-------
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
ft.
WATER SYSTEM
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ANCILLARY
FEATURES
TREATMENT
TECHNOLOGY
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Owners, Enginee
Manufacturer, Sta
Raw-water intake,
pumping station,
clearwclls.transmissions
ind distribution systems
Pressure clarifier, depth
filler and GAC filler,
disinfeclion
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(ireen Cove
Condominiums
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Owners, Enginee
.Manufacturer
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disinfeclion
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Ronald, WA
(old coal mine she
(groundwaler)
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Manufaclurer and
Inslallalion
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Owner, Manufact.u
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Packaged reverse osmosis
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(350 students & si
Non-Ira nsieni
Non -community
Howe, IN
(groundwaler)
Lima Brighton
Memenliiry School
3wner evaluated &
installed
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Raw water intake
modifications,
chlorinalion
modifications, piping
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Crawford, CO
(Crystal Creek)
(surface water)
nil Hand Domestic
Water Co.
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Owner, Manufaciui
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disinfeclion
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Transient non-
communiiy water sys
= 0
Ml. Hood Nation
Forest, 1 iood River,
(Ijjsi bike)
(surface water)
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Owner, Engineer,
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roundwaler well, pump
station, chlorination
Tdifications, filler house
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~ 600 (2,000 peop
Designed for 800
Appleton, Wl
(groundwaler)
Darboy Sanitary
District
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Owner, Engineer,
Contractor
Raw water intake,
transmission main,
orage tank, filler bldg.,
cess road, bridge, sewer
line extension
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Pressure clarifier, depth
filler disinfeclion
144
(400 people)
Readsboro, VT
(surface water)
teadsboro Water
realmeni Facility
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ns, Negotiation with
llanufacturer and
Inslallalinn
Owner, Engineer,
Manufaclurer
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Pressure clarifier, depth
filter and reverse
osmosis, disinfeclion
(1, KM) employees
Non-transient
Non -community
EIko, NV
(groundwaler)
urrick (ioidstrlke
Mines, Inc.
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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
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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
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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
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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
-------
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
-------
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.
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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
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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
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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
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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.
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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.
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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
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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
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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
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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
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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.
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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
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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
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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
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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.
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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.
A-6
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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.
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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
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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. .
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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
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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. .
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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.
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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
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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
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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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