for each of the nine
 water systems. Total project costs, treatment technology costs and operation and maintenance costs are shown
 for each facility, if available, together with the associated cost per connection. Direct comparison of all the
 values shown  is not possible because the available information  was not  provided on a common basis.
 Estimates were made for some of the costs to try to achieve a level basis for evaluation. Note the costs shown
 are not at a common price level but represent the cost for the facilities at the time of installation. The date
 of installation varies for each of the systems.
         The Total  Project Cost column shows the identified total costs of the facilities installed during the
 improvement project. These facilities include the treatment equipment and the additional facilities required
 for each project, such as buildings, pipelines, storage tanks, wells  etc.   The total  cost per connection is
 generally less than S800, with the exception of the  Readsboro, Barrick (assumed) and Taycheedah facilities.
 The Readsboro facility incorporated substantial water system improvements.  The Barrick. and Taycheedah.-
 facilities included substantial  improvements for relatively small service populations.
        The Treatment Technologies Cost is the actual or estimated cost of the treatment equipment installed
 at each of the water systems. Estimates of these costs are shown in the cases where treatment equipment costs
 were not.identified separately from, project or water plant costs.  Estimates were made based on discussions
 with the owners.
        The Operation and Maintenance Costs shown for the Fruitland Domestic system is the total annual
 cost for operating the system including staff salaries, debt sen/ice, equipment maintenance and miscellaneous.
 The costs shown for Lima  Brighton includes only a one-time annual maintenance checkup by the equipment
supplier, since  the school purchased the system from  capital funds and operates the system with school
maintenance personnel. The Darboy and Readsboro costs shown include normal operation and maintenance
activities but do not include debt service costs for loan/bond repayment. In both cases, the.water system

                                                39

-------
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 utilized FmHA and state grants and loans to finance the improvements. The Readsboro water system received
 approximately 5800,000 in state and Federal grants  for the project. The cost shown for Lost Lake Camp
 includes debt service for equipment only and filter costs; but not operational costs which are incorporated in
 a separate contract to operate the entire Camp.
        The costs shown in Table 6 indicate that, in general, treatment technologies can be installed for S200
 per connection or less.  However,  if total project  costs are considered, the cost per connection ranges from
 S50 to 38,220.  These total project costs are not always considered in the operation and .maintenance costs
 since project costs may be incorporated into  the  development infrastructure costs  (i.e., Green Cove), paid
 through  capital funds  (i.e, Lima Brighton,  Lost Lake Camp, Barrick Goldstrike and Taycheedah) or
substantially offset Federal and/or state grants (i.e.,  Readsboro, Fruitland, Darboy).  The project costs will have
to be considered for communities and water systems that can not take advantage of these alternative financing
arrangements.
                                               41

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                                             SECTION 4
                                           CONCLUSIONS
                                                               /
        Nine small water systems were selected for evaluation as part of this study to assess Low-Cost, In-

Place Technologies at small water systems.  The nine systems represent different installed technologies,

different ownership types, several types of operation and maintenance strategies and different approaches to

improving the quality of their drinking water.  The installed technologies include pressure filtration units, bag

and cartridge filter units, ion exchange units and reverse osmosis units..  Systems range in size from 100

connections to 800 connections. Six systems are community water systems, two systems are non-transient non-

community water systems and one system is a transient non-community water system.

        In general, all of the systems meet the goal of improving the quality of their drinking water.  The

treatment technologies installed at the water systems are capable of reducing the level of the contaminant of

concern to below state standards according to the results of finished water quality analyses and discussions with

state personnel. The two bag and cartridge  filtration systems,  however,  rely on assessment of the overall

system design and performance, chlorine additions and third party certification to qualify as meeting state

standards.  Review of specific water quality analyses for one of the systems indicates that the filters do not

meet the exact standards, however the state has apparently approved the system based on its overall design.

        Operation and maintenance of the system is an important parameter in achieving effective operation

of each of the systems. Review of the procedures indicates that operation of most of the systems could be

improved with technical assistance and/or better qualified operators.

        The.specific conclusions of the study  are presented below:

        1. The type of treatment  technology and the extent of improvements installed at the water
       system were dependent on the reason for installation and financial  strength of the owner.
       Systems that were responding to requirements of the SDWA, generally installed only the
        treatment  technology.  Systems that were installed for  new or expanding  communities
       provided more extensive improvements in addition to the treatment technology. These latter
       systems also had greater financial strength to absorb the cost of improvements.

       2.  Water systems  need adequate  facilities,  qualified operators,  technical assistance and
       adequate funding to meet requirements of the SDWA.  Performance of the nine systems, even
       with adequate facilities, was impacted by the level of operator  training and qualifications.
       Better qualified operators were able to  adequately operate the facilities and  recognize
       problems and assess possible solutions. Less qualified operators may be capable of operating
                                                42

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  the system but appeared to lack the ability to identify problems and find solutions."~"The
  impacts on the finished water quality were most apparent for systems with changing raw water
  quality.

  3. Three techniques were utilized by the water systems to evaluate, select and procure the
  appropriate treatment technology.  The selected technique was dependent primarily upon the
  extent of required improvements and ability of the owner.  Systems that required "significant
  improvements in addition to the treatment technology utilized the."traditional approach,"
  relying on a consulting engineer to develop plans, specifications and bid documents to select
  and award installation contracts. Systems that installed only the treatment technology utilized
  the internally developed "lease purchase" approach or an "in-house purchase" approach. Each
  approach was appropriate for the facility to accomplish the required procurement. However
  the latter two approaches placed greater responsibility on the water system owners.

 4. Guarantees on the performance of the treatment equipment were required by all the water
 systems except Fruitland Domestic. The extent  of guarantees ranged from basic one-vear
 parts and labor guarantees, to equipment performance and serviceability guarantees   Some
 systems with engineering plans  and specifications identified more restrictive guarantees on
 system performance over time and  individual components.

 5.  The relationship among the owners, state officials, engineers and manufacturers and their
 roles in project development was dependent on the size and complexity of the proposed
 improvements.  Water systems that installed significant improvements relied on consulting
 engineers to evaluate alternatives  and develop  plans, specifications and  bid documents
 Responsibility for technical effectiveness and system performance rested with the consulting
 engineers in this case. Water systems that installed only the treatment technology relied more
 heavily on state  officials and suppliers/manufacturers for  alternatives evaluation, process
 selection  and performance. In  this  case, responsibility for technical effectiveness shifted to
 state officials and manufacturers, at least that was believed  by the owners.

 6.  Qualified water system operators are required to operate systems  as well as to identify
 problems and assess possible solutions.  Problems not identified (i.e., washing out bag filters')
 will not be fixed unless operators are qualified and can recognize the problems: Operators
 require technical assistance on a periodic basis to properly operate and maintain the facilities!

 7.  Low-Cost, In-Place Treatment Technologies can be installed for S200 per connection or
 less according to  the costs identified for the nine systems.  However,  the total cost for all
•required system improvements ranged from S50 to S8.220 per connection  depending on the
 condition and design of the existing facilities. The total project costs have to be considered
 by  communities and water systems  in  assessing the  feasibility and approach to installing
 system improvements.  '
                                         43

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                                             SECTION 5
                                       RECOMMENDATIONS

         The results of the study efforts indicate that treatment technologies for small water systems are

 available to provide effective treatment of surface water and groundwater sources to meet the requirements

 of the SDWA. The treatment technologies installed alone can be "low-cost" and affordable for small systems.

 However, if significant other improvements to the water system are required the costs can increase, impactin»

 the affordability of the needed improvements. •

         Additional operator training and continued assistance in the operation  and  maintenance of water

 systems, particularly small  water systems, is needed due  to  the increasing technical and administrative

 requirements of system operation. Assistance can be provided by state personnel, circuit riders, consulting

 engineers or equipment manufacturer representatives, experienced in water system operations.  In addition,

 use of performance guarantees on equipment operation can be used to guarantee satisfactory performance and

 operation of the system.

        Continued education of owners, state regulators and local engineers is required to encourage  the use

 of low-cost treatment technologies.   Information  is needed  regarding the treatment options  available.

 performance and  limitations  of treatment technologies,  ancillary  components such as water storage,

 transmission and distribution systems,  and  costs for treatment equipment  as well as  ancillary facilities for

 various water system sizes.  A  design manual developed for  each major treatment technology could provide

 needed information to aid in- the evaluation, selection, design  and operation of small water-systems.  The

 manual would be useful for the evaluation and selection of treatment technologies appropriate to small water

 systems as well as the identification of the ancillary components and procedures that may also be needed to

 meet regulatory requirements. The manual could present information and expected  performance data on

various sizes of each treatment technology to assist owners, state regulators, engineers,  and manufacturers in

 the selection of the appropriate system.  Specific components of the manual could include:

        *     Detailed description of the treatment processes.

        *     Detailed description of system components.
                                                44

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Investigation and discussion of contaminants that could be treated by the technology.

Investigation and discussion of system performance relative to raw water quality, chanees in
chemical additions and other operating parameters.

Detailed breakdown of water system costs for various sizes and types of systems. Costs could
be provided for treatment, storage, distribution and transmission facilities, as well as operating
and mamtenance requirements such as filter replacement and chemical additions.

Detailed description of  the operation and maintenance required  for  the water
including the level of effort and associated skill.
                                45

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        APPENDIX A




WATER SYSTEM DESCRIPTIONS

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                                            APPENDIX A
                                  WATER SYSTEM DESCRIPTIONS

  A.1     GREEN COVE CONDOMINIUM DEVELOPMENT

         The Green Cove Condominiums water system is a community water system that serves the potable

  water needs of the 750-unit recreational resort located along the shore of Lake Erie, near Oak Harbor, Ohio.

  The new water system was installed in mid-1987 and became operational in September 1987. The water system

  was designed to  reduce the levels of turbidity, bacteria and giardia from the surface water supply.

  A.1.1    Installed Treatment System

         The water treatment facilities installed at the Green Cove Condominiums include a raw water intake

  low service pump station, pressurized clarification and filtration system, granular activated carbon  filters.

 disinfection system and distribution facilities. The system was designed, manufactured, supplied and tested by

 Culligan International Company. The water system includes two separate trains consisting of a Culligan  Multi-

 Tech system with clarifier, depth filter and a granular activated carbon filter. Additional space is provided in

 the water plant for a third train, if needed, for future expansion.  The  system is designed to  produce  230

 gallons per minute (gpm) of treated drinking water. The system is controlled by a Programmable Controller.

        The following sections describe the installed equipment and the operation and control philosophy of'

 the system.                                    	

 A. 1.2   Raw Water Intake

        Raw water for the water system is obtained from a small cove connected to Lake Erie.  The cove is

 surrounded by the Green Cove Condominium  units.  The raw water intake is located approximately 6.5 feet

"below the low lake level, about 1150 feet from the low service pump station. The intake is screened and

 surrounded with rip-rap, and has dual openings to minimize icing problems.

 A. 1.3    Low  Service  Pump Station

      •  The main low service pump station is equipped with three submersible.turbine .pumps, one rated  for

 115 gpm at 50 feet total  discharge head (TDH) and the other two each rated for 230 gpm  at 47 feet TDH.
                                              A- 1

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 The emergency intake low service pump station is equipped with two submersible turbine pumps, each rated




 for 115 gpm at 50 feet TDH.  One pump in each pumping station is a standby.




        Each low service pump station is equipped with a check valve on the discharge side and an air release




 valve. Each pump station is housed in a 6-foot inside diameter by 21-foot deep concrete manhole. A 4-foot




 square locking aluminum door provides access for maintenance. Both pump stations can discharge into the



 6-inch polyethylene low service pressure main to the plant.



 A.1.4   Treatment System                                                     '    .




 Chemical Feeders




        Two chemical feed systems are available to supply alum and either chlorine or polymer to the raw



 water supply.  Alum is added from an 80-gallon polyethylene solution tank with a tank-mounted mixer. A




 second 80-gallon polyethylene solution tank system is available for the mixing and adding of polymer to the




 raw water.  Currently, polymer is  not added because good quality  water is produced with only the alum




 addition, thereby reducing chemical  costs.   Chlorine  is added  to the raw water as an oxidant to oxidize



 dissolved metals and provide some disinfection.



 Clarification and Filtration




        The system includes one Culligan Multi-Tech Depth Clarifier and one Culligan Multi-Tech Depth




 Filter for each of two treatment trains. The feedwater, following the addition of alum, is passed through a



Clarifier and a filter to reduce the levels of turbidity and remove suspended solids.




        The system includes Multi-Tech 72-inch diameter depth clarifiers with 60-inch sideshell heights. The




clarifiers are designed for bulk turbidity removal in order to limit solids loading on the polishing filtration




step.  Culligan has rated the clarifiers at 7 gpm/sq. ft. of media, however the Green Cove units  are approved




 to operate at 4 gpm/sq.ft. (the maximum allowed without high rate demonstrations).  Following clarification




the pre-treated water passes through Multi-Tech 72-inch diameter multi-media filters. The filters have a 60-




inch sideshell height.  The filters remove suspended solids to improve water quality of the effluent to less than




the maximum state turbidity level of 1.0 NTU. Currently, the system  is  producing filtered water at 0.1  to 0.2




NTU based on an analysis of samples taken after the granular activated carbon filters.






                                             •  A-2

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          The system is designed to produce 320,000 gallons of water per day at 4 gpm/sq.ft. of filter bed area,



  as required by Ohio EPA.




          The system can be backwashed based on time of operation or pressure differential as maintained by



  a Programmable Controller  (PC).  Manual reconditioning, as  is currently the practice at the Green Cove



  facility, is available by push button.  Pressure gauges placed before and after the units indicate the need for



  backwashing.  The PC-Panel contains status lights to indicate the status of operation of the system:  green light



  for in service; red light for backwashing; and amber light for standby. -      	•••••••   - •



  Granular Activated Carbon Filter




         A granular activated  carbon filter (GAC) is provided on each of the two treatment trains. The GAC



 filters are designed to remove  objectionable tastes and odors as well as to further reduce  turbidity. The



 loading on the filters is 4 gpm/sq. ft.  The filters are 72 inches in diameter and 84 inches in sidewall height.



 Clearwells
                                                        v



        Two 100,000 gallon underground clearwells were installed for finished  water  storage instead of an



 elevated tower because of cost  and low water usage during winter months. The clearwells  are  30 feet in



 diameter  and  19.5 feet deep.   At the design flow of 226 gpm, 7.6 hours of theoretical detention time is



 provided in each clearwell.  Piping is arranged to allow series or parallel operation of the clearwells as well



 as taking either tank out of service.—-          ~           -                 '               -    -




        The clearwells discharge into a 12,700-gallon high service suction well.  Three high service pumps,



 submerged in the^uction well,  are provided.  Two pumps are rated at 135 gpm at 130 feet TDK, and the third



 pump is rated  at 40 gpm at 134 feet TDK  The pumps discharge into a 6-inch ductile iron pipe to the



 distribution system.



 Disinfection




        Chlorine is added to the filtered water prior to the clearwells, for disinfection. Chlorine dosages are




adjusted to maintain 1.5..to-2:0 mgA-chlorineresidual-in the finished water.	'
                                               A-3-

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 Backwashing




         Backwashing the Green Cove system is performed after each service run, usually after each 8 to 12




 hours of system operation. Each treatment train is backwashed as a unit. Backwashing is performed manually,




 primarily to satisfy the Ohio EPA requirements for close monitoring of the system. The backwash cycle could



 be regulated by time, pressure differential or effluent turbidity.




         The backwash loading on each separate unit process in the treatment train is  14 gpm/sq ft.  The




 duration of the backwash cycle is 10 minutes which includes 6 minutes of air scour for the  clanfier only.




 Following the backwash a 113 gpm downflow rinse cycle is initiated for a duration of 5 minutes. The waste




 backwash water and the rinse water is pumped to a settling pond which discharges to a 250 acre marsh and



 then to Lake Erie. The source of the backwash water is the finished water from the high service suction well.




 The clarifier and filter rinse water is chemically treated raw water while the GAC rinse uses finished water.



 A.2      PINELOCH SUN BEACH CLUB




 A.2.1    Installed Treatment System




     ,   The Pineloch Sun Beach Club water system  is a community water system that serves the potable water




 needs of the 400-unit recreational community located in Ronald, Washington. The water system was installed



 to reduce high levels of iron, manganese and sulfide in the raw water, which is obtained from an old coal mine




 shaft near the water system.  The water system currently serves the needs of  10-18 full-time cabins and about




 210 part-time occupancy cabins.  The installed treatment system includes a Hydrosystems,  Inc.  multi-media



 pressure filter with ion exchange media and chlorination.




        The Pineloch water system was having mechanical problems with one of the two filter units at the




 time of the site visit.  The system operator indicated  that a spacer washer on the backwash timing, mechanism




 broke during operation which prevented the filter unit from being backwashed. At the time of the site visit.




 the unit had been out of operation for about 2 months. The replacement part was on order with the supplier/




 manufacturer, however apparent problems-between the owners, supplier and manufacturer delayed the delivery




of the replacement part.  Information from the supplier/manufacturer was not available to assess the reasons



for the problems.
                                               A-4

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          Available information on the Pineioch water system was limited due to the above described problems.
  A.3     LIMA BRIGHTON ELEMENTARY SCHOOL
          The Lima Brighton Elementary School water system is a non-transient non-community water system
  that serves the drinking water needs of the students and staff of the elementary school, located in Howe,
  Indiana.  The water system was installed  in June 1990 to  reduce the level of nitrates  from the existina
  groundwater supply.  Testing performed by EPA indicated that nitrate concentration in the groundwater supply-
  exceeded drinking water standards. As a result, a reverse osmosis water treatment unit was installed to reduce
  the level of nitrates in the drinking water supply.
 A.3.1   Prior Water System
         The area surrounding Howe is primarily agricultural.  The water system at  the elementary school.
 prior to June 1990, included a groundwater well  and piping to the school. No water treatment facilities were
 provided in the system.  The groundwater well was approximately 45 feet deep.
         The results of water testing conducted by EPA, in 1988, indicated that the raw water had nitrate levels
 in excess of the established maximum contaminant level  (MCL).  EPA identified three possible causes of the
 nitrate contamination in the drinking water source:  (1) overfertilization of an agricultural field in the vicinity
 of the source; (2)  leaking septic tanks near the source; and (3) a barn or feedlot near the source.
         EPA also identified three possible alternatives to obtain an acceptable drinking water supply.  The
 alternatives included:  (1) purchasing water from a neighboring water  utility; (2) construction of a new well
 into a groundwater aquifer of acceptable water quality; (3) treating the existing groundwater source.
 A.3.2    Installed Water System
         In January 1989, representatives of the Lima Brighton Elementary School  began an investigation of
 water treatment alternatives to reduce the  level of nitrates in  the drinking water supply.   Several water
 treatment equipment suppliers were contacted to obtain information on treatment  options.  Hawkins Water
 Tech. Inc. proposed two alternatives to treat  the nitrate problem at the elementary school: The first option
was an anion exchange unit using a strong base anion resin in the chloride form to remove the nitrate. The
second alternative would be to use a reverse osmosis system.  Both options were considered appropriate lor
                                               A-5

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 the removal of nitrate from the water supply. Initial comparisons of the two technologies indicated that the




 anion exchange unit would have the lowest initial capital cost.  However, the reverse osmosis would have a




 lower long-term operational cost.  Based on the results of the technical and parameters and cost, a Water




 Factory Systems HP-400 Reverse Osmosis Treatment System was selected for the Elementary School.




        The Water Factory Systems 'HP-400  system was  installed in August,  1990.  The unit produces




 approximately 250  to 280 gallons  per day (gpd) of treated water for potable use in the school.  Nitrate



 reduction through the reverse osmosis process is from approximately  14.0 milligrams per liter (mg/1) in the



 raw water to less than 1.0 mg/1 in the finished water.




        The HP-400 includes a 5-micron cartridge prefilter, the reverse osmosis unit, a pH control filter



 adding calcite to control corrosivity, a granular activated carbon (GAC) filter, storage and repressurization




 tanks and post-treatment GAC filters at each point of use (5 sites) in the school.  The system has a raw feed




 water pressure requirement of 20 to 85 psi.  A self-contained pump raises the line pressure to between  180




 and 200 psi for greater water production and efficiency. The treated water recovery is 25 to 30% and  the




 typical Total Dissolved Solids (TDS) rejection is greater than 96 percent.



 A.4     FRUITLAND DOMESTIC WATER COMPANY




        The Fruitland Domestic Water Company is a community water system  serving approximately 100



 customers in the area surrounding Crawford, Colorado.  The Company's customers and owners are ranchers




 and farmers located in a distribution  area encompassing 75 to 100 square miles near Crawford.  The water




system was built in Stages over the last 20 years, with the latest modifications, addition of the bag and cartridge




 filters, in 1984.   The bag and' cartridge filters were  installed to  remove  turbidity  and bacteriological



contamination, specifically giardia.



A.4.1    Water Svstem




        The Fruitland Domestic Water Company is located on the Fruitland Mesa near Crawford, Colorado.




Crawford is located in an aridrmountain*desert portion of western Colorado approximately 30 miles southeast



of Grand Junction, Colorado. The availability of water  in the area is limited.
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          The water supplied to most Fruitland Mesa residents is from Crystal Creek, which originates in a




  valley fifteen miles south of Crawford. The water from Crystal Creek enters the water system through 800 feet




  of perforated pipe buried seven feet beneath Crystal Creek, within the stream bed. The water Hows through




  1300 feet of pipe to the  chlorinator system.  Chlorine is added as needed to disinfect the  raw water and




  provide a residual. After the chlorinator, the water flows approximately 10 miles to the filter house containing




  the bag and cartridge filters. After the filter house, the finished water enters approximately 8 to 10 miles of



  distribution piping to the individual customers.                                •    «  r



  A.4.2   Water Treatment Svstem




         The initial water treatment system installed by the Fruitland Irrigation Company - Domestic Company




  included an infiltration gallery as the water intake facility, chlorinator and transmission and distribution pipina.




 The water system operated by gravity and delivered water to each customer on a continuous basis.  Water




 control valves or doles were installed on each customer's connection to control the amount of water to each




 user.  Each resident has a storage tank or cistern to store water until needed. Excess flow not  used by the



 customers is bypassed.




         In the early 80's, a spring flood on Crystal Creek (water source) damaged the infiltration gallery by



 removing some of the filter media surrounding the perforated pipe.  Unfiltered surface water entered the




 pipeline and was distributed to the water customers. Several of the users became sick, some with'giardiasis"  '




 Complaints to the state drinking water personnel resulted in requirements to filter the surface  water supply.




    . :.  The water system owners investigated various options  for filtering the surface water supply.  A local




 engineer designed changes to the infiltration gallery.  Discussions with state drinking water personnel and




 recommendations from a Dr. Charles Hibler at Colorado State University, resulted in the selection of bag




 filters as the appropriate technology to remove turbidity, particulates and bacteriological contamination from




 the raw water.  Dr. Hibler had  been researching the use of bag filters for  turbidity  and bacteriological




contamination control  for surface water supplies. The results  of his  research indicated that the technology



was appropriate for the Fruitland water system.  The selection of this technology was made based on the



recommendations of Dr. Hibler and approval from the state drinking water  personnel.
                                               A- 7

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        A preliminary design of the filter system was prepared by the water system owners, Dr. Hibler and




 the state representatives. Final design documents were submitted by a local engineer to the state for approval.




 Piping and bag filter units were enclosed in a simple concrete block house. No pumps were required for the




 system, as the water flows by gravity from the intake to each individual customer's storage  tank.




        The filtration system consists of two interconnected parallel flow paths containing a  10-micron bag




 filter unit followed by a 5-micron bag filter unit followed by a 1-micron cartridge  filter unit. The parallel




 system was installed to provide a backup during filter-cleaning  and/or bag or cartridge replacement in order




 to maintain a constant flow of water through the system.




        The 10-micron and 5-micron bag filters are contained in Filter Specialists, Inc. FS-800 filter housings.




 Six 10-micron bag filters and  four 10-micron bag filters are installed in two FS-800 multi-bag filters that



 operate in parallel. Three 5-micron bag filters are installed in  an additional FS-800 multi-bag filter located




 downstream of the 10-micron filters. The 1-micron cartridge filters are contained in two Brunswick Technetics,




 Filterite C-150 MSO High Flow Filter units. The two units contain forty-four 1-micron cartridges and twenty-



 two 1-micron cartridges, respectively.  The units are also operated in parallel.




        Start-up of the  new filtration system occurred in  1984.  Initially, the system contained the 5-micron




 bag filters and the 1-micron cartridge filters. An excessive amount of turbidity was being collected in the 5-



 micrdn bag filters, which caused clogging and required numerous filter changes. The 10-micron bag filters




were then installed upstream to remove large particles, thereby reducing the amount of turbidity to be removed




by the 5-micron bag filters. Following installation of the 10-micron-bag filters, turbidity removal has been high



and bag filter replacement has been minimized.



A.5     LOST LAKE CAMP




        In 1989, the U.S. Department of Agriculture, Forest Service investigated alternatives for the addition




of a water treatment system at the"Lost Lake Camp to meet the  Surface Water Treatment Rule requirements




of the State of Oregon.  Lost Lake Camp is a campground located in the Mount Hood National Forest near




Hood River, Oregon. The Camp is owned by the U.S. Department of Agriculture, Forest Service and operated




through contract arrangements.  Lost Lake is located ten miles northwest of Mt. Hood and about one mile
                                              • A-8

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  east of the crest of the Cascade Mountain Range. The total surface, area of the lake is 290 acres and it has




  4.4 miles of shoreline. The lake is about 5,400 feet long and 4,150 feet wide at its greatest point and 167 feet




  deep.  The lake is 3,100 feet above sea level and is generally accessible from  mid-May until snow blocks the



  road, usually late October.




  A.5.1    Prior Water Svstem




          The water system at the lake provides potable water supply to approximately 140 campsites in the




  campground.  The system is operated only during the  time the campground is open, usually May through




  October.  Prior to 1989 the system consisted of a water intake located  about 60 feet from the shoreline and




 5 feet below surface. The water was chlorinated and then pumped to a storage tank and then distributed to




 the individual  campground sites.  A small spring was also used at times as a water source, although water



 supply was not always reliable.  Attempts to drill a groundwater well were unsuccessful.




         Prior to passage of the Safe Drinking Water Act Amendments  of 1986, the State of Oregon allowed




 the Forest Service to operate the system without filtering based upon  the "unlikely" event of a  giardia  cyst




 entering the pump intake located 60 feet from shore and 5 feet deep.  Following passage of the Amendments




 and the Surface Water Treatment Rule, the waiver to filter water at Lost Lake was no longer acceptable to




 the State Department of Health. As a result the Forest Service began an investigation of alternatives to meet



 the filtration requirements.



 A.5.2   Filtration Options




        The  Engineering  Department within the Forest  Service at Gresham, Oregon evaluated  various



 alternatives to meet the filtration requirements. The alternatives included both conventional technologies and




 alternative technologies that required review by the State of Oregon. Several technologies were investigated




 to meet the filtration requirement of the Surface Water Treatment Rule:  Conventional Rapid Sand filtration;




 Direct Rapid Sand  filtration; Slow Sand  filtration; Diatomaceous Earth filtration; and Cartridge filtration.



The results of the evaluation by  the Forest Service indicated that cartridge filters appeared to be the most




feasible method. Lake water is consistently below 1.0 NTU for turbidity which indicated that cartridges could



be competitive with the other forms of filtration.                                       .   •
                                               A-9

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          To confirm the results of the initial investigation, a pilot test was conducted to demonstrate the

  effectiveness of the cartridge filtration process to remove giardia-sized particles. The pilot test using cartridge

. and bag filters was initiated in July 1989.  The results of the pilot test indicated that cartridge and bag filters

  were appropriate for the Lost Lake Water System.

  A.5.3    Selected Water System

          The water  treatment system selected for the Lost Lake  campground was a CENSYS 3MB-921

  filtration system.  The system was selected based on  the results of the Pilot Test.' Tfie system is a" skid-

  mounted self-contained filtration plant designed for the removal of Giardia lamblia cysts from drinking water.

  The system also provides for significant reduction of turbidity and chlorine injection capability for control of

  viral and bacteriological contamination.

         The water system consists of  the following:

         Flow Rate:         55 gpm

         Prefilters:          Two CUNO stainless steel housing, in parallel, with 5-micron/25-micron
                            cartridge  filters (each housing holds 5, 30-inch cartridges).

         Final Filter:        Two 3M NS122 stainless steel housings, in parallel, with a 3M 525A bae
                            filter.                                                            &

         Flow Meter:        Battery operated  flow meter with totalizer Signet Model MK586.

         Chlorine Metering  Precision  metering pumps. Series 11000. One for
         PUMP:            prechlorination, one for system chlorination.

         Other Features:    Differential pressures gauges on filter housings.
                           Drain valves and  air release valves on each housing.
                           Isolation ball valves.

        The instrumentation provided  indicates the rate of water flow, total amount of water passed through

the system,  and the differential pressure across each filter housing.

A.6     DARBOY SANITARY DISTRICT

        In late 1989 and early 1990, the Darboy Joint  Sanitary District  installed a new pump station and

groundwater well pump and zeolite softeners, and modified the existing chlorination equipment at the existing

water treatment facilities. The new system started operation in March, 1990. The facilities were installed due
                                               A - 10

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  to expansion of the customer base and the need for water supply for future system growth.  The water
  softeners were installed to reduce the hardness and combined radium 226 and 228 of the incoming raw water.
  A.6.1  Existing Water System
         The Darboy Joint Sanitary District water system sewes approximately 2,000 people in the vicinity of
  Appleton, Wisconsin.  The water system utilizes two groundwater wells as its source of water supply.  Both
  wells are located at the water treatment plant in Darboy. .Well No. 1 is 575 feet deep and Well No. 2 is 595 .
  feet deep.  Well No. 2 was added during expansion of the water treatment system.
  A.6.2   Installed Water Treatment System
         The water facilities installed in 1989 and  1990  included an addition to the existing pump station to
  house Well No. 2 and the softening equipment. Wells  No. 1 and No. 2 were designed to be operated on an
  alternating basis with water from both wells to be treated by the softening equipment.  The softeners were
  expected to reduce the hardness from 512 milligrams per liter (mg/1) to 65 mg/1 or 30 grains/gallon down to
 3.8 grains/gallon and to reduce the combined radium from  5.1 pico curies per liter (pCi/1) down to 0.9 PCi/l.
 Pump Station

        A 40 foot by 56 foot masonry addition was constructed on the north end of the existing pump station.
 The building includes a pump and softener room, storage garage, maintenance and meter repair rooms and"
 storage room.                             .            _
 Well Pump  and Discharge Piping
        -I^e installed well pump was a vertical turbine  pump with a capacity of 550 gpm at 515 feet total
discharge head (TDH). The 100 horsepower (hp) water lubricated pump was set at a depth of 350 feet. The '
well was equipped with a well vent and airline with altitude gauge.  The well discharge piping includes  a"
pressure gauge, pump control-valve, check valve, smooth end sampling tap, butterfly valve and meter.  The
pump control valve allows wasting a set amount of water on pump start-up. The wasted water,  high in taste
and odor, discharges to,an adjacent ditch.                      •     ...
       TTie  discharge piping from Well No. 1 was modified to route the water through the softeners.     .
                                             A- 11

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Softeners



        Two Tonka Water Treatment Company zeolite softening units were installed. The softener tanks are




96 inches in diameter and have a straight side sidewall height of 108 inches. The tank height is sufficient to




allow up to 75% expansion of the 54-inch deep zeolite bed.  Each tank holds 225 cubic feet of 20,000 grain




zeolite media.  Based on an influent hardness of 512 mg/1, each softener was designed to produce about



150,000 gallons of zero hardness water before regeneration was required. During actual operation this value



was reduced to 135,000 gallons of softened water before regeneration.     "        ..,..,...




        During normal operation 484 gallons per minute passes through the softeners and 66 gallons  per




minute  is bypassed and blended with the treated water to reduce its aggressiveness. The flow  through each




softener is 242 gallons per minute.  With a cross sectional area of 50.25 square feet and a flow of 242 gallons




per minute the normal flow through the media is 4.8 gallons per minute per square foot.




        The softeners are regenerated with water from the system.  One thousand three hundred and fifty




pounds  of salt is required to regenerate each softener. The brine distributor system in each softening tank




distributes the brine over the entire area of the zeolite bed. The regeneration of the  softeners is initiated



automatically based  on  the volume of water  treated and controlled by a pilot valve.  The softeners  are




equipped with  air relief valves, pressure gauges, water  meters  and sampling taps.   The softened water




discharges to the distribution system. Bypass piping is, provided for the softeners.



Salt and Brine Storage




        Salt is stored in a 12-foot by 12-foot by 10-foot deep underground concrete tank.  The volume of




makeup water is regulated by a float control and distributed above the normal water level in the brine tank.




A reduced pressure backflow preventer is provided on the feed line. A. 50-gallon per. minute brine pump




supplies the brine from the brine tank to the softeners during the regeneration cycle.



Chemical Feed Equipment




       An additional-regulator was provided and  dedicated for We'll'No'."2." The chlorine solution is piped



from the chlorine room and injected into the softener discharge line.
                                               A-  12

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   Wastewater
          The backwash, brine and rinse waters discharge to a holding tank beneath the building.  The holding
   tank discharges to the sanitary sewer at a rate that is limited to 50 to 90 gpm.
   A.7    READSBORO WATER TREATMENT FACILITY
          The Readsboro water system is a community water system that serves the potable water needs of
   approximately 400 people in the town of Readsboro, Vermont.  The new water system was installed in 1989
   to meet the requirements of the Surface Water Treatment Rule. Prior to installation of the water treatment
   system, water flowed directly from the raw water intake to the distribution system. The new water system was
   designed to provide filtration and reduce the level of turbidity from the existing surface water supply.
   A.7.1   Existing Water System
          The water system  includes a water  treatment facility,  a 275,000 gallon storage tank,' 12-inch water
   transmission main and water distribution mains, which are  8-inch, 6-inch, and 4-inch in size.  The  svstem
   consists of primarily branched  pipes with only one loop in the system.
          The source of water is the Howe Pond Brook.  The source is treated at the water treatment  facility
  and pumped to the 275,000 gallon storage tank via booster pumps located inside the water treatment facility.
          The water treatment facility, 275,000-gaUon storage tank, and approximately 1,000 linear feet of 12--"
  inch transmission main are improvements  that  were  made and put into service in 1989.  The 12-inch
  transmission main was constructed from the 275,000 gallon storage tank to a previously installed 6-inch water
  main east of Jarvis Road and two previously installed 6-inch water mains on  Harriman Station Road.
         Most of the  distribution system, constructed about  1890,  is approximately  100 years  old.  The
- exceptions are the 8-inch main from the Howe Pond Brook catchment area constructed in 1910, a 6-inch main
  on Route 100 across the Deerfield River  bridge constructed in  1957, a 4-inch main from Main Street to the
  school constructed in  1961, a 2-inch main serving Glen Avenue constructed in 1968, and a 6-inch main along
  East Main Street constructed in 1970. The distribution svstem  was constructed of unlined cast iron pipe.
  A-7.2   Water Treatment Svstem
         The Readsboro treatment process consists of booster pumps, chemical addition, clarification, filtration,
  and chlorination.  The booster pumps increase the  influent raw water pressure to  overcome the headloss   .
  through the treatment svstem and to boost finished water up to the new storage tank. Sodium  hydroxide.
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 alum, and polymer may be injected prior to clarification. These chemicals are injected by metering pumps.


 The clarifiers and filters are a package system supplied by Culligan International Company.  The package
                                                                                  i

 system consists of two treatment trains, each train capable of producing 35 gpm, 70 gpm total or 100,000 gpd.


 Backwash of both the clarifiers and filters can be started automatically but is generally initiated manually prior


 to each treatment run. Following treatment, chlorine, a corrosipn inhibitor (Aqua-mag), and sodium hydroxide


 can be injected.  Finished water.is retained in the chlorine contact tank prior to entering the distribution


 system to obtain sufficient contact time for disinfection.


        Wastewater from the system backwash cycle flows to the Town's wastewater treatment plant.


 Booster Pumps


       Two Peerless Pump booster pumps are provided to add pressure to the incoming raw water.  The


 pumps are located in the treatment plant just downstream of the incoming raw water line. The pumps are


 rated at 70 gpm each at 48 feet Total Discharge Head (TDH).


 Chemical Feeders


       The treatment system includes chemical feed systems to supply sodium hydroxide, alum, and polymer


 to the raw water supply and Aqua-Mag and chlorine to the finished water supply.  Each feed system includes  -


 one 50-gallon solution tank with mixer, one 0.24-24 gallon per day (gpd) Liquid Metronics, Inc. metering pump


 and one injection quill.


 ClarificatiQn and Filtration


       The feedwater, following the addition of sodium hydroxide, polymer and alum, is passed through a


 Culligan  Duplex MT-36D System.  The system is  comprised of two identical trains which are  designed to


operate concurrently with each other. Each train consists of a clarifier, filter, solenoid panel, pneumatic valves.


 manual valves, and other pertinent equipment and piping.


       The system includes two 36-inch  diameter •clarifiers with 60  inch sideshell heights. The units arc


designed to process 35 gpm each, at an  operating pressure of 20-100 psig. The clarifier is designed for bulk


turbidity removal in order to limit solids loading in the polishing filtration step.  Following clarification the


pre-treated water passes through the 36-inch diameter multi-media filters. The filters have 60-inch sideshell


heights. The filters remove suspended solids to improve  water quality of the effluent to less than 1.0 NTU.
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         Both trains of the system can be backwashed based on time of operation or pressure differential as
  maintained by a programmable controller (PC). Inputs to the PC are the storage tank, water level, differential
  pressure and turbidity.  Manual reconditioning, as is currently the practice  at  the Readsboro facility, is
  available by push button. Pressure gauges placed before and after the units indicate the need for backwashing.
  The PC Panel contains status lights to indicate the status of operation of the system: green light for in service;
  red light for backwashing; and amber light for standby.                                                . -
  Post-Treatment System
         Chlorine and Aqua-Mag (trade name) are added to the product water following filtration to provide
 disinfection and corrosion control.
    *
 Chlorine Contact Tank
        A chlorine contact tank (CCT) is provided to allow sufficient detention time such that the disinfectant
 can react with the finished water.  Proper chlorination and detention time will inhibit microorganisms in the
 finished water and provide a chlorine residual to maintain this condition throughout the distribution system.
 The CCT is a buried 8-ft. diameter, 18-ft.  long, 6,257-gallon steel tank.  The tank provides 90 minutes of
 detention time at design flow and working  pressure of 150 psi.
        Treated water flows from the chlorine contact tank to a 275,000  gallon reinforced concrete storage-
 tank and to the  distribution system.
 A-8     BARRICK GOLDSTRIKE MINES. INC.              ~ . '     "
        The Barrick Goldstrike water system is a non-transient non-community water system that serves the
 potable water needs of the mine's 1,100 employees. The Barrick Goldstrike Mines, Inc. facility is located near
 Elko, Nevada. The new water system was installed in mid-1990 and became operational in August 1990. Prior
 to installation of the water system  the Company used bottled water for its potable water needs.  The water
system was installed because of the expected expansion of the mine and the high cost of bottled water.  The
new  water system was designed to reduce the levels of arsenic, turbidity, and salt density  index from  the
existing groundwater supply.
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  A.8.1   Installed Treatment System


         The water treatment facilities installed at the Barrick Goldstrike Mines include a pretreatment system,


  a reverse osmosis system and a post-treatment system. The system was designed, manufactured, supplied and


  tested by Culligan International Company.


         The system is designed to produce 56 gallons per minute (gpm) of treated drinking water. The system


  components include  a  Multi-Tech System with  Alum and Polymer feeders, a Polymer Trap,  Acid and


  Antiscalant Feed Systems, a KP-90 Reverse Osmosis System and a Forced Draft Type Decarbonator.  The


  system is controlled by a Programmable Controller.

                                                                                               #
  A.8.2   Pretreatment System


  Chemical Feeders


         The pretreatment system includes two chemical feed systems to supply polymer and alum to the raw


 water supply. Each feed system includes one 50-gallon solution tank with mixer, one 0-24 gallon per day (gpd)


  metering pump, and one injection quill.  A common 3-inch in-line static mixer is located downstream of the


 injection quills for mixing the chemicals with  the feedwater.


 Clarification and  Filtration


         The feedwater, following the addition of polymer and alum, is passed through a clarifier and a filter


 to reduce the levels of  turbidity and the silt  density index  (SDI) value.  The system includes one  54-inch


 diameter clarifier.  The clarifier is designed for bulk turbidity removal in order to limit solids loading on the


' polishing filtration step.  Following clarification the pre-treated water passes through a 54-inch diameter multi-


 media filter. The filter removes suspended solids to improve water quality of the effluent to less than 1.0 NTU


 and the SDI to less than 5.


        The system is designed to operate at  90 gpm.  Actual operation is based on 75 gpm of raw water


 passing through the filters.


        The system can-be backwashed based on time of operation or pressure differential as maintained by


 an Allen Bradley Programmable Controller (PC).  Manual reconditioning, as is currently the practice at the


 Barrick facility, is available by push button.  Pressure gauges placed before and after the units indicate the




                                               A - 16

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  need for backwashing.  Whenever the pressure drop across the filters exceeds the original (when the filters
  were clean) pressure by 10 psi, manual reconditioning is initiated.  The PC panel contains status lights to
  indicate the status of operation of the system: green light for in service; red light for backwashing; and amber
  light for standby.
  Polvmer Trap
         The filtered water from the Multi-Tech System may contain excess polymer.  The polymer, being a
  cationic nature, may react with the anionic antiscalant and also has the potential to foul the Reverse Osmosis
  membranes. The automatic polymer trap removes any excess polymer from the Multi-Tech process.
         The PC controls the operation and regeneration of the polymer trap.
 Acid Feed System
         The addition of hydrochloric acid (HCI) is used to control salt precipitation and subsequent scaling
 of the RO membranes.  Hydrochloric acid is used instead of sulfuric acid due to barium in the feedwater.
 Under design conditions, 38 ppm of 100 percent hydrochloric acid is required to lower the feedwater pH to
 approximately  7.15.  This pH produces  a  +1  Langelier Saturation Index (LSI) in the RO wastewater
 concentrate. The antiscalant is able to prevent calcium sulfate and calcium carbonate precipitation at this LSI.
 level.
 Antiscalant Feed System             .
        The antiscalant, Rocon 100, is  used  to delay the precipitation of soluble salts in the'concentrate
 (waste) stream, reducing the possibility of salt precipitation and subsequent scaling of the RO membranes.
 Under design conditions, 12 ppm of antiscalant solution is added to the feedwater. The dosage of antiscalani
 added to the feedwater is dependant on the raw water characteristics; variations in  fluoride content and
 maximum temperature will affect the dosage.
 A.8.3   Reverse Osmosis System
       The Barrick system includes one  Culligan KP-90 Reverse Osmosis System. The KP-90 RO system is
capable of producing 41 gpm of RO permeate when the feedwater temperature is between 60-80° F. The RO
system operates at 55 percent recovery and a flux recovery of approximately 14 gallons per square  foot  of

                                             •A- 17

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  membrane area per day (gfd).  This lower recovery is due to high silica content combined with the presence




  of heavy metals in the RO feedwater (75 gpm feed, 41 gpm finished, 34 gpm wastewater).




         The KP-90 RO system consists of four 3-element long FRP housings arranged in a 2:1:1 array.  The




  RO system has 21 TKO 5-micron cartridge filters.  The cleaning connections are designed for a flow rate of



  70 gpm in the first stage and 35 gpm in the second and third stages.   .




         A prefilter removes smaller particles that the Multi-Tech filter could not eliminate. The filter housing




 contains seven 30-inch long 5^micron elements. Two 0-160 psi range pressure gauges are located before and




 after the housing to measure the pressure drop through the filters. A feedwater conductivity element measures




 the amount of dissolved solids in the feedwater stream and sends  a signal to. the conductivity controller on th




 KP-90 control panel. This measurement is compared with the product water conductivity to determine unit




 efficiency. A low pressure switch is provided to shut the system off at 10 psi to prevent damage to the hi. h




 pressure pump due to low inlet pressure.  A high pressure pump brings the filtered and chemically treated




 water to the appropriate operating pressure to  the RO modules.  Pressure gauges before and after the pump




 indicate the pump discharge pressure and the module feed pressure respectively.  The module feed pressure



 is controlled by a glove valve  located after the  high pressure pump discharge.




        The KP-90 RO housings each contain  three 8-inch thin  film composite spiral wound RO elements.




 The pressurized feedwater enters the  membrane vessel and  flows through the channels  between the spiral




 windings of the first spiral wound cartridge.  Some of the feedwater permeates through the membrane and




 travels ,a spiral path to the product water collection tube at the center of the cartridge. The remaining feed




 continues through  the spiral layers, the length of the cartridge.  It then encounters the next cartridge in the




 vessel and the process is repeated. The product from each cartridge exits from the common product tube in




 the membrane vessel. The feedwater becomes  more concentrated as it  passes through each membrane and




 exits from the membrane pressure vessel as concentrate.  The housings are oriented in a waste to feed cascade




 fashion. The concentrate from the first-two housings becomes the  feedwater for the tiext pressure vessel. And




 finally, the concentrate from the third housing feeds the last pressure vessel.  All four pressure vessels share



a common header to collect the product water.
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   A.8.4   Post-treatment System                        •                    •      ,




   Decarbonator




          A decarbonator with blower and starter panel is included to remove carbon dioxide (COj) in the




   permeate water. The RO permeate contains approximately 42 ppm of carbon dioxide, which was formed by




   addition of the HCL. Ninety-five percent of the carbon dioxide is removed by the decarbonator.




          Product water from the decarbonator flows to a 500-gallon sump to be blended with 15 gpm of bypass



   water from the pretreatment system to maintain acceptable water quality.



   Post-treatment Feeders




          Chlorine and polyphosphate are added to the product water following blending with the bypass water



   to provide disinfection and corrosion control.




          Treated water flows to a 45,000-gallon storage tank and the distribution system.



  A.9     TAYCHEEDAH CORRECTIONAL FACILITY




  A.9.1    Installed Water Svstem




          The Taycheedah water system is a community water system serving the potable water needs of 375



  inmates and staff of the correctional facility located near Fon du Lac, Wisconsin.  A System Mario  ion"




  exchange water treatment system was installed to reduce the levels of radium. The water supply is obtained



  from two groundwater wells.




         The water system  was designedly a consulting engineer with  input from the owner and the state




  drinking.water  personnel.   Plan, specifications and bid  documents were prepared for the purchase  and




.- installation of the treatment equipment.  A mechanical contractor purchased and installed the equipment in




  an existing building.  The plant is operated and maintained  by the correctional facility maintenance personnel.




  The mechanical contractor  provides assistance as needed, with support from the equipment supplier.




         Additional information on the water system was not available from Taycheedah Correctional  Facility



  personnel due to restrictions on the use of facility data.
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