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DESIGN REPORT FOR
City of Prior Lake, MN
November 2006
Presented by:
DESIGNING FOR A BETTER TOMORROW
DESIGN REPORT
WATER TREATMENT AND STORAGE
FACILITY
CITY OF PRIOR LAKE, MINNESOTA
NOVEMBER 2006
BMI Project No. M21.38412
I hereby certify that this plan, specification or report was prepared by me or under my direct supervision, and that I
am a duly Licensed Pr fi . al ngineer under the laws of the State of Minnesota.
Typed or Printed Name: Seth A. Peterson
Date 'L.. q. JJoV. l.0v~
Reg. No. 26468
BOLTON & MENK, INe.
CONSULTING ENGINEERS AND LAND SURVEYORS
TABLE OF CONTENTS
SECTION I .......................... ......................................................................................................................1-1
INTRODUCTION................................. ........... ...... ................................................................................... .1-1
A. GENERAL ....................................................................................................................................l-l
B. REPORT ORGANIZATION ........................................................................................................1-1
C. PROJECT BACKGROUND .........................................................................................................l-l
D. AUTHORIZATION.... .......... ... ........ ... ... ........ ................ ...... ........ ... ... ..... .... ... ... ................... ........ .1-2
SECTION 2 .................................................................................................................................. ............. .2-1
WATER SUPPLY CHARACTERISTICS ................................................................................................2-1
A. GENERAL. ......... .... ..... ..... .... ..... ... ...... ............ ............. ............... ... ..... ... ............ ... ......... ....... .... ... .2-1
B. WATER SUPPLY CHARACTERISTICS ...................................................................................2-1
C. QUALITY. ... ...... ...... .......... ...... .......... .... ...... .......... .... .... ...... ........ ... ... ... .... ....... .... ...... ......... ...... ....2-2
D. PILOT PLANT TESTING........... ............... ............................ .............. ........... ....................... ..... .2-4
SECTION 3 ..................................................................................................................................... ...........3-1
FACILITIES SITING AND ARCHITECTURAL FEATURES ...............................................................3-1
A. GENERAL ............... ... ....... ...... ....... .................. ......... .... ............ ..... ...... ........... .... .... .... .......... .......3-1
B. PLANT SITE .............. ....... ...................... ............... ... ...... ....... ........ ......... .... ...... ..... .... ..... ..... ....... .3-1
e. STORMW ATER CONSIDERATIONS .......................................................................................3-1
D. PLANT FACILITIES.................................................................................................................... 3-2
E. ARCHTECTURAL FEATURES.. .................. ................... ...... .......... ............... ......... ..... .... .... .... ..3-3
F. LANDSCAPE ARCHITECTURE FEATURES ...... ................ ....... ......... ........ ............ ........... ......3-3
G. ENERGY CONSIDERATIONS ......... ........... ........ .... .... ... .............. ...... ....... .... ... ......... .... ............ .3-4
SECTION 4 ........................................................................................................................................ ....... .4-1
TREATMENT PROCESS AND DESIGN CRITERIA - 6.5 MGD FACILITY ......................................4-1
A. GENERAL................................................................................................................................. .. .4-1
B. PLANT PROCESS....................................................................................................................... .4-1
C. TREATMENT PROCESS........................................................................................................... .4-5
1. Aeration.............................................................................................................................. ... .4-5
2. Detention............................................................................................................................. .. .4-6
3. Filtration............................................................................................................................ .... .4-6
4. High Service Pumping with Clearwell/Reservoir .............................. .....................................4-7
5. Backwash Water Reclamation Facilities. ............ ......... ............ ................. .............. ..... ..........4-7
D. TREATMENT PLANT HYDRAULIC PROFILE .......................................................................4-7
E. CHEMICAL FEED SYSTEM ..................... .................. ............ ......... ......... ......... .......... .... .... .... ..4-8
1. GeneraL......................................................................................................................... ......... .4-8
2. Chlorine ....... ...... .......... ............... ... ............ ....... ................ ........ .................. ........... ....... ...... ..4-1 0
3. Potassium Permanganate ...... ...... ............................... .............. .................................. ..... ..... .4-11
4. Fluoride.... .... ...... ... ....... .... ....... ........................... ..... ... ... ... ... ...... ... ... ....... ....... ............. .... .... ...4-11
5. Polyphosphate...................................................................................................................... .4-12
6. Polymer........................................................................................................................... ..... .4-12
F. SUPPORT SERVICE FACILITIES ...........................................................................................4-12
1. Water Metering Testing Area, HV AC, Lighting, Air, Wastewater Service, Dehumidification
System.................................................................................. .............. ................................. .4-12
2. Overflow Structure....... .................................. .................... ................ ................................. .4-13
3. Electrical Service................................................................................................................. .4-13
4. Security.................................................. ..... ....................................... .................................. .4-13
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page i
Prepared by Bolton & Menk, Inc.
G. CONTROL SySTEM.................. .............................................................................................. .4-13
I. Control..... .... ........... ..... ... ....... ................. ................. ..... ... ...... ...... .................. ....... ............. ...4-13
2. Monitoring................. ........................................................................................................ ...4-14
SECTION 5 .................................................. ........................... ............................................................... ....5-1
TREATMENT PROCESS AND DESIGN CRITERIA.............................................................................5-1
FOR EXPANDED FACILITY -7.5 MGD ...............................................................................................5-1
A. GENERAL.................................................................................. ....... .......................... ............. ....5-1
B. PLANT PROCESS ...... ..... .................... ..... ......... ..... .......... ... .... ... ......... ..... ... ..... ... ....... .... .... ..... .....5-1
C. TREATMENT PROCESS.............. ........... ............. ............ ........................... ....................... ...... ..5-5
D. TREATMENT PLANT HYDRAULIC PROFILE .......................................................................5-6
E. CHEMICAL FEED SySTEM.............. ..................... ............................................... ............. .......5-6
F. SUPPORT SERVICE F ACILITES.... ....... ....... ........ ............ ..... ...... ............. .... ................... ..... .....5-8
G. CONTROL SYSTEM ............................... ............ ............... ................... ........ ...................... ...... ..5-8
SECTION 6........................ ............ ................... ...................................... ............. ...... .......... ...... .......... ......6-1
ESTIMATED CONSTRUCTION COSTS, FUNDING AND PROJECT SCHEDULE...........................6-1
A. ESTIMATED CONSTRUCTION COSTS AND PROJECT FUNDING.....................................6-1
B. ASSOCIATED IMPROVEMENTS ....... ......... ........... ......... ........... .......... ..... ............................ ...6-2
C. PROJECT SCHEDULE .... .... ....... ...... ....... .... ..... ..... ..... ............... ...... ... ....... ... ........... .... .......... ..... .6-3
Table
2-1
2-2
2-3
2-4
4-1
4-2
4-3
4-4
5-1
5-2
6-1
6-2
6-3
Figure
3-1
4-1
4-2
4-3
5-1
5-2
LIST OF TABLES
Page
Well Construction Summary .... ................. ................. ............................. ......... .....2-1
Water Pumped Summary ........ .......... ......... ..... ............ ....... ......... ...... ...... ........ .......2-2
Summary of Raw Water Quality Parameters.........................................................2-3
Pilot Plant Test Results .................. ........... ........................ ........ ..................... ........2-4
Design Criteria - 6.5 MGD ....................................................................................4-2
Chemical Feed Design Criteria. ...... ..... ...... .............. ................................ ........... ...4-9
Supervisory Control Instrumentation Functions...................................................4-16
Supervisory Control Alarm Points.......... ............ ............... ............ .................... ...4-16
Design Criteria -7.5 MGD ....................................................................................5-2
Chemical Feed Design Criteria...... .............. ................. ...... ...... ..................... ........5-7
Construction Cost EstimatelProject Funding.... ............ ...................... ................... 6-1
Associated Improvements...................................................................................... 6-2
Proposed Schedule................................................................................................. 6- 3
LIST OF FIGURES
Follows Page
Facilities Location Plan - 6.5 MGD ............................................................3-2
Flow Diagram ........... ...... ....... ........ ................... ... ................................. ....... 4-1
Floor Plan -6.5 MGD ..................................................................................4-5
Hydraulic Profile..... ....... ......... ............ ......... ............ ......... ............ .............. 4-7
Facilities Location Plan - 7.5 MGD ............................................................5-1
Floor Plan - 7.5 MGD .................................................................................5-5
Page ii
Prepared by Bolton & Menk, Inc.
City of Prior Lake, Minnesota
Design Report - M21.38412
LIST OF APPENDICES
Appendix
A Water Pilot Plant Report
B Proposed Elevations and Computer Generated Graphics
C Preliminary Landscaping Plan
D Tree Survey Results
E Equipment Data Sheets
City of Prior Lake, Minnesota
Design Report - M21.38412
Page iii
Prepared by Bolton & Menk, Inc.
SECTION 1
INTRODUCTION
A. GENERAL
This "Design Report" summarizes the results of the preliminary design engineering for the Water
Treatment Facility Improvements. The report presents the recommended design criteria, unit
processes, equipment selection, and facilities layout for the proposed water treatment facilities.
The purpose of this report is to provide the necessary information for review of major design
concepts by the City of Prior Lake and its staff prior to preparation of final plans and
specifications for construction of the project.
B. REPORT ORGANIZATION
The text of the "Design Report" is divided into six sections that describe the findings of the
preliminary design engineering. This section presents general information and the project
background. Section 2 outlines the water supply characteristics and treatment requirements.
Section 3 presents the facilities site plan and architectural features, including energy
considerations. Section 4 describes the recommended system for each unit process and includes
detailed design criteria, preliminary layouts, and equipment selections for a facility with a
capacity of 6.5 mgd. Section 5 describes the recommended system for a facility with capacity of
7.5 mgd. Section 6 summarizes the estimated construction costs, funding sources, and project
schedule.
Five appendices are included with the "Design Report" to provide supplemental information.
Appendix A presents the pilot testing results for the treatment facility site and Appendix B
contains the proposed elevations and computer generated graphics. Appendix C and D contain
the preliminary landscaping plan and the tree survey results respectively. The equipment data
sheets for selected equipment are presented in Appendix E.
C. PROJECT BACKGROUND
The City of Prior Lake draws the majority of their drinking water from the Jordan Aquifer. In
Prior Lake this aquifer is high in both iron and manganese. The water is safe to drink, however,
the levels of iron and manganese present in the water exceed secondary drinking water standards
established by the Environmental Protection Agency (EP A). As a result numerous residents
experience water staining, odor and even taste issues at their residences. In addition, these
minerals cause build-up in the water system piping and can substantially reduce the capacity of
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page I-I
Prepared by Bolton & Menk, Inc.
watermains and water services. In addition, the natural environment in Prior Lake causes
problems with the water system as the lake acts as a barrier resulting in numerous deadend
watermains causing a lack of water circulating through the piping systems and thereby increasing
the potential for water staining, odor and taste issues. City staff flushes the watermains on an
aggressive schedule to keep them as clean as possible.
In June 2006, the City's Water Treatment Plant Committee (WTPC) solicited Requests for
Qualifications from interested consultants for the design and construction management of a water
treatment and storage facilities. The WTPC reviewed the qualifications and short-listed four
consulting firms to receive formal proposals for the water treatment and storage facilities.
In August 2006, the City of Prior Lake authorized a standard professional services agreement
with Bolton & Menk, Inc. for design and construction services associated with the design and
construction management services for a 6.5 mgd water treatment facility with a 1.5 million gallon
reservoir.
The purpose of this "Design Report" is to provide the City with the necessary information
regarding the City's water treatment facilities so the City can move directly into the design phase
for the treatment and storage facilities.
D. AUTHORIZATION
This "Design Report" has been completed in accordance with the terms of the Professional
Services Agreement between the City of Prior Lake and Bolton & Menk, Inc. Consulting
Engineers for design services of the new water treatment and storage facilities.
Page 1-2
Prepared by Bolton & Menk, Inc.
City of Prior Lake, Minnesota
Design Report - M21.38412
SECTION 2
WATER SUPPLY CHARACTERISTICS
A. GENERAL
The quantity and quality of raw water and the treatment requirements have been discussed in
detail in the City of Prior Lake Comprehensive Water Works Plan prepared by Engineering
Resources, Inc. in December 2004. A brief summary of this information along with other
updated water quality and raw water data will be presented in this section.
B. WATER SUPPLY CHARACTERISTICS
The City of Prior Lake's water supply currently consists of five wells. Two additional wells,
wells Nos. 8 and 9 are scheduled to be complete in 2007. A summary of the existing well data
and pumping capacities is presented in Table 2-1.
Table 2-1
Well Construction Summary
City of Prior Lake, Minnesota
Well No. 3 4 5 6 7 8 9 10
Operational Yes Yes Yes Yes Yes No No No
Year Installed 1973 1975 1988 2001 2003 2006 2007 2007
Inner Casing Dia. 16 16 24 & 18 30 & 24 12 24 NA NA
(in.)
Total Depth (ft) 364 345 372 410 640 402 NA NA
Capacity (gpm) 1,200 1,100 1,000 1,100 450 1,200 450 1,100
Pumping Rate 1,050 950 750 NA 450 1,200 450* 1,100*
(gpm) **
* Anticipated Pumping Rates
** Rate reflects influence of other wells running at the same time
As shown in Table 2-1, there is a drop off in well pumping rates when multiple wells are running.
This is especially true when wells 3, 4 and 5 are running simultaneously. Once well 10 is on-line,
it is anticipated that well 5 will be used as an emergency or standby well. By operating the wells
in this manner, it should allow for greater production from wells 3 and 4. Well 6 will not be
piped to the water treatment facility; therefore, it is not accounted for in determining the
maximum flow rate to the water treatment facility.
An indication of future water use can be determined by examining past water use records. A
summary of the water pumped from the wells to the distribution system is presented in Table 2-2.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 2-1
Prepared by Bolton & Menk, Inc.
Table 2-2
Water Pumped Summary
City of Prior Lake, Minnesota
Total Water Average Day Maximum Day A vg. Day to
Pumped Pumped Water Pumped Max. Day Total Per Capita
Year Population (MG) (MGD) (MGD) Ratio Pumped (gpcd)
2000 15,917 614.6 1.68 4.34 2.58 106
2001 16,457 626.4 1.72 4.47 2.60 104
2002 17,310 597.6 1.64 3.75 2.29 95
2003 19,662 775.1 2.12 5.99 2.82 108
2004 21,156 722.9 1.98 4.79 2.42 94
2005 21,395 704.8 1.93 5.66 2.93 90
2006 * 21,800 684.3 2.51 5.98 2.39 86
* Data through September
From table 2-2, the average ratio of average day demand versus maximum day demand is 2.58.
Water demand will continue to increase with increases in population similar to what is shown in
Table 2.2.
Wells 3,4 and 7 are located at the water treatment facility site and wellS has a raw water
transmission line piped to the northeast comer of the site. In the future, wells 8 and 9 will have
raw water transmission lines run to the site. It is anticipated that the City will drill well 10 near
Fire Station No.1 and this well will utilize the raw water transmission main from wells 8 and 9.
It is anticipated that no additional future well raw water transmission lines will be run to this site,
other than those described, due to various requirements from the Minnesota DNR and well siting
restrictions due to the local topography and groundwater characteristics. Based on this, the well
capacity to the site is expected to be 6.5 million gallons per day (mgd) and up to 7.5 mgd if well
10 is piped to the site. From review of table 2-2, the City had a maximum day demand of nearly
6 million gallons in 2006. Based on this, the proposed facility will not have adequate capacity to
treat future peak demands. In order to provide the necessary treatment capacity as the City
experiences growth, additional water treatment facilities will be required at other locations within
the City.
c. QUALITY
A summary ofthe water quality data from the existing wells is presented in Table 2-3. The water
quality from new wells in the same aquifer should produce similar water quality characteristics.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 2-2
Prepared by Bolton & Menk, Inc.
Table 2-3
Well Water Quality
Prior Lake, Minnesota
Well No.
Parameters Units MCL/S 3 4 5 6 7 8
MCL
PH 6.5 to 8.5 7.5 7.4 7.4 7.7 7.4 7.7
Total Alkalinity mg/L N/A 361 349 318 254 365 359
CaC03
Total Organic mg/L N/A 0.9 0.9 0.8 1.9 1.1 <2.0
Carbon
Hardness, Total as mg/L N/A 344 333 317 237 340 306
CaC03
Fluoride ml!lL 4 0.2 0.18 0.17 0.16 0.20 0.21
Sulfate mg/L 250 15.7 15 13.9 8.6 17.8 15.8
Chloride mg/L 250 <3 7.2 6.7 <3 <3 2.5
Nitrate + Nitrite mg/L as N N/A <0.2 <0.2 <0.2 <0.2 <0.2 ND
Nitrogen, mg/L N/A 0.2 0.06 0.07 0.21 0.24 ND
Ammonia
Sulfide, Total mg/L N/A <I <I <I <I <I <I
Total Dissolved mg/L 500 . 336 331 318 245 336 348
Solids
Calcium ml!lL N/A 82.6 80.5 77.5 57.7 82.1 74.5
Magnesium mg/L N/A 33.4 32 29.9 22.5 32.9 29.1
Sodium mgJL N/A 4.2 5.87 3.76 3.34 6.16 6.13
Barium mgJL 2 0.05 0.051 0.071 0.358 0.062 0.015
Chromium mgJ L 0.1 <0.006 <0.006 <0.006 <0.006 <0.006 0.0048
Copper ml!lL N/A <0.005 <0.005 1.06 <0.005 <0.005 <0.005
Iron ml!lL 0.3 0.019 0.04 0.074 1.170 0.616 NA
Manganese mg/L 0.05 0.28 0.319 0.343 0.337 0.199 0.278
Silicon as Silica mg/L N/A 16.8 16.2 17.8 23.8 12.7 NA
Arsenic mg/L 0 <0.5 <0.5 <0.5 3.05 <0.5 0.27
(MCLG)
Gross Alpha pCi/L 15 4.6 4.4 3.5 3.1 3.1 6.32
Radium 226 pCi/L N/A 1.9 0.89 0.7 1.2 1.2 1.15
Radium 228 pCi/L N/A 0.84 1.2 1.8 1.70 0.76 1.60
Combined Radium pCi/L 5 2.74 2.09 2.54 2.9 1.96 2.75
From the above table, water quality issues for the City of Prior Lake can be summarized as
follows:
1. All of the wells exceed the secondary standard level for manganese.
2. Wells 6 and 7 exceed the secondary standard for iron.
3. The water quality for all wells do not exceed the arsenic or radium primary drinking water
standards
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 2-3
Prepared by Bolton & Menk, Inc.
4. Future wells may require treatment to lower the iron and manganese levels.
5. The new treatment facility will be designed to meet secondary drinking water standards for
both iron and manganese.
D. PILOT PLANT TESTING
Pilot plant testing is an effective tool in the water treatment design process as it supports the
maximum degree of treatment, minimizes the use of costly chemicals in the filtering process and
minimizes problems during start-up of the water treatment facility. The Bolton & Menk, Inc.
pilot plant was delivered to the site on October 9, 2006 and pilot plant testing was completed on
well 4 from October lOth through October 13th. Well 4 was used for pilot testing due to the higher
concentrations of manganese in the raw water and manganese is typically the more difficult
parameter to remove. Two different media combinations were used in testing. One was a
combination of IS-inches of anthracite and IS-inches of greensand and the other was IS-inches of
anthracite and IS-inches of silica sand. The pilot plant was setup to run the influent water
through aeration, detention chamber, chemical addition of potassium permanganate after the
detention tank and then filtration. Both media combinations achieved similar success in removal
of the iron and manganese achieving results well below the secondary treatment standards as
shown in Table 2-4.
Table 2-4
Pilot Plant Test Results
Parameter Greensand! Anthracite Silica Sand! Anthracite
Iron (mg/l) 0.037 0.020
Manganese (mg/l) 0.018 0.015
* Secondary Standards - Iron - 0.3 mg/l; Manganese - 0.05 mg/l
The pilot plant testing results indicate that substantial removal of iron and manganese can be
achieved using chemical addition of potassium permanganate and a media combination of
anthracite and silica sand. Based on the pilot plant test results, it is proposed to use dual media
filters with IS-inches of silica sand and IS-inches of anthracite. A copy of the full water pilot
plant report is provided in Appendix A.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 2-4
Prepared by Bolton & Menk, Inc.
SECTION 3
FACILITIES SITING AND ARCHITECTURAL FEATURES
A. GENERAL
An important consideration in water treatment facility design is to develop a site plan and
architectural features that are functional, provide low level of maintenance, and are aesthetically
pleasing. In recent years, the incorporation of energy conservation elements also has taken on
added importance. This section presents the site plan, stormwater issues, architectural features
and energy considerations with specific discussion in regards to these three areas.
B. PLANT SITE
The proposed site for the new water treatment facility is in the Brooksville Hills neighborhood
and is a City owned, 7.5-acre parcel. The City has identified this site for the location of the
treatment facility for many years and the City currently has three wells on the site (wells 3, 4 and
7) and one well (well 5) piped to the site.
Geotechnical investigations will be performed at the site and will indicate whether existing soils
are adequate for the construction of the water treatment and storage facilities and will locate
ground water levels, which are critical for the structural design of the facility. From inspection of
previous soil reports from the area, it is anticipated that the soils present will be adequate for the
construction of the treatment and storage facilities. If water is detected during the geotechnical
investigation, dewatering during the construction may be required.
C. STORMWATER CONSIDERATIONS
The proposed water treatment facility site has an area of approximately 7.5 acres. The southerly
and easterly areas of the site are heavily wooded with the remainder of the site having a fair
amount of grass cover. The site collects storm water runoff from its neighboring properties to the
north and west and also serves as a discharge point for three surrounding storm sewer systems:
two storm water outlets exist in the southwest comer of the site and one in the northeast comer.
The site is relatively flat within its northwest comer, facilitating storm water infiltration in this
area, but increases to grades of one to five percent as it ultimately drains east to a series of ponds
in Cardinal Ridge Park.
Page 3-1
Prepared by Bolton & Menk, Inc.
City of Prior Lake, Minnesota
Design Report - M21.38412
According to the City's current wellhead protection plan, the treatment facility site and Cardinal
Ridge Park to the east are within a high Drinking Water Supply Management Area (DWSMA)
vulnerability zone. This raises some concerns with the City, as untreated storm water runoff that
is allowed to infiltrate within this area could potentially impact the groundwater quality, and
ultimately the drinking water quality in the area.
The construction of the treatment facility will increase the amount of impervious surface on the
site and, accordingly, the amount of runoff from the site. This development, alone, will
prompt storm water management requirements relative to runoff rates, runoff quality, and/or
infiltration requirements. These requirements may include ponding, storm water treatment
structures, or shallow rain garden! infiltration facilities, all of which could be incorporated into
the project's site development and landscaping plans.
In addition to the storm water management requirements generated by the site's development, the
City is also researching the potential of the site to serve the broader storm water management
needs of the surrounding area. The site, as previously mentioned, accepts runoff from the
surrounding area, amounting to nearly one hundred acres. Currently this runoff is not
significantly treated until it passes through the site and into the ponds at Cardinal Ridge Park. As
the City works towards updating its current wellhead protection plan and continues to evaluate
the storm water treatment needs of the surrounding areas, it appears that the treatment facility site
could serve as an integral part of an overall storm water management plan for the surrounding
area. The City's analysis will continue into the final design phase ofthe water treatment facility,
during which time additional storm water management techniques on the site will be considered.
D. PLANT FACILITIES
The proposed site layout is shown in Figure 3-1 and the facility consists of the following major
structures: 1) water treatment plant; 2) underground reservoir; 3) garage facilities and 4)
backwash water reclaim facilities. Other elements of the site will include raw water piping,
overflow structures, standby generator, driveway and parking area, and site piping.
The facility has been located to the southeastern portion of the site, which allows the greatest
distance from Brooksville Hills neighborhood residents located to the North and West.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 3-2
Prepared by Bolton & Menk, Inc.
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FACILITIES LOCATION PlAN
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3-1
E. ARCHTECTURALFEATURES
The basic construction materials that will be used for the water treatment facility will be poured-
in-place concrete, masonry block and precast concrete plank. The new water treatment facility's
exterior construction will be designed architecturally to be aesthetically pleasing, to conserve
energy, to be low in maintenance, and to be cost effective, and yet meet the requirements of the
neighborhood.
Since the treatment facility will be located in the Brooksville Hills neighborhood, several
neighborhood meetings were held with residents to determine a consensus for the exterior of the
building and a lot of time and effort was spent on preparation for these meetings. During these
meetings, architectural concepts were shared and discussed with the residents and two
architectural options were presented, a civic and a residential type fayade and are shown in
Appendix B. From the information obtained at the neighborhood meetings, a residential type
fayade was pursued and is presented in this report in Appendix B. Even though a residential
fayade was chosen, the exterior of the building has brick and rock face type block. These are cost
effective building materials and are low maintenance. Building elevations of the proposed design
are included in Appendix B along with computer-generated renderings of the proposed building
using photographs of the site. The computer generated renderings and the proposed building
elevations were shown to the residents to build consensus for the type of building architecture.
The last neighborhood meeting with the residents was held on-site and the final proposed
elevations and computer-generated renderings were shared with the residents and the proposed
location ofthe building was staked to give the residents a feel for the location and magnitude of
the treatment facility.
F. LANDSCAPE ARCHITECTURE FEATURES
A preliminary landscape architecture plan was prepared and shared with the residents at the
second neighborhood meeting. The preliminary landscape plan provides a filter with strategic
views of the NW neighborhood side. On the service side (SE elevation) the landscaping provides
softening with screening at the driveway entrance. The WTFC plans to host a landscaping
meeting with residents sometime during the final design to solicit more input as the design nears
completion. This will also allow us to properly show the proposed storm water improvements. A
preliminary concept of the landscaping plan is presented in Appendix C and we anticipate
meeting with the neighborhood residents during final design to formalize a landscaping plan.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 3-3
Prepared by Bolton & Menk, Inc.
Due to the location of the facility, many trees on the site will be removed during construction of
the facility. Therefore, a tree survey conducted by the Kunde Co., Inc. was completed for the site
and 262 trees were listed with only five (5) of the 262 considered "significant". Replacement of
trees will be according to the City's tree ordinance. The tree survey information is included in
Appendix D.
G. ENERGY CONSIDERATIONS
The new water treatment facility will incorporate energy saving features and equipment. These
energy saving items include the following:
energy efficient motors on equipment
· exterior doors of insulated construction
· night set back and set up thermostat control strategies
· translucent window panels for passive lighting
· efficient heating distribution system using individual fan coil units or unit heaters that would
allow zoning of the building spaces
variable frequency drive motors for the high service and backwash pumps
· energy saving lamps and ballasts for lighting.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 3-4
Prepared by Bolton & Menk, Inc.
SECTION 4
TREATMENT PROCESS AND DESIGN CRITERIA - 6.5 MGD FACILITY
A. GENERAL
This section describes the treatment process and design criteria for the water treatment facility
improvements for the removal of iron and manganese from the raw water supply. The City does
have hard water and it is possible to soften the water supply, however, a softening treatment
facility is considerably more expensive and requires additional operation and maintenance due to
the treatment process. Therefore, due to the high capital and operation and maintenance costs
associated with a softening process and since a majority of residents currently have home water
softening systems, it was determined that softening is not a cost effective option for treatment.
The treatment process and design criteria are based on a new iron and manganese water treatment
facility with a capacity of 6.5 million gallons per day (mgd) or 5,420 gallons per minute (gpm).
The gpm rate is based on a 20-hour day, allowing 4-hours of rest for the production wells. It is
not good practice to operate wells for 24-hours continuous, however, this is often not feasible for
growing communities such as Prior Lake. Therefore, the benefit of designing the treatment
facility around a 20-hour day is it provides additional operational flexibility. It allows for routine
maintenance of the facility even during peak demand periods and allows for expanded capacity
without making any changes to the facility. The facility will also allow for adaptation to meet
potential future limits. Some additional space is provided for additional chemical feed points and
other equipment to meet potential future limits or to adjust to potential changes in water quality.
The design philosophy for the water treatment improvements is to provide a high quality finished
water, a plant that is easy to operate, and has low maintenance costs.
B. PLANT PROCESS
The main water treatment process consists of aeration, detention, and filtration. The following
sections describe the treatment units and criteria. Figure 4-1 shows the new plant process flow
diagram. Table 4-1 presents the design criteria for the water treatment improvements.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-1
Prepared by Bolton & Menk, Inc.
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PRIOR lAKE. MINNESOTA
WATER TREATI.IENT FACILITY
FLOW DIAGRAM
4-1
fiGURE
Table 4-1
Design Criteria - 6.5 MGD (5,420 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Aeration
Quantity number 2
Construction type Aluminum housing with induced draft PVC
Capacity gpm 3,600 gpm
Size feet 12'x 12'x 10'
Blower capacity 10,800 cfm
Blower HP hp 2 x 1.5 HP
Detention Tank
Quantity number 1
Construction type concrete
Detention Time @ 5,420 gpm minutes 31.3
Volume gallons 169,600
Basin Depth (Normal) feet 20
Basin Width feet 9
Basin Length (Effective) feet 126
Filters
Quantity number 6
Construction type concrete
Control Method Influent Flow Splitting
Filter Area Per Cell sq. ft. 360
Total Filter Area sq. ft. 2160
Filtration Rate gpm/sq. ft. 2.5
Media type Dual media (anthracite and Silica sand)
Anthracite Depth inches 15
Effective Size mm 0.8 - 1.0
Silica Sand Depth inches 15
Effective Size mm 0.45 - 0.55
Underdrain System type Leopold Universal
Media Retainer type 14" Reverse Graded Gravel
Method of Backwashing type Air and Water
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-2
Prepared by Bolton & Menk, Inc.
Table 4-1
Design Criteria - 6.5 MGD (5,420 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Rate of
Air Scour scfm/SF 3
Water Backwashing gpm/SF 15
Hi2h Service Pumps
Quantity number 3
Capacity gpm 2,750 @ 165' TDH
Pump type Vertical Turbine
Pump Speed rpm 1,750
Drive type VFD
Motor hp 150
ClearwelllBackwash Supply
Quantity number 1
Cells number 2
Construction type Concrete
Volume (total) gallons 249,400
Basin Depth feet 15
Basin Width feet 39
Basin Length feet 57
Reservoir
Quantity number 1
Cells number 1
Construction type Concrete
Volume gallons 1,260,250
Basin Depth feet 15
Basin Width feet 115
Basin Length feet 117
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-3
Prepared by Bolton & Menk, Inc.
Table 4-1
Design Criteria - 6.5 MGD (5,420 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Backwash Reclaim System
Quantity number 3
Construction type Concrete
Effective Capacity per Basin gallons 76,795
Basin Depth (water depth) feet 16
Basin Length feet 55
Basin Width feet 35
Reclamation Pump
Quantity number 3
Capacity gpm 250 @ 32' TDH
Pump type Submersible
Speed rpm 1,750
Motor hp 5
Slud2e Disposal Pump
Quantity number 3
Capacity gpm 100
Pump type Submersible
Speed rpm 1,750
Motor hp 5
Backwash Pump
Quantity number 1
Capacity gpm 5,400 @ 50' TDH
Pump type Vertical Turbine
Pump Speed rpm 1,180
Drive type VFD
Motor hp 125
Backwash Aeration System
Quantity of Blowers number 1
Blower type Positive Displacement
Blower Capacity cfm 1,080
Motor hp 60
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-4
Prepared by Bolton & Menk, Inc.
Table 4-1
Design Criteria - 6.5 MGD (5,420 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Chemical Feed
Chlorine
Feed System type Liquid
Control Method type Flow Proportioned Chemical Feed Pumps
Storage Tank gallons 2 @ 1,700/1 @ 165
Potassium Permanganate
Feed System type 2% Dilute Mix Solution
Control Method type Flow Proportioned Chemical Feed Pumps
Storage/Mix Tank gallons 2 @ 750
Fluoridation
Feed System type Hydrofluosilicic Acid
Control Method type Flow Proportioned Chemical Feed Pumps
Storage/Mix Tank gallons 1 @ 750/1 @ 165
Polymer
Feed System type Polyblend Type Mix Feed
Control Method type Flow Proportioned Chemical Feed Pumps
Corrosion Inhibitor
Feed System Type Polyphosphate liquid
Control Method Type Flow Proportioned Chemical Feed Pumps
Storage Tank gallons 1 @ 165
c. TREATMENT PROCESS
The preliminary floor plan for the treatment facility structure is shown in Figure 4-2 and the
various treatment processes are described in further detail below.
1. Aeration
The induced draft aerator will be installed ahead of the detention tank. Providing
oxidation of the iron in the raw water with air is economical, reduces chemical
requirements, and forms a more filterable precipitate. The aerators will be manufactured
of aluminum shell with PVC internal components. Water cascades downward through
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-5
Prepared by Bolton & Menk, Inc.
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PRIOR lAKE. MINNESOTA
WATER TREATMENT FACILIlY
FLOOR PLAN
6.5 MGD
FIGURE
4-2
the aerator releasing gases in the water, and oxygen is provided from the upward flowing
air that is drawn through the aerator by fans located on the top of the structures. Aeration
helps to reduce the concentration of many dissolved gases such as carbon dioxide,
hydrogen sulfide and radon, which are normally found in well water supplies. Bypass
piping for each aerator will be provided to allow routine maintenance without disrupting
the plant operations. Manufacturer's literature on the type of aerator that will be provided
is included in Appendix E.
2. Detention
The detention basin will be constructed to provide the needed reaction time for oxidation
of iron and manganese for both the new and existing water treatment facilities. The basin
will be constructed of concrete and baffled to provide approximately 30 minutes of
detention time. Sludge draw off piping will be provided to aid in cleaning any settled
solids from the bottom. The settled solids will be discharged into the sanitary sewer.
Bypass piping will be provided so routine maintenance can be provided without
disturbing the plant operations. The preliminary layout for the detention basin is
presented in Figure 4-2.
3. Filtration
After the detention tank, the water will be able to flow into the four concrete filters. The
filters will operate at a maximum filtration rate of 3-gpm/sq. ft. The filters will operate
under influent flow splitting mode. As the filters collect the iron and manganese
particulates, the water level in the filters raises until it reaches an elevation where the
filter needs to be cleaned. An available head equivalent to 6-feet of head loss will be
provided for headloss development in the new filters. Dual filter media consisting of
anthracite and sand will be provided. This will allow for the iron and manganese to be
captured in the entire depth of the filter media, which will increase the filter run lengths.
A preliminary layout of the new filters is presented in Figure 4-2. The filtered water will
be collected through a Leopold type of underdrain system. Manufacturer's literature for
the Leopold type of underdrain system is included in Appendix E. The filter backwash
system will incorporate both air and water wash for backwashing the filters. The use of
air in the backwashing system will ensure a cleaner filter media and reduce the amount of
water that has to be used for backwashing the filters. A backwash pump will be provided
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-6
Prepared by Bolton & Menk, Inc.
with a VFD drive type to provide low, medium and the high rate water backwash rates
required with Leopold type of underdrain system.
4. High Service Pumping with Clearwell/Reservoir
A 1 ,500,000-gallon clearwelllground reservoir will be constructed with the treatment
facility. The clearwell will be divided into two compartments so that maintenance can be
provided without curtailing the water treatment facility operations. Three high service
pumps will be provided, each having a rated capacity of2,750 gpm at 165 feet TDH and
150 hp motor. The high service pumps will be provided with variable frequency drives
(VFD) for pumping at variable rates. The high service pumps will also have the
capability to be used for filter backwashing if necessary.
Information on examples ofthe high service and backwash pumps are included in
Appendix E.
5. Backwash Water Reclamation Facilities
Backwash water reclamation facilities allow the waste wash water from the filters to be
recycled back to the water treatment facility. The settled solids in the backwash water
would be discharged into the sanitary sewer system.
The State of Minnesota Legislature has passed legislation that requires all communities
serving more than 1,000 persons to prepare a Water Conservation and Emergency Plan.
This plan requires communities to develop strategies to reduce the amount of water
usage. Any type of recycling of water is highly recommended.
The backwash water reclamation tanks would be a separate buried concrete structure.
Based on recovering over 95 percent of the backwash water, the estimated annual savings
of well water usage is 20 to 25 million gallons and also saves the same amount from
entering the sanitary sewer system.
D. TREATMENT PLANT HYDRAULIC PROFILE
The hydraulic profile for the treatment facility is shown in Figure 4-3. The raw water from the
wells is pumped to the top of the aerator; from there it flows by gravity to the detention tank.
After the detention tank, the water flows into the filters and there is approximately 6 feet of
available headloss in the filters. The water will then pass into the clearwell/reservoir and the high
service pumps then pump the finished water into the distribution system.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-7
Prepared by Bolton & Menk, Inc.
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PRIOR lAKE, MINNESOTA
WATER TREATMENT FACILITY
HYDRAULIC PROFILE
A NWS 11-13-06
FIGURE
J:\PRIOR LAKE\I-fYDRAUUC PROFJLE.dwg 11/10/06 3:18 pm
-
4-3
E. CHEMICAL FEED SYSTEM
1. General
The chemicals fed at the existing well houses are chlorine, fluoride and polyphosphate.
These chemicals will continue to be added at the new water treatment facility as well as
the following chemicals:
· Potassium Permanganate solution will be added to the detention tank effluent for
manganese removal;
· Chlorine for disinfection;
· Polyphosphate for corrosion inhibition and lead and copper control.
· Hydrofluosilicic Acid for fluoridation.
Each chemical feed system is discussed separately below. The chemical addition
locations are shown in the Process Flow Diagram, Figure 4-1. The chemical feed design
criteria are presented in Table 4-2 and basic equipment information is provided in
Appendix E.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-8
Prepared by Bolton & Menk, Inc.
Table 4-2
Chemical Feed Design Criteria
Prior Lake Water Treatment Facility Improvements
Description Units Value
Flow Capacity
Maximum GPM 5,420
Potassium Permanganate
Dosage (maximum) mg/L 1.0
Dosage (average) mg/L 0.5
Metering Pumps
Type Positive Displacement
- Hydraulic Actuated Diaphragm
Number No. 2
Capacity
Maximum gallhr . 32
Average gallhr. 16
Storage Capacity gal. 1,500
(2 x 750 gal. tank)
Fluoride
Dosage (maximum) mg/L 1.2
Dosage (average) mg/L 1.0
Metering Pumps
Type Positive Displacement
- Solenoid Actuated Diaphragm
Number No. 2
Capacity
Maximum gallhr. 1.6
Average gallhr. 1.3
Storage Tank Cap. gal. 165
Feed Tank gal. 750
Hypochlorite
Dosage (maximum) mg/L 2.0
Dosage (average) mg/L 1.0
Metering Pumps
Type Positive Displacement
Number No. 3
Capacity
Maximum gallhr . 5.4
Average gallhr . 2.7
Day Tank gal. 165
Storage Tank gal. 2 x 1700
City of Prior Lake, Minnesota
Design Report - M21. 3 8412
Page 4-9
Prepared by Bolton & Menk, Inc.
Table 4-2
Chemical Feed Design Criteria
Prior Lake Water Treatment Facility Improvements
Description Units Value
Polyphosphate
Dosage (maximum) mg/L 2.0
Dosage (average) mg/L 0.5
Metering Pumps
Type Solenoid Actuated
Capacity
Maximum gallhr . 0.5
Average gallhr. 0.12
Storage Tank gal. 165
Filter Aid Polymer
Dosage (maximum) mg/L 0.3
Dosage (average) mg/L 0.1
Feed System Stranco PolyBlend
2. Chlorine
The primary chlorination feed point will be high service pump discharge. The
chlorinators will be sized to feed up to 2.0-mg/L chlorine at the feed point. In addition,
chlorine injection points will be provided at the following locations:
· Raw water inlet to aerator (manual control)
· Aerator effluent (flow paced control)
· Filter influent (flow paced control)
· Filter effluent (flow paced control)
· Reclaimed water pump discharge (flow paced control).
Aerator inlet and aerator effluent chlorination will be an intermittent operation for
maintaining the aerator and detention tank so they are free of iron bacteria and other
microbial growth.
As mentioned previously, the City currently uses gaseous chlorine at their various well
house locations. Some discussion with City staff has indicated a possibility of using
liquid bleach (sodium hypochlorite) instead of gaseous chlorine at the water treatment
facility. Using gaseous chlorine requires less building space and is a more stable product
to use, however, there are additional reporting requirements for gaseous chlorine and
there is often a negative public perception when using gaseous chlorine. Sodium
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 4-10
Prepared by Bolton & Menk, Inc.
hypochlorite, on the other hand, requires substantially more space because it is a liquid
and only 12.5% available chlorine. Sodium hypochlorite is not as stable and over time
will lose strength, thereby requiring additional chemical to be added to meet the desired
chlorine residual. There are minimal reporting requirements for liquid chlorine and a less
negative public perception. The design report is based on using sodium hypochlorite.
3. Potassium Permanganate
Manganese removal is achieved by adding potassium permanganate (KMn04) after raw
water has passed through the aerator. Multiple potassium permanganate feed locations
will be provided. The ideal feed location will depend on the raw water characteristics;
generally, the outlet of the detention tank is a good location for potassium permanganate
addition.
Potassium permanganate will be delivered to the plant site in powder form and mixed
with plant water to create a two percent solution. Two chemical feed tanks with mixers
will be provided. The drum containing dry potassium permanganate will be set on a
weighing scale and chemicals will be transferred into the mix tank using an eductor
system. A mixer in the tank is operated by an automatic timer that keeps the potassium
permanganate in solution. Two flow proportional chemical feed pumps will be used to
feed potassium permanganate solution. A potassium permanganate analyzer will
continually analyze the concentration ofKMn04 in the filtered effluent. If the feed rate is
too high and the filtered water turns pink, the analyzer will send out an alarm and shut
down the chemical feed pump. The potassium permanganate feed rate will be determined
by routinely using the "KMn04 Demand" test using the feed solution. The details of this
test will be presented in the operations and maintenance manual.
4. Fluoride
Fluoride will be fed using Hydrofluosilicic acid (23% solution). The acid will be fed
"neat" without any dilution. One-day storage tank and one bulk storage tank will be
provided. Chemical metering pumps will feed out of the smaller day tank as the tank is
calibrated in one-gallon increments to measure daily usage. From the day storage tank,
fluoride will be pumped to the high service pump discharge feed point by a flow paced
solenoid metering pump. Fluoride metering pump will be flow paced by the finished
water flow rate.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-11
Prepared by Bolton & Menk, Inc.
5. Polyphosphate
To comply with lead and copper control regulations, a corrosion inhibitor will be added
to the finished water. Polyphosphate will be stored in a storage tank and fed by a flow
paced chemical metering pump. Flow pacing will be done by a flow rate signal from the
finished water flow meter.
6. Polymer
The option of polymer addition to help settle iron and manganese in the filters will be
available. Based on pilot plant testing, it is anticipated that polymer addition will not be
required, however, since source waters can change, polymer addition equipment will be
installed.
F. SUPPORT SERVICE FACILITIES
1. Water Metering Testing Area, HV AC, Lighting, Air, Wastewater Service,
Dehumidification System
The water treatment facility will utilize HV AC strategies depending on the functional
area within the facility.
The chemical feed area will have electrical or hot water heat unit heaters and special
ventilation depending on building code requirements. The high service pump, filter area,
and piping gallery will have electric or hot water heat unit heaters. The control room area
will have a commercial electric heating and air conditioning unit located in the
mechanical room. High efficiency fluorescent lighting will be utilized throughout the
new water treatment facility. The compressed air system will be designed for the
pneumatic valve operators. A dual air compressor unit will be provided and information
is provided in Appendix E. A desiccant type of dehumidification unit (Bry-Air) will be
provided where open water is present in tanks such as the filters or detention tank. All
other areas will be dehumidified using refrigerant type (Hi-E Dry by Thermastor)
dehumidifiers.
Service water is required in the chemical feed area for dilution of the chemicals and
transferring of these chemicals to the different treatment areas. Service water will also be
provided throughout the new treatment facility for operation and maintenance purposes.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 4-12
Prepared by Bolton & Menk, Inc.
Wastewater service will be provided to the water treatment facility. Men and women
restrooms will be provided. The settled backwash solids will be pumped and discharged
to the sanitary sewer.
A watermain from the water treatment facility will be constructed for providing the
treated water into the distribution system.
The garage area will include a storage mezzanine, workshop, and vehicle parking areas.
2. Overflow Structure
Overflow structures for the detention basin and clearwell will be provided to protect the
new treatment facility from flooding. Drainage facilities will be designed for all of the
new structures and incorporated into the stormwater drainage for the site.
3. Electrical Service
The electrical service to the water treatment facility will be installed to provide a reliable
source of power. The service should consist of a three phase 400 KV A pad mounted
transformer with a secondary voltage of 277/480 the transformer size will be verified
during final design. This service will provide the necessary power to operate all of the
pump motors, heaters, and lighting panels that include the controls and instrumentation.
In addition, a backup generator will be provided to allow the plant and wells on-site to
operate in the event of a power outage.
4. Security
Currently the west, south and east sides of the site are fenced with galvanized chain link
fence. Since the northwest elevation of the proposed building has no entrance or access
points, it is proposed to run fencing only along the south, east and west sides of the
building, tying the fence into the building. This will provide the security necessary
without running fencing around the entire perimeter of the site. In addition, a building
security system for the facility will be installed.
G. CONTROL SYSTEM
1. Control
The control system recommended for the new water treatment facility is a computer
based system using non-proprietary hardware and software. A Programmable Logic
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-13
Prepared by Bolton & Menk, Inc.
Controller (PLC) would be the main computer hardware located at the new water
treatment plant. The elevated tower and the wells would be tied into the PLC by radio
remote terminal units or direct buried control wires. The PLC manufacturer would
provide a standard communication card programmed with a standard communication
protocol. The computer system could be expanded, modified or reprogrammed by any
system integrator.
The PLC manufacturers that we would recommend are Allen Bradley or General Electric.
Both of these manufacturers are multi-national, million dollar sales companies with
proven sales, service and distribution support. These companies have distributors located
in every major metro area of the United States.
The Supervisory Control Panel (SCP) will be located in the water treatment facility. The
SCP will contain the PLC's; Operator Interface Terminal (OIT), modem and an
uninterruptible power supply (UPS). Linked to the SCP will be a computer system,
running Intouch by W onderware, or equal, to control the water plant operations, set
points, and monitor alarms. A laptop computer will also be provided for monitoring the
water treatment facility operations for the on-call duty staff.
The water system will be controlled by the water level in the elevated water tower. The
water tower level will control the high service pumps.
The high service pumps will be rotated in sequence after the tower is full and all pumps
have stopped. If there is a pump failure, the pump that is not being used as a lead or lag
pump will replace the down pump.
The wells will be controlled based on the levels in the clearwelllreservoir.
Sample computer screens are included in Appendix E.
2. Monitoring
Influent and finished water quantities will be metered at their respective locations. The
values will be transmitted to the SCP for indication, recording and totalization. Magnetic
flow or propeller meters will be provided for the various flow monitoring points.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-14
Prepared by Bolton & Menk, Inc.
The influent flow signal will be utilized for pacing of chemical feed equipment including
chlorine and potassium permanganate. In addition, the flow meter signals from the
existing wells can be brought to the treatment facility and used as a backup for the
influent flow meter
Level indication of the clearwell/reservoir will be provided for monitoring of available
in-plant storage. This device will indicate if sufficient finished water is available for
filter backwashing during high service distribution demand. An ultrasonic level
indicator will be provided to measure the water level in the clearwell.
A pressure indicator will be provided in the high service discharge manifold to monitor
the pressure of the pump discharge. A pressure relief valve will be provided to relieve
any excess pressure in the high service pump discharge manifold.
A summary of instrumentation functions proposed for the SCP is contained in Table 4-3.
A list of the proposed alarms intended for annunciation at the SCP is shown in Table 4-4.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 4-15
Prepared by Bolton & Menk, Inc.
Table 4-3
Supervisory Control Instrumentation Functions
Function Type of Monitoring
Flow Metering
Influent-Raw Water Indicate, Totalize - Local
Indicate, Totalize, Record - SCP
High Service Indicate, Totalize - Local
Indicate, Totalize, Record - SCP
Backwash Reclaim Indicate, Totalize - Local
Indicate, Totalize, Record - SCP
Levels
Filter Indicate - SCP
Indicate - Filter Console
Clearwell Indicate - SCP
Indicate - Filter Console
Reclaim Tank Indicate - SCP
Elevated Water Tower Indicate - SCP
Table 4-4
Supervisory Control Alarm Points
Location of Equipment Alarm Value
Well Pumps Pump Failure
Well House Low Temperature
Well Pumps High Drawdown
Aerator Blower Failure
Detention Tank High Level Alarm
Clearwell Low Level
Clearwell High Level
Potassium Permanganate Analyzer High Level
Chlorine Booster Pump Failure
High Service Pumps Failure
Backwash Pump Failure
Reclaim Pump Failure
Aerator Pipe Gallery Flooding Flooding Level
Tower No.2 High Level
Tower No.2 Low Level
Tower No.3 High Level
Tower No.3 Low Level
Reclaim Tank High Level
Reclaim Tank Low Level
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 4-16
Prepared by Bolton & Menk, Inc.
SECTION 5
TREATMENT PROCESS AND DESIGN CRITERIA
FOR EXPANDED FACILITY - 7.5 MGD
A. GENERAL
City staff originally planned to add an additional water treatment facility on the west side of the
City of Prior Lake. However, during the preliminary design phase for the water treatment
facility, the City discovered that adding the amount of wells required on the west side of the City
for a water treatment facility is not feasible due to the geology of the area. Therefore, it was
determined that an option to expand the proposed facility to 7.5 mgd (6,250 gpm) should be
explored in the preliminary design report. Similarly to Section 4, the gpm rate is based on a 20-
hour day, allowing 4-hours of rest for the production wells since it is not good practice to operate
wells for 24-hours continuous. Operating on a 20-hour day often is not feasible for growing
communities such as Prior Lake. Therefore, the benefit of designing the treatment facility around
a 20-hour day is it provides additional operational flexibility. It allows for routine maintenance of
the facility even during peak demand periods and allows for expanded capacity without making
any changes to the facility. The facility will also allow for adaptation to meet potential future
limits. Some additional space is provided for additional chemical feed points and other
equipment to meet potential future limits or to adjust to potential changes in water quality.
The design philosophy for the water treatment improvements is to provide a high quality finished
water, a plant that is easy to operate, and has low maintenance costs. This section will discuss the
design criteria and plant layouts for increasing the treatment facility, by 1 mgd, to facility with a
capacity of7.5 mgd.
B. PLANT PROCESS
The main water treatment process consists of aeration, detention, and filtration. The following
sections describe the treatment units and criteria. Figure 5-1 shows the revised site plan for the
larger facility and Table 5-1 presents the design criteria for the water treatment improvements.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 5-1
Prepared by Bolton & Menk, Inc.
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5-1
Table 5-1
Design Criteria - 7.5 MGD (6,250 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Caoacitv
Description Units New Facilities
Aeration
Quantity number 2
Construction type Aluminum housing with induced draft PVC
Capacity gpm 3,600 gpm
Size feet 12' x 12' x 10'
Blower capacity 10,800 cfm
Blower HP hp 2 x 1.5 HP
Detention Tank
Quantity number 1
Construction type Concrete
Detention Time @ 6,250 gpm minutes 30
Volume gallons 196,100
Basin Depth (Normal) feet 20
Basin Width feet 9.5
Basin Length (Effective) feet 138
Filters
Quantity number 6
Construction type concrete
Control Method Influent Flow Splitting
Filter Area Per Cell sq. ft. 440
Total Filter Area sq. ft. 2,640
Filtration Rate gpm/sq. ft. 2.5
Media type Dual media (anthracite and Silica sand)
Anthracite Depth inches 15
Effective Size mm 0.8 - 1.0
Silica Sand Depth inches 15
Effective Size mm 0.45 - 0.55
Underdrain System type Leopold Universal
Media Retainer type 14" Reverse Graded Gravel
Method of Backwashing type Air and Water
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 5-2
Prepared by Bolton & Menk, Inc.
Table 5-1
Design Criteria - 7.5 MGD (6,250 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Rate of
Air Scour scfm/SF 3
Water Backwashing gpm/SF 15
Hh!h Service Pumps
Quantity number 3
Capacity gpm 3,125 @ 165' TDH
Pump type Vertical Turbine
Pump Speed rpm 1,750
Drive type VFD
Motor hp 175
ClearwelllBackwash Supplv
Quantity number 1
Cells number 2
Construction type Concrete
Volume (total) gallons 249,400
Basin Depth feet 15
Basin Width feet 39
Basin Length feet 57
Reservoir
Quantity number 1
Cells number 1
Construction type Concrete
Volume gallons 1,260,250
Basin Depth feet 15
Basin Width feet 115
Basin Length feet 117
City of Prior Lake, Minnesota
Design Report - M21. 3 8412
Page 5-3
Prepared by Bolton & Menk, Inc.
Table 5-1
Design Criteria -7.5 MGD (6,250 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Backwash Reclaim System
Quantity number 3
Construction type Concrete
Effective Capacity per Basin gallons 93,500
Basin Depth (water depth) feet 16
Basin Length feet 67
Basin Width feet 35
Reclamation Pump
Quantity number 3
Capacity gpm 250 @ 32' TDH
Pump type Submersible
Speed rpm 1,750
Motor hp 5
Slud2e Disposal Pump
Quantity number 3
Capacity gpm 100
Pump type Submersible
Speed rpm 1,750
Motor hp 5
Backwash Pump
Quantity number 1
Capacity gpm 6,600 @ 50' TDH
Pump type Vertical Turbine
Pump Speed rpm 1,180
Drive type VFD
Motor hp 150
Backwash Aeration System
Quantity of Blowers number 1
Blower type Positive Displacement
Blower Capacity cfm 1,320
Motor hp 75
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 5-4
Prepared by Bolton & Menk, Inc.
Table 5-1
Design Criteria -7.5 MGD (6,250 gpm)
Prior Lake Water Treatment Facility Improvements
Size of Capacity
Description Units New Facilities
Chemical Feed
Chlorine
Feed System type Liquid
Control Method type Flow Proportioned Chemical Feed Pumps
Storage Tank gallons 2 @ 1,700 /1 @ 165
Potassium Permanganate
Feed System type 2% Dilute Mix Solution
Control Method type Flow Proportioned Chemical Feed Pumps
Storage/Mix Tank gallons 2 @ 1,000
Fluoridation
Feed System type Hydrofluosilicic Acid
Control Method type Flow Proportioned Chemical Feed Pumps
Storage/Mix Tank gallons 1 @ 750/1 @ 165
Polymer
Feed System type Polyblend Type Mix Feed
Control Method type Flow Proportioned Chemical Feed Pumps
Corrosion Inhibitor
Feed System Type Polyphosphate liquid
Control Method Type Flow Proportioned Chemical Feed Pumps
Storage Tank gallons 1 @ 165
c. TREATMENT PROCESS
The treatment process for the expanded facility is the same as proposed and discussed in Section
4 and will not be further discussed in this section. Similarly, the flow diagram for the 7.5 mgd
does not change for the larger facility and can be referenced in Figure 4-1. The revised floor plan
for the 7.5 mgd facility is presented in Figure 5-2.
Page 5-5
Prepared by Bolton & Menk, Inc.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
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WATER TREATt.tENT FACIUlY
FLOOR PLAN
7.5 t.tGD
FlCURE
5-2
D. TREATMENT PLANT HYDRAULIC PROFILE
The hydraulic profile for the treatment facility is similar to that presented previously as shown in
Figure 4-3. The raw water from the wells is pumped to the top of the aerator; from there it flows
by gravity to the detention tank. After the detention tank, the water flows into the filters and there
is approximately 6 feet of available head loss in the filters. The water will then pass into the
clearwell/reservoir and the high service pumps then pump the finished water into the distribution
system.
E. CHEMICAL FEED SYSTEM
The chemicals fed system for the 7.5 mgd facility is similar to that described in Section 4 and the
chemical feed design criteria are presented in Table 5-2. The chemical processes will not be
further described in this section and can be referred to in Section 4.
City of Prior Lake, Minnesota
Design Report - M21.38412
Page 5-6
Prepared by Bolton & Menk, Inc.
Table 5-2
Chemical Feed Design Criteria
Prior Lake Water Treatment Facility Improvements
Description Units Value
Flow Capacity
Maximum GPM 6,250
Potassium Permanganate
Dosage (maximum) mg/L 1.0
Dosage (average) mg/L 0.5
Metering Pumps
Type Positive Displacement
- Hydraulic Actuated Diaphragm
Number No. 2
Capacity
Maximum gal/hr. 37.5
Average gal/hr. 18.75
Storage Capacity gal. 2,000
(2 x 1,000 gal. tank)
Fluoride
Dosage (maximum) mg/L 1.2
Dosage (average) mg/L 1.0
Metering Pumps
Type Positive Displacement
- Solenoid Actuated Diaphragm
Number No. 2
Capacity
Maximum gal/hr . 1.85
Average gal/hr. 1.5
Storage Tank Cap. gal. 165
Feed Tank gal. 750
Hypochlorite
Dosage (maximum) mg/L 2.5
Dosage (average) mg/L 1.5
Metering Pumps
Type Positive Displacement
Number No. 3
Capacity
Maximum gal/hr . 5
Average gal/hr . 2.5
Day Tan gal. 165
Storage Tank gal. 2 x 1,700
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 5-7
Prepared by Bolton & Menk, Inc.
Table 5-2
Chemical Feed Design Criteria
Prior Lake Water Treatment Facility Improvements
Description Units Value
Polyphosphate
Dosage (maximum) mg/L 2.0
Dosage (average) mg/L 0.5
Metering Pumps
Type Solenoid Actuated
Capacity
Maximum gal/hr . 0.54
Average gal/hr. 0.13
Storage Tank gal. 165
Filter Aid Polymer
Dosage (maximum) mg/L 0.3
Dosage (average) mg/L 0.1
Feed System Stranco PolyBlend
F. SUPPORT SERVICE FACILlTES
The support service facilities will be similar to those discussed in Section 4 and will not be
further discussed in this section.
G. CONTROL SYSTEM
The control system recommended for the 7.5 mgd facility is similar to that discussed in Section 4
and will not be further discussed in this section.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 5-8
Prepared by Bolton & Menk, Inc.
SECTION 6
ESTIMATED CONSTRUCTION COSTS, FUNDING AND PROJECT SCHEDULE
A. ESTIMATED CONSTRUCTION COSTS AND PROJECT FUNDING
The estimated construction cost is based on published and unpublished data on costs for similar
facilities and current equipment costs provided by manufacturer's representatives and suppliers.
Table 6-1 summarizes the estimated construction costs for the Water Treatment and Storage
Facility for both the 6.5 mgd and 7.5 mgd options. In addition, Table 6-1 denotes the projected
funding sources and amounts.
Table 6-1
Construction Cost Estimate/Project Funding
Prior Lake, Minnesota
Item 6.5 MGD 7.5 MGD
Estimated Construction Cost $10,905,000 $12,535,000
Design Contingency* $475,000 $475,000
Construction Contingency* * $200,000 $200,000
AdminlEngineering/Legal/T esting* * * $868,300 $918,300
Bonding Costs $208,000 $208,000
Estimated Proiect Cost $12,656,300 $14,336,300
Funding Source
Water Storage Fund $2,000,000 $2,000,000
Trunk Reserve**** $798,504 $2,332,260
Water Revenue Bonds $9,857,796 $10,004,040
Total Revenue $12,656,300 $14,336,300
* For changes during design and material cost changes
** For changes during construction
*** Includes City Admin. Costs ($150,000)
****8% (0.5 MGD) New Development Cost Participation for 6.5
MGD/20% (1.5 MGD) for 7.5 MGD
The cost difference between the 6.5 mgd and 7.5 mgd facility is related to increased building size
for the filters and detention tank, larger pipe sizes, higher capacity pumps and increased size for
the chemical equipment including pumps and chemical storage tanks.
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 6-1
Prepared by Bolton & Menk, Inc.
There is a potential savings of approximately $200,000 for both options if the hip roofs were
eliminated from the garage and pump room areas. In lieu of the hip type roofs, a rubber
membrane, flat-type roof would be installed.
As noted in Table 6-1, the City of Prior Lake plans to fund the water treatment and storage
facility improvements through a variety of sources. The majority of the water treatment facility
will be paid for through the sale of water revenue bonds, to which, water rates have already been
raised. In addition, the storage portion of the project would be financed from the water storage
fund and a portion of each facility would be financed through trunk reserves.
Operation and maintenance (O&M) costs will increase with the addition of this facility due to
increased power and chemical consumption and user rates have been raised accordingly to
account for the increased O&M costs. City staff will provide a detailed analysis on the impacts of
the projected O&M costs on the user rates prior to awarding the water treatment facility project.
In addition, the City may be eligible for a Minnesota sales tax refund on the qualifying capital
equipment for the production of water. This would include all equipment for the production of
water and the necessary portions of the buildings required to house this equipment. City staff is
currently reviewing the viability of obtaining a sales tax refund on the qualifying equipment.
B. ASSOCIATED IMPROVEMENTS
Various additional improvements are required as a result of the new water treatment facility and
are for installation of new raw watermain to the plant site for wells 8, 9 and 10. The
improvements are shown below in Table 6-2 along with the estimated construction costs. These
improvements will be paid for through the trunk reserve fund and will be completed prior to
placing the water treatment facility on-line.
Table 6-2
Associated Improvements
Prior Lake, Minnesota
Year Description Estimated Cost
2007 Well No. 10 $1,000,000
C.R. 21 Watermain $400,000
2008 Brooksville Hills Watermain $250,000
City of Prior Lake, Minnesota
Design Report - M2lJ 8412
Page 6-2
Prepared by Bolton & Menk, Inc.
C. PROJECT SCHEDULE
The project schedule for completion of the design and the projected construction schedule for the
project is presented in Table 6-3.
Table 6-3
Proposed Schedule
City of Prior Lake Water Treatment Improvements
Item Date
1. WTPC and City of Prior Lake staffreviews Design Report. November 13, 2006
2. Present Design Report to City Council December 4, 2006
3. Prepare final plans & specifications. Dec. 2006 - March 2007
4. City of Prior Lake staff review plans & specifications at 50 and 90 Dec. 2006 -March 2007
percent levels.
5. Minnesota Department of Health review plans & specifications. March 2007
6. Advertise for bids. April 2007
7. Open bids and award contract. May 2007
8. Initiate construction. June 2007
9. Initiate operations and complete construction. Dec. 2008/Jan. 2009
City of Prior Lake, Minnesota
Design Report - M21.3 8412
Page 6-3
Prepared by Bolton & Menk, Inc.
APPENDIX A
PILOT PLANT TESTING REPORT
Water Pilot Plant Report
for the
BMI Project No. M21.38412
November 2006
Prepared by:
WATER PILOT PLANT REPORT
PRIOR LAKE, MINNESOTA
NOVEMBER 2006
BMI PROJECT NO. M21.38412
I hereby certify that this plan, specification or report was prepared by me or under my direct supervision, and that I
am a duly Licensed Pro essional En i eer under the laws of the State of Minnesota.
Signature:
Typed or Printed Name: Seth A. Peterson
Date O-=t- AJ{)1/ > 2eDb
Lic. No. 26468
BOLTON & MENK, INe.
CONSULTING ENGINEERS & LAND SURVEYORS
SECTION
TABLE OF CONTENTS
EXECUTIVE SUMMARY
SECTION 1- BACKGROUND
SECTION 2- OPERATIONAL PROCEDURES
A.
B.
C.
SET UP
BACKWASH PROCEDURE
FILTRATION
SECTION 3 -SUMMARY OF OPERATIONS
A.
B.
c.
RUN 1
RUN 2
RUN 3
SECTION 4 - SUMMARY OF RESULTS
SECTION 5 - RECOMMENDATIONS
Figure No. 1 - Pilot Plant Process Flow Diagram
Table No.1 - Water Treatment Facility Prior Lake Filtration Log - Run No. 1
Table No.2 - Water Treatment Facility Prior Lake Filtration Log - Run No.2
Table No.3 - Water Treatment Facility Prior Lake Filtration Log - Run No.3
Table No.4 - Summary of Data - Prior Lake Pilot Plant Study
PAGE
1
2
3
4
5
6
7
8
9
10
11
Follows Page 3
Follows Page 7
Follows Page 8
Follows Page 9
Follows Page 10
M21.38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 1
EXECUTIVE SUMMARY
The City of Prior Lake has higher than recommended levels of iron and manganese in their water
supply wells. Levels of manganese have been higher than the secondary drinking water standard
of 0.05 mglL in all wells while levels of iron have been higher than the secondary standard of 0.3
in some wells. There has been minimal to no issues with primary drinking water standards in all
wells. Pilot plant testing was performed to demonstrate the effectiveness of treatment at
addressing the iron and manganese issues. The pilot plant removed iron and manganese to below
the secondary limits and was effective in producing a high quality and safe drinking water from
the City's wells.
M21.38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 2
SECTION 1: BACKGROUND
Municipal water is monitored fro two standards of usage: primary standards and secondary
standards. Primary standards are to protect the health and well being of consumers. Ifwater
exceeds a primary standard, acute or chronic health issues may be caused for consumers. Acute
health issues occur very rapidly and may be caused by a single exposure or consumption of the
water. Chronic health issues may require 20, 30, or 50 years of consistent and constant exposure.
The City of Prior Lake has had minimal to no issues with primary drinking water standards.
Secondary standards are a recommendation to improve the usability of water. Standards for iron
and manganese prevent colored water and stains. Other secondary standards include, odor, taste,
and hardness.
The City of Prior Lake will use existing wells 3,4,5, and 7 in their water treatment facility as well
as new wells 8 and 9. Wells 3,4, and 5 exceed the secondary drinking water standards for
manganese and well 7 exceeds the secondary drinking water standards for iron and manganese.
As water is pumped from the aquifer, these minerals are removed from the ground in the water.
The City of Prior Lake is monitoring the levels ofthese constituents to improve the overall water
quality. A pilot test was run to determine the effectiveness of treatment and the associated
operational and maintenance costs.
The iron and manganese in these has the potential to stain laundry and water fixtures as well as
minimal taste and odor issues. The secondary standard for iron is 0.3 mg/L and the secondary
standard for manganese is 0.05 mg/L. The concentration of iron in the existing wells ranges
from .019 mg/L to 0.62 mg/L while the concentration of manganese range from 0.199 to 0.343
mg/L.
M21.38412 -Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 3
INFLUENT
FROM
WELL NO.4
FILTER A
INFLUENT
VALVE
-0
:;0
o
-00
:;OfTl-o.,.,
0(/)--
:;o(/)r0
Oc
.,.,-1:;0
S;:S-ofTl
~:ES;:Z
~ zO
o .
~--1-->>
Ze:;
:;0
}>
~
FILTER
A
MANGANESE
GREEN
SAND
MEDIA
FILTER A
EFFLUENT
VALVE
AERATOR
POTASSIUM PERMANGANATE
DIFUSSER
BACKWASH MAIN LINE
FILTER A FILTER B
BACKWASH INFLUENT
EFFLUENT VALVE
VALVE
FILTER A
BACKWASH
INFLUENT
VALVE
SAMPLE
TAP
FILTER B
EFFLUENT
VALVE
FILTER
B
SILICA
SAND
MEDIA
DETENTION TANK
BACKWASH EFFLUENT
FILTER B
BACKWASH
EFFLUENT
VALVE
FILTER B
BACKWASH
I N FLU ENT
VALVE
SAMPLE
TAP
FILTER
PUMP
TANK
OVERFLOW
WASTE TO
STORM
SEWER
AIR BACKWASH
MAIN LINE
VALVE
EFFLUENT
SECTION 2 - OPERATIONAL PROCEDURES
Figure No. I shows the process flow diagram for the pilot plant.
A. Setup Procedure
l) Connect raw water supply to pilot plant.
2) Connect pilot plant to power supply.
3) Air is supplied from an air compressor.
4) Connect chemical feed equipment to chemical feed points.
5) Prime chemical feed pumps. Verify chemical is fed to water.
6) Set chemical feed rate.
7) Start well pump and open valve to supply water to the pilot plant.
8) Set raw water flow rate to 3.5 gpm. Connect air supply and record aeration rate. Verify
drain valves are closed.
9) Fill detention basins. Basin shall be flowing full to operate at a design detention time of
30 minutes.
lO) Close influent valve.
11) Proceed to backwash.
M21.38412 -Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 4
B. Backwash Procedure
1) Relocate air line from aerator to air backwash connection.
2) Verify all filter effluent valves are closed. Open the valve on the backwash main line
(blue handled valve).
3) Open the backwash drain valve at the top of the filter being backwashed and close the
corresponding valve on any other filter not being backwashed.
4) Gradually open the backwash valve of the selected filter to slowly fill it with water. If
media is being pushed up the column, tap the side of the filter to loosen media. When
water column reaches maximum height close the backwash main line valve. After the
backwash main line valve is closed be sure to fully open the selected filter backwash
valve.
5) Start the air compressor.
/
6) Air wash the filter by gradually opening the air wash valve. Air wash the filter as
necessary, approximately 4 to 5 minutes, to ensure all filter media has been dispersed.
After the air wash has been completed close the air wash valve, close the selected filter
backwash valve, and open the backwash main line valve.
7) Backwash the selected filter by gradually opening its backwash valve to fill the column
with water. Keep opening the valve until media is fluidized and at approximately 10"
from the top of the column. Backwash the filter for 10-15 minutes. Verify the water
leaving the top of the filter is clear prior to termination of backwash.
8) After filter has been successfully backwashed gradually close the filter's backwash valve,
taking care that the media descends at a slow rate.
9) Repeat Steps 3 through 7 for any other filter that needs to be backwashed. When finished
backwashing filters make sure that all filter backwash valves are closed including the
main line valve.
M21.38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 5
c. Filtration Procedure
I) Take raw water sample directly from well sample tap, test for iron and manganese
according to procedures outlined in the HACH users manual, and record findings.
2) Verify raw water supply is operational.
3) Attach air line to aerator and verify that it is operational (bubbles in aerator).
4) Open the raw water valve and set to 3.5 gpm.
5) Turn on chemical feed pump. Verify chemical pump is set to specified chemical feed
rate.
6) Operate filter feed pump.
7) Open filter influent valves and set to desired rate. 0.4 gpm corresponds to filter design
rate of2.0 gpm/ft? while 0.6 gpm corresponds to filter design rate of3.0 gpm.
8) Take samples at regular intervals from the effluent sample tap of each filter and test for
iron and manganese according to HACH users manual. Record findings and filter head
conditions.
9) Adjust chemical dosage to optimize iron and manganese removal.
10) Record water level at each reading until level is 18" above discharge point or until there
is iron or manganese breakthrough. At this point filters will need to be backwashed.
11) If in the middle of a run at the end of the day close filter effluent valves, close the raw
water valve, shut down aerator, shut off chemical feed pumps, and unplug filter feed
pump.
M21.38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 6
SECTION 3 - SUMMARY OF OPERATIONS
A. Run No. 1 - October 11 th, 2006
General
The City of Prior Lake has manganese issues in all of their existing wells and iron issues in one
oftheir existing wells. Well No.4 has the highest levels of manganese and was tested to ensure
the technology employed will achieve the desired results. Silica sand and manganese greensand
were tested side by side to determine media selection. Potassium permanganate chemical
solution was fed for manganese removal.
At approximately 9:00 AM raw water sample from Well No.4 was analyzed for iron and
manganese. After the raw sample was taken, the pilot plant was started and the first effluent
samples were taken at 10:00 AM. The water flow to each filter was 0.4 gpm, which equates to a
filter feed rate of2.0 gpmlfY. Effluent samples were taken from the manganese greensand filter
and the silica sand filter. These samples were analyzed for iron and manganese after they were
collected. The chemical feed rate was changed throughout the day to determine the optimum
feed rate. The pilot plant was shut down for the day at 5:00 PM.
Iron and Manganese Removals
Table No.1 shows the filtration log for run number one. As shown in the table, Well No.4 has
low concentrations of iron in the raw sample. There were no significant increases or decreases in
the iron concentrations on samples taken throughout the day. The level of manganese in the raw
water for Well No.4 was 0.300 mglL, which is significantly higher than the secondary standard
of 0.05 mglL. As shown in Table No.1 manganese levels decreased throughout the day as the
optimum chemical feed rate was found. The water head height rose slightly through the day and
no signs of breakthrough were observed.
M21.38412 -Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 7
TABLE NO.1
Water Treatment Facility
Prior Lake Filtration Log
PILOT FILTRATION LOG FOR RUN NO. 1 Start Time 9:00 AM
Chemical Feed Pump Setting: 6.1 @ start. 5.5 @ 12:40 PM, 5.25 @ 3:20 PM. 5.0 @ 4:15 PM
Stop Time
5:00 PM
Operator Air Flow Sample Iron Manganese Water Head Water Flow
Name Date Time Well No. (cfm) Location (maIL) (mg/L) Height Meter (gpm)
Steve Oct. 11.
Attema 2006 9:00 AM 4 NA Raw 0.01 0.300 NA NA
Steve Oct. 11. Silica Sand 0.00 0.123 44.50 0040
Attema 2006 10:00 AM 4 2.5 Greensand 0.14 0.300 42.50 0.40
Steve Oct. 11. Silica Sand 0.00 0.085 45.50 0040
Attema 2006 11 :00 AM 4 2.5 Greensand 0.00 0.123 43.00 0.38
Steve Oct. 11. Silica Sand 0.02 0.065 45.50 0040
Attema 2006 11 :30 AM 4 2.5 Greensand 0.02 0.070 43.50 0040
Steve Oct. 11. Silica Sand 0.02 0.068 45.75 0.40
Attema 2006 12:00 PM 4 2.5 Greensand 0.00 0.074 43.50 0040
Steve Oct. 11. Silica Sand 0.01 0.056 46.00 0040
Attema 2006 12:30 PM 4 2.5 Greensand 0.00 0.073 43.50 0040
Steve Oct. 11. Silica Sand 0.00 0.063 46.00 0040
Attema 2006 1 :00 PM 4 2.5 Greensand 0.00 0.071 43.50 0040
Steve Oct. 11, Silica Sand 0.02 0.054 46.00 0040
Attema 2006 1 :30 PM 4 2.5 Greensand 0.01 0.051 43.75 0040
Steve Oct. 11. Silica Sand 0.01 0.051 46.25 0040
Attema 2006 2:00 PM 4 2.5 Greensand 0.02 0.041 43.75 0040
Steve Oct. 11, Silica Sand 0.01 0.034 46.50 0040
Attema 2006 2:30 PM 4 2.5 Greensand 0.01 0.050 44.25 0.40
Steve Oct. 11, Silica Sand 0.02 0.039 46.50 0040
Attema 2006 3:00 PM 4 2.5 Greensand 0.03 0.050 44.25 0040
Steve Oct. 11. Silica Sand 0.01 0.042 46.75 0040
Attema 2006 4:00 PM 4 2.5 Greensand 0.00 0.040 44.00 0040
Steve Oct. 11, Silica Sand 0.03 0.054 47.00 0040
Attema 2006 4:30 PM 4 2.5 Greensand 0.02 0.031 45.00 0040
Steve Oct. 11, Silica Sand 0.01 0.045 47.00 0040
Attema 2006 5:00 PM 4 2.5 Greensand 0.01 0.031 45.00 0040
B. Run No.2 - October 12th, 2006
General
At approximately 8:30 AM a raw water sample was taken from Well No.4 and analyzed for iron
and manganese. The water flow to each filter was increased from 0.4 gpm (2.0gpmlft2) to 0.6
gpm (3.0gpmlft2) to determine the feasibility ofincreasing the flow to each filter in the water
treatment facility. The first effluent samples were taken from both filters at 10:30 AM. The
chemical feed rate was changed throughout the day to optimize performance at the new 0.6 gpm
feed rate. The pilot plant was shut down for the day at 4:30 PM.
Iron and Manganese Removal
Table No.2 shows the filtration log for run number two. Similar to the previous day the raw
sample showed low concentrations of iron and high levels of manganese. Iron concentrations
remained low throughout the day as expected. Manganese concentrations decreased throughout
the day as the optimum chemical feed rate was found. The water head height rose slightly during
the day and no signs of breakthrough occurred.
M21.38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 8
TABLE NO.2
Water Treatment Facility
Prior Lake Filtration Log
PILOT FILTRATION LOG FOR RUN NO. ~ Start Time
Chemical Feed Pump Setting: 5.0 A start. 5.5 au1 :15 PM, 6.0 au 2:45 PM
8:30 AM
Stop Time
4:30 PM
Operator Air Flow Sample Iron Manganese Water Head Water Flow
Name Date Time Well No. (cfm) Location (mg/L) (mg/L) Height Meter (gpm)
Steve Oct. 12,
Attema 2006 8:30 AM 4 NA Raw 0.03 0.296 NA NA
Steve Oct. 12, Silica Sand 0.00 0.052 52.25 0.6
Attema 2006 10:30 AM 4 2.5 Greensand 0.00 0.114 49.75 0.6
Steve Oct. 12, Silica Sand 0.02 0.043 54.25 0.6
Attema 2006 11 :00 AM 4 2.5 Greensand 0.00 0.043 50.50 0.6
Steve Oct. 12, Silica Sand 0.02 0.041 54.75 0.6
Attema 2006 11 :30 AM 4 2.5 Greensand 0.02 0.058 50.50 0.6
Steve Oct. 12, Silica Sand 0.01 0.035 54.25 0.6
Attema 2006 12:00 PM 4 2.5 Greensand 0.01 0.043 50.25 0.6
Steve Oct. 12, Silica Sand 0.00 0.035 54.75 0.6
Attema 2006 1 :00 PM 4 2.5 Greensand 0.00 0.045 51.25 0.6
Steve Oct. 12, Silica Sand 0.00 0.016 55.25 0.6
Attema 2006 2:00 PM 4 2.5 Greensand 0.00 0.043 51.75 0.6
Steve Oct. 12, Silica Sand 0.02 0.02 55.75 0.6
Attema 2006 2:30 PM 4 2.5 Greensand 0.01 0.038 51.75 0.6
Steve Oct. 12, Silica Sand 0.04 0.023 56.00 0.6
Attema 2006 3:00 PM 4 2.5 Greensand 0.01 0.039 52.50 0.6
Steve Oct. 12, Silica Sand 0.02 0.025 56.25 0.6
Attema 2006 3:30 PM 4 2.5 Greensand 0.04 0.026 52.75 0.6
Steve Oct. 12, Silica Sand 0.02 0.01 56.50 0.6
Attema 2006 4:00 PM 4 2.5 Greensand 0.00 0.028 53.00 0.6
Steve Oct. 12, Silica Sand 0.02 0.011 56.75 0.6
Attema 2006 4:30 PM 4 2.5 Greensand 0.00 0.026 53.25 0.6
c. Run No.3 - October 13th, 2006
General
At approximately 9:00 AM a raw water sample was taken from Well No.4 and analyzed for Iron
and Manganese. After the raw water sample was taken, the pilot plant was started and the first
effluent samples were taken from both filters around 10:45 AM. The chemical feed rate
remained constant all day and the pilot plant was shut down for the day at 1 :30 PM.
Iron and Manganese Removal
Table No.3 shows the filtration log for run number three. Again, similar to the previous days,
the raw sample showed low concentrations of iron and high levels of manganese. Iron
concentrations remained low throughout the day as expected. Manganese concentrations
decreased throughout the day in both filters. The water head height rose slightly during the day
and no signs of breakthrough occurred in either filter.
M21.38412 -Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 9
TABLE NO.3
Water Treatment Facility
Prior Lake Filtration Log
PILOT FILTRATION LOG FOR RUN NO. ~
Chemical Feed Pump Setting: 6.0 all day
Start Time
9:00 AM
Stop Time
1 :30 PM
Operator Air Flow Sample Iron Manganese Water Head Water Flow
Name Date Time Well No. (cfm) Location (maIL) (mg/L) Heiaht Meter (apm)
Steve Oct. 13,
Attema 2006 9:00 AM 4 NA Raw 0.07 0.300 NA NA
Steve Oct. 13, Silica Sand 0.00 0.045 57.50 0.6
Attema 2006 10:45 AM 4 1.5 Greensand 0.03 0.058 53.00 0.6
Steve Oct. 13, Silica Sand 0.01 0.022 58.00 0.6
Attema 2007 11:30 AM 4 1.5 Greensand 0.05 0.014 54.00 0.6
Steve Oct. 13, Silica Sand 0.03 0.007 58.25 0.6
Attema 2008 12:00 PM 4 1.5 Greensand 0.05 0.018 54.25 0.6
Steve Oct. 13, Silica Sand 0.05 0.000 58.50 0.6
Attema 2009 12:30 PM 4 2.5 Greensand 0.03 0.012 54.50 0.6
Steve Oct. 13, Silica Sand 0.03 0.016 58.75 0.6
Attema 2010 1 :00 PM 4 2.5 Greensand 0.02 0.001 54.50 0.6
Steve Oct. 13, Silica Sand 0.00 0.000 59.00 0.6
Attema 2011 1 :30 PM 4 2.5 Greensand 0.04 0.003 54.75 0.6
SECTION 4 - SUMMARY OF RESULTS
October 11 th through October 13th, 2006
Table No.4 summarizes the results of the pilot plant study for the City of Prior Lake, MN. Iron
has not been an issue in Well No.4 but through aeration and filtration some iron was removed in
both the silica sand and greensand filters. Data indicates that both the silica sand filter and the
manganese greensand filter achieved excellent removals of manganese as indicated on the
average for run number 3. Run number 3 is the best indication of pilot plant performance since
both the water flow to the filters and the chemical feed rate was optimized.
M21.38412 -Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 10
TABLE NO.4
Summary of Data
Prior Lake Pilot Plant Study
Average Iron and Manganese for Runs 1, 2, and 3
Run No.1 Run No.2 Run No.3
Iron Manganese Iron Manganese Iron Manganese
(mg/L) (mg/L) (mg/L) (mg/L) (mg/L) (mg/L)
Raw Water Well
No.4 0.01 0.300 0.03 0.296 0.07 0.300
Effluent of Silica
Sand Filter 0.01 0.052 0.02 0.026 0.02 0.015
Effluent of
Greensand Filter 0.01 0.053 0.01 0.039 0.04 0.018
Note: Data from the first effluent samples were not included on the manganese average
for runs 1 and 2. This was to allow conditions to stabilize in the pilot plant.
SECTION 5 - RECOMMENDATIONS
Based on the information obtained from the pilot testing, both media types performed very well
in removal of iron and manganese. Since removal is similar for both media types, it is proposed
to use dual media filters with 15-inches of silica sand and 15-inches of anthracite due mainly to
the cost savings and availability in using silica sand instead of greensand.
M21. 38412 - Prior Lake, MN
Water Pilot Plant
Prepared by Bolton & Menk, Inc.
Page 11
APPENDIX B
PROPOSED ELEVATIONS AND COMPUTER
GENERATED GRAPHICS
PROPOSED ELEVATIONS FROM 2ND
NEIGHBORHOOD MEETING
CIVIC
1
3.0
NORTHWEST ELEVATION
SCALE: 3/32".,'-0" ,......
,.
SOUTHEAST EVATION
1
30Y " -
SCALE: 3/32".'.-0 "'...
I
;.
PROPOSED ELEVATIONS FROM 2ND
NEIGHBORHOOD MEETING
RESIDENTIAL
NORTHWEST ELEVATION
1
30Y -
SCALE: 3/32".1'-0. !S&ri
I
SOUTHEAST ELEVATION
301 =
. y SCALE: 3/32..'.-0. .....
-
I
FINAL PROPOSED ELEVATIONS
I
I-
I
I
I
I
j
I
I
I
I
L_______
I
r--------
I
_J
I i
I
L_________________J
I
___....-J
NORTHWEST ELEVATION
Q
SCAlE: 3/32"."-0.
SOUTHEAST ELEVATION
0)
~ SCAlE: 3/32"."-0.
.L.-. . I
I I
I I
I I
I I
I
I I
L________________~___J
I HEREBY CERTFY ~T THIS PlAN, SPECIfICATION OR REPORT WAS PREPARED
BY W( OR UNDER lIY DIRECT SUPERVISION. AND 1W.T lIMA DUlY I...ICENSED
ARCHITECT UNDER THE lAWS OF THE STATE Of MINNESOTA. (ARCHITECTURAL ONLY)
"" SEPTEWBER 28, 2008
~0lIl1WI(: DAVID J. WEDIN
FIB. NO. 9898
ARCH. PROJ #: 2850
11 architects plus
203 nw first ave.
farlbault, minn.
507/J34.Z2S1 55021
SlI7i334"3SOFA.X
IiiiIC>L. -n::>N 8- ...........N K., INC:
~ CONSULTING ENGINEERS & SURVEYORS
tr.lANKA TO, t.lN f AIRt.lONT, loiN BURNSV1ill. JoIN SlEEPY EYE, "'N
'MlUlAR, l.lN OiASKA, '-IN RAMSEY, MN AMES, 1.1.
o TolH
8-28-06
PRIOR LAKE. MINNESOTA
WATER TREATJ.IENT FACIUTY
EXTERIOR ELEVATIONS
SHEET
3.01
I
-~
j-
NORTHEAST ELEVATION
o
~ SCAlE: 3/32--1'-0-
i
!
l__~
SOUTHWEST ELEVATION
0)
~ SCAlE: 3/32--1'-0-
"" SU'TEllBER 28, 2006
:mOIl N.fM:: DAV10 J. MEDIN
It(C,. NO. 9898
ARCH. PAOJ. #: 2850
11 architects plus
203 nw first ave.
farlbault, mlnn.
507!J34.2251 55021
SOTIJ34-8J50 FAX
IiiICL.. "T"ON 8- ........Iiiiii:N K, INC
~ CONSUL TING ENGINEERS & SURVEYORS
"""NKAro. WN FAlRJr,lONT, UN BURNSVIl1.E. UN SlEEPY m, lotH
'MllMAR. MN CHASl<A, MN RAMSEY, WN AMES, IA
o
TJII
11-_
PRIOR LAKE. MINNESOTA
WATER TREATMENT FACILITY
EXTERIOR ElEVATIONS
SHEET
I HEREBY CERTIfY THAT TI11S PI.AA, SPEClflCATlON OR REPORT WAS PREPARfD
BY WE OR UNDER IN DIRECT SUPERVISION. AND THt.T I AM A DULY UCENSEO
AACHITECT UNDER THE LAWS or THE STArr or WINNESOTA. (ARCHITECTURAl. ONLY)
3.02
FINAL PROPOSED COMPUTER GENERATED
GRAPHICS
North View
~\..
--
/
I.
/
West View
Southwest View
=::F
APPENDIX C
PRELIMINARY LANDSCAPING PLAN
-L-
6
L
7
8
11
13
9
14
15
12
10
;-4
,.
I. ~ :1
~
'" ',;9 ~',
.ANDSCAPIt.<C . _ _
-~"~
, I
* 0, ~--
D.
-1>.
'~;~~:C, O.
'-.
-, ---- -;Ja CliP
.J
.p~
\- ~.-=
;''C _ --:..-
'--
::. 'C'-"-*_*-,
~
-30- ~p _
, '~3c--;-C~p
;
~~--p--
- , -'
'---~2" R:P
-~, - !
/-'
-.:\e~
IIOOOED AP.tA
.''')
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:"l"! 10 OCT, 2006
15137
key:
:-:',-:,::y~.sp'1 _~:-'1./J',~)'''::::: t-,
landscape plan
scale:
1" to 30'-0"
>:':'(,:'0';'.:1 '" _ "
:>F
!'E--:;
~
o 30'"
PR:OR LAKE, MINNESOTA
WATER TREATMENT FACILITIES
5 10'
~
s~rr-
APPENDIX D
TREE SURVEY RESULTS
Tree List, Prior Lake Water Treatment Facility
__.I!~~_tt._ Tree Spe.~!~~~ DBH
1 Boxelder 7.0
_,m "____.___~___ __~_~
2 Boxelder 7.5 6 No
1--. --'..---- -=:c-____uu__u_ ~_,u__..__ __"u_ ..,_..u...u.., .uu_, __"__'_ _,___ ___ u~,____.,_
3 Elm, American 6.0 4 No
-.-........-.---.-. ------------ ------ -~-~_._._----- -,--.-'."---"--' ...- -~---_.__._~--- .-.-'..--.
4 Boxelder 12.0 4 No
_ , .,...._.'_.'__' .u __u,_..u .__,..._ ,.,..___ _.__ ._..u,__...".u... _ _._uu..,. _.. ,. .,~u~___~_
5 Elm, American 6.5 4 No
__'_"_ =____.,......,_.,_'_,.., ___,____,~____..,....___, .,_ _'u., ."..._u.. .....,.. .,_u..,_ ,., "u...,_.~~
6 Elm, American 6.0 4 No
c"'u . _u.... __ ----'-__,_ ..u__ ,_ _..,___'___ __,.__ .,_. _uu..u..,._ ,. ..,..._,~_.__.._ ,....,.......__. __.. _,___
7 Boxelder 19.5 2 No
,,__ ______.__ u~-'---__c_ _u___...._ _u__.___+________
8 Boxelder 14.5 4 No
9 Boxelder 6.5 2 No
10 Elm, American 6.5 2 No
_u
11 Boxelder 20.5 3 No
12 Boxelder 15.5 2 No
13 Elm, American 6.5 4 No
14 Boxelder 12.0 2 No
..
15 Boxelder 15.0 2 No
-'
16 Boxelder 10.0 2 No
17 Boxelder 8.5 2 No
18 Boxelder 16.0 2 No
19 Boxelder 18.0 3 No
20 Boxelder 17.5 3 No
21 Boxelder 8.0 5 No
22 Boxelder 8.0 4 No
23 Boxelder 7.5 4 No
24 Boxelder 7.5 2 No
25 Boxelder 9.5 6 2 No
26 Cherry, black 11.5 4 No
27 Boxelder 10.0 2 No
--
28 Boxelder 6.0 4 No
29 Boxelder 12.0 4 No
30 Boxelder 11.0 4 No
31 Cherry, black 15.5 4 No
32 Boxelder 8.0 2 2 No
'-,-c--
33 Boxelder 7.0 6 No
34 Boxelder 12.0 4 No
35 Boxelder 13.5 2 No
------------
__.36 lAsh, green..,-t 10.5 8 Yes
....- ;F~~::~:~ +-1i% ~---4 _..___u____, ~~
39 Boxelder 8.0 2 2 No
-.
40 Boxelder 8.0 2 No
41 Maple, silver 20.0 4 3 Yes
42 Boxelder 9.0 4 No
.-
43 Oak, red 29.5 6 Yes
44 Boxelder 9.0 4 No
.u.,.._~_
:~=-~;~:~:: u_ 1 ;~' -- -1 - ~~ ..-
r--u--u- _._,___ _,..____~_'u,. .. .. .,., _..".._.__~ __.__
48 Cottonwood 28.5 6. No
. ..--..____' "_U'__ U'_"__~ C-' ________.m_+~'__._ ,~_., ,_..___.,_...._____
.__ 49 Elm, American___u ,. ~ 7.0 -n~-----~f __ ~__No_......
50 Elm, American 6.0 4: No
----s1".--' Boxelder 7.0 31 No
Condition
,..__u_
4
Stems Height Significant
__~U
No
_._-~-~,.- -,..,.._--
_.
--
--
Kunde Co., Inc.
RECEIVED
OCT 2 0 2006
BOLTON & MENK, INC
BURN~VILLE, MN
.
i
1 of 6
Tree #
1----
52
~-~~-'.,~ .
53
- ..--. --~---~._.- ..----.-
54
._--~~----
55
~---~
56
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
74
75
76
77
78
79
80
81
82
83
84
85
86
87
88
89
90
91
92
-~--,
93
94
--
95
96
97
---,
98
___,
99
100
-------- ---
101
102
---
Kunde Co., Inc.
Tree Species
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Elm, American
Boxelder
Elm, American
Boxelder
Elm, American
Boxelder
Elm, American
Boxelder
Boxelder
Elm, American
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Boxelder
Elm, American
Elm, Siberian
Elm, American
Ash, green
Elm, American
Cherry, black
Elm, Siberian
Cherry, black
Cottonwood
Boxelder
Cherry, black
Elm, Siberian
Cherry, black
Cherry, black
Boxelder
Elm, Siberian
Boxelder
Boxelder
Elm, American
Cherry, black
Boxelder
Elm, Siberian
Boxelder
Elm, Siberian
Boxelder
Tree List, Prior lake Water Treatment Facility
DBH Condition Stems Height
--1--
17.5 2
--- ------ -, ~---"- -,-,-----, ~-, ,-J-'---------, ~---" - ,
8.0 4
_... _.______ _~_,_ '__'.__ '_'_m _+______,____.., __,___
10.0 2
-, .--- --- -,.--....- -- .,-f---------'J-',.....---,... ---
8.0 4
onn,__ _ _______.____ ___.._ ,.._..._
10.5 4
__,___.__,_.____. .._._.__ _.._m_'.____ ~_ _.._____ ..___,_______
6.5 4 >--_
8.0 6
---!---- --------~!----
7.5 4
--1-----
6.5 4
6.5 4
7.0 4
7.0 5
13.0 2
16.0 6
7.0 4
7.5 6
7.5 5
9.5 4
8.0 4
8.5 4
6.5 6
7.5 4
11.0 4
6.5 4
6.5 4
6.0 4
7.0 4
8.0 4
7.0 4
8.5 8
9.0 4
13.5 4
19.0 4
8.5 5
16.5 4
8.5 4
7.0 6
7.0 2
16.0 5
8.0 4
6.0 4
7.5 4
6.5 4
8.0 4
8.0 4
8.5 6
9.0 4
15.0 4
.---I---....-----f----
11.5 4 2
__~_,.._,_,__I------ on_'
6.0 4,
--- -.-- 13.5 ---41
__ _n __
--
2
2
2
2
2
2
2
.,---
.-
2
3
Significant
No
____on_
No
No
"-'--'-~-~~
No
--~-_.~
No
No
----
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
Yes
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
No
-'-~-
No
No
No
2of6
Tree List, Prior lake Water Treatment Facility
Tree # Tree Species DBH Condition Stems Height Significant
~----~.. ~~ - '~--
103 Elm, Siberian 9.0 4 No
r---'~ n._._._ ._--,. ------~-_._--- -----~---- ~~--~._--- _.~--~--
104 Boxelder 11.0 4 No
- --- ----- ------~----..- _,.__u~ _~.__....__ ------- ~--- ---.----.-.---.-----
105 Elm, American 7.5 4 No
-, ' "- - .-.-.....--.-.- u .__..___,_ --------- ___u_,
106 Elm, American 6.0 6 No
-------- --
107 Boxelder 8.0 4 No
----- -, --,-- ., "'-::C ------ - ---- - - . ----...--- ---- ----,---,' ~-'-----"--'--
108 Boxelder 7.0 6 No
..-- ------
109 Boxelder 8.0 4 No
110 Elm, American 9.0 4 No
-4 --
111 Boxelder 7.0 2 No
112 Elm, American 8.0 4 No
113 Boxelder 9.0 4 2 No
114 Elm, American 6.0 6 No
115 Cherry, black 7.0 4 No
116 Boxelder 8.5 4 No
117 Elm, American 8.0 4 No
118 Elm, American 7.0 6 No
119 Elm, American 7.0 4 No
120 Elm, American 8.0 7 No
121 Elm, American 6.5 5 No
122 Elm, American 6.0 4 No
123 Elm, American 7.0 4 No
124 Elm, American 9.5 4 No
125 Elm, Siberian 9.5 2 No
126 Boxelder 9.0 4 2 No
127 Elm, American 6.0 6 No
128 Elm, American 6.0 6 No
129 Boxelder 6.0 4 No
130 Boxelder 10.0 4 2 No
131 Boxelder 10.0 4 No
132 Boxelder 10.5 4 2 No
133 Boxelder 12.0 4 2 No
134 Elm, American 8.5 4 No
135 Boxelder 8.5 4 No
136 Boxelder 6.5 4 No
137 Elm, American 6.0 6 No
138 Boxelder 7.0 3 2 No
139 Boxelder 7.0 4 No
140 Boxelder 9.0 4 2 No
_.----- -
141 Boxelder 9.0 4 No
142 Boxelder 8.0 4 No
143 Boxelder 6.5 4 No
144 Boxelder 7.5 4 No
--
145 Elm, American 7.5 4 No
- --
146 Boxelder 8.0 4 No
____u ------.--_.-
147 Boxelder 8.5 4 No
,-,'---
148 Boxelder 9.0 4 No
----.- --, ~,
149 Boxelder 8.0 4 No
150 Boxelder 9.5 4 No
--.-..---
151 Boxelder 7.0 4 No
---. -- -,--
152 Elm, American 7.0 4 I No
---------._----
153 Boxelder 7.0 4 No
Kunde Co., Inc.
3of6
Tree List, Prior lake Water Treatment Facility
Tree # _ Tree Spe~ie~ DBH Condition Stems Height Significant
~"---- u, ,-, -- -- -'-c--::- ----'-----"---,-- _u__'_'__---=- -~-
154 Boxelder 15.0 4 2 No
---------~-- _._-----_..._~- -- m ----,-.-- ------
155 Elm, American 6.5 4 No
. ..- -.---------.-- --..--- ------- .____.__n _.__..____._.__.__.._ ___._.0_________.._._...__ ---.,---..- ,---- .-----.
156 Boxelder 8.0 4 No
------....---.--- --------'----- _m__ ._" "-'. ._-.. ....---....---- ----- ~-..- .._'.-----
157 Boxelder 11.0 4 No
-- ---_._~ -- -- -- ---- ---.
158 Boxelder 8.5 4 No
r----- ---- ,._--'-----'~ __..__..u._._.____ --~--_._.__._~-_._---..- --- _..__.----~-
159 Elm, American 6.0 6 No
f-_. -.--- c-,.__,__ --------,--" --- -----..-, n____ ----- -,--
160 Boxelder 8.0 2 No
-- --
161 Boxelder 10.0 4 No
162 Boxelder --- -- 6.0 -4' -- No
163 Boxelder 12.0 4 2 No
164 Elm, American 6.0 4 No
------ .-...---- -------- --~--- ---,.,-----,- -~--
165 Elm, American 7.0 4 No
---- ---- -
166 Boxelder 10.5 4 No
167 Boxelder 13.5 4 2 No
168 Elm, American 8.0 6 No
169 Boxelder 7.0 4 No
170 Boxelder 14.0 4 3 No
171 Boxelder 6.5 4 No
172 Elm, red 7.0 4 No
173 Boxelder 9.0 4 2 No
174 Cottonwood 15.5 6 No
175 Cottonwood 16.0 6 No
176 Redcedar, eastern 3.0 6 14 Yes
177 Elm, Siberian 9.5 4 2 No
178 Cottonwood 16.0 6 No
179 Boxelder 14.0 2 2 No
180 Cottonwood 12.5 4 No
181 Elm, Siberian 11.5 4 No
182 Elm, American 9.5 5 No
183 Boxelder 8.0 4 No
184 Boxelder 6.0 4 No
185 Boxelder 11.5 4 No
186 Elm, Siberian 11.5 4 No
187 Boxelder 6.0 4 No
188 Boxelder 11.0 4 2 No
189 Boxelder 9.5 4 No
190 Boxelder 6.5 4 No
-,
191 Boxelder 10.0 4 No
192 Boxelder 9.5 4 No
-- 4 No
193 Boxelder 20.0 5
194 Boxelder 13.5 4 3 No
195 Boxelder 6.5 4 No
196 Elm, American 6.5 4 No
197 Willow 15.0 5 2 No
".- No
198 Willow__~i__ ~ 6
-~,-- -
199 Willow 8.5 4 No
-- -,- -.._-- ------
200 Willow 21.0 6 No
______...n..__'.__ ------
201 Cottonwood 29.0 5 No
--~.-_._----------_-.- -- ---_.--~ _ --.---- ---
202 Elm, American 6.5 4 No
------ - ~----- ----- ---
203 Elm, American 7.0 4 No
_____.n ---.---- -- -------...-
204 Elm, American 6.5 4 No
Kunde Co., Inc.
40f6
Tree List, Prior Lake Water Treatment Facility
Tree # Tree Specie~s. _ DBH Condition Stems Height _~ignificant
..__._._---_..._-~- ----~_... ---- _.._--~- ---
205 Willow 9.0 4 No
~------ ---._--. --..- -..- ------ __~.m.___... '..' _ --- ----------.--. ---~....__..- -----,._--
206 Willow 9.5 4 No
--~- - - -'-' -.... ---~-- -----.---.-. - -- __ __ ___ ___n___un --- 0.. ____ ___._~_._ ~-~-~--
207 Boxelder 9.5 4 No
-----. ___ __u_ __ .., ._.~--- __.____.n__'_."'__ _.____.. ',_____ ____u_ -,- -- _.-_._-----.._~.._.- --,~--,-
208 Cottonwood 15.0 6 No
-----."- ---- - ---P-.- _._.'._n__ -- ---_..__.~,......_- , ----- ~----- ------
209 Elm, Siberian 6.5 4 No
----- e.--' .._,~.._-- c--'--'- ---- ---
210 Cottonwood 24.0 6 No
--------
211 Cottonwood 23.5 4 No
212 Cottonwood 30.0 4 3 No
213 Cottonwood 16.0 4 No
214 Elm, American 7.0 4 No
215 Elm, Siberian 14.0 4 No
216 Boxelder 6.0 4 No
217 Boxelder 6.5 2 No
218 Boxelder 6.0 4 No
219 Cottonwood 33.0 4 No
---.
220 Elm, American 6.0 4 No
221 Elm, Siberian 8.0 4 No
222 Cottonwood 16.0 6 No
223 Elm, American 6.5 4 No
224 Elm, American 8.0 4 No
225 Cottonwood 11.0 4 No
226 Cottonwood 17.0 6 No
227 Cottonwood 12.0 6 No
228 Elm, American 6.0 4 No
229 Elm, American 6.0 4 No
230 Cottonwood 19.0 6 No
231 Cottonwood 47.0 4 3 No
232 Elm, American 8.5 4 No
233 Boxelder 15.0 2 2 No
234 Boxelder 10.0 4 No
235 Boxelder 8.0 4 No
236 Boxelder 14.5 4 No
237 Boxelder 10.0 4 No
238 Boxelder 8.0 2 No
239 Boxelder 6.0 4 No
240 Boxelder 17.5 4 2 No
241 Boxelder 8.5 4 No
242 Boxelder 7.0 4 No
243 Boxelder 10.5 4 No
244 Boxelder 7.5 4 No
245 Boxelder 6.0 4 No
246 Boxelder 8.5 4 No
247 Boxelder 12.5 4 No
--------------- -- -- ."-'-- No
248 Boxelder 6.5 4
"._---.-- ~..-. _..__.~ --
249 Boxelder 12.5 4 No
.--.
250 Boxelder 12.0 4 No
..-
251 Boxelder 6.5 4 No
-... ----....----------.-- ~..- -------
252 Boxelder 8.5 4 No
-.-------
253 Boxelder 11.5 4 No
m~' --4 --~- ,~-- f-~
254 Boxelder 8.0 No
--.--.--- ~--, --...,
255 Boxelder 12.0 4 No
Kunde Co., Inc.
5of6
Tree List, Prior lake Water Treatment Facility
Tree # Tree Species DBH Condition Stems Height Significant
~_. f--
256 Boxelder 6.5 4 No
-- -- --~---- '--'-----,--,- ----------,- --~._--~ f-------, ~--'----
257 Boxelder 10,0 4 No
------.--,--.---- -. ..--...., -----.-- ,-------- --- 1-----, -- --------- - ..~ --_.__.---_. ----_._---~
258 Boxelder 9.5 4 No
--------, - "..------ --_._----~.._-_..~- ~.._.---~- ----- -------
259 Boxelder 12.0 4 No
--,.--.-. -----.. .u__..____.__~__ -- -- - ----.-------- 1-----
260 Boxelder 16.0 3 2 No
__~_____..____. _u_ -, ..--- -~--~-- _n_.______ ~-~_._-
261 Boxelder 18.0 4 2 No
--- ----- --
262 Boxelder 9.5 2 No
Total Number of Significant Trees = 5 (#36,41 ,43,81 & 176)
1. DBH is diameter of tree measured at 4.5' above ground
level.
2. Condition is rated on scale of 0-10 with 0 being a dead
tree and 10 a perfect tree.
3. Trees tagged with round, aluminum, numbered tag.
4. Significant Trees shown in bold above.
k/ ,.I.~ /lJ//8!Ch
/V ?-~.
Stephen 1. ~icholson Date
Certified Forester #2369
2489 Rice St. #160
Kunde Co., Inc. Roseville, MN 55113
651-484-0114
www.kundeco.com
Kunde Co., Inc.
60f6
APPENDIX E
EQUIPMENT DATA SHEETS
I. Aerators
2. Underdrain System
3. High Service Pumps
4. Submersible Pumps
5. Valves
6. Air Compressor
7. Air Wash Blower
8. Kalwall Panels
9. Example of PC Screens for Water Treatment System
10. Chemical Feed System
Aerators
'll" ~r,. ,
-"..
--....
-.
I
..
I -.: ~
r-~~]~!
I
i
'C..!t!,r~
':p
i ..
-:-
.4
f,:
'&
-!' .....--------=
',=-~'
,.:' -:-
~~.-
.--
~
......
.... ;;,
--
1
:1>'
'~
AERATION is EFFECTIVE
AND INEXPENSiVE
4.75 MCDAerator Installat;on
AERATOR
SPECIALISTS
2
PROVEN PERFORMANCE SINCE 1935
USFilter's General Filter products and processes have effectively treated water supplies
since 1935. USFilter has been a leader in the design and development o/many 0/
today's accepted designs. Our first product was the Atomerator>' system, a pressure
Aerator. Ever since, we have been at the forefront as Aerators have evolved from red-
wood to steel to fiberglass to maintenance-free aluminum construction.
Induced draft aeration IS an effective,
inexpensive and low-maintenance method
of improving finished water quality in a
large number of applications. Generally
used at the head of a water treatment
plant facility, these units efficiently help
remove unwanted water components and
help stabilize the pH of corrosive waters
for a large range of flows.
The most common aerator application
introduces air and water for intimate
contact in counter-current flows to pro-
mote the oxidation of unwanted iron and
manganese. Air is induced up through
the aerator chamber, while the water is
Our specialists apply Aerators on a daily
basis to a broad range of applications.
From positive draft to natural draft to
pressure Aerators, they know which to
apply when, and for which conditions.
Our Aerator specialists have dependable,
proven answers because of the
Company's experience with aeration. No
one knows aeration like USFilter.
introduced at the top of the unit to
free-fall through the aerator internals.
The upflowing air sweeps through the
falling water to increase the oxygen
content of the water, removing unwanted
dissolved gases such as carbon dioxide
and hydrogen sulfide. Dissolved solids
such as Hon and manganese are
transformed to their oxidized states,
enabling them to be removed by down-
stream clarification and filtration equipment.
In addition, the aeration process can
remove objectionable tastes and odors
and reduce the chemical requirements in
lime softening.
Alum;num Induced Draft Aerator
General Filter Aerators have proven their value in thousands o/installations.
Our experience includes:
INSTALLED
EXPERIENCE
. Iron and Manganese Oxidation
. Oxygen Addition
. Carbon Dioxide Removal
. Hydrogen Sulfide Removal
. Volatile organic compound removal,
including Trichloroethylene (TCE),
Tetrachloroethylene (PCE), Trihalo-
methane (THM), and Chloroform
. Methane Removal
. Radon Removal
AERATOR BENEFITS
. Experience since 1935 - Proven,
results-oriented Aerator performance.
. Thousands of applications - Thorough
knowledge of most water conditions.
. Aluminum construction - Corrosion-
resistant units are maintenance-free
and retain their like-new appearance.
. Replacement parts availability-
Aerators won't become obsolete.
. Working model - Helps match right
Aerator to application.
PILOT PLANT
TESTING
A pilot plant can be easily and economically
installed at a specific location to fine-
rune Aerator design.
Especially useful for evaluating
Aerator performance factors for special
applications, it may also be used to veri-
fy the conclusions of a predictive model.
Forced Dmft Aerators fOr VOC Removal
-
*j
.
:;}Ni..~ Jr:;. - ~
.1 ..
'~: j
. Complete range of Aerators - Cost-
effectively fits the application needs.
. Proven Aerator designs - Assure
structural integrity and performance.
. Factory assembled - Minimizes instal-
lation costs, prevents errors in the field.
. Low headloss distributor tray -
Reduced pumping cost.
. Pilot units - For evaluation of
oxidizing and degasifying performance
of full scale units.
Aeration, Detention and
Filtration Pilot Plallt
Aerator Pilot Plallt
3
AERATOR
OPERATIONS
I~
I
n ~ n
I I I I
d h I. ~
~ hi
I , V-
~ , -I
~ . ,
rl I 1 "
., I " ,~
I r H H I
, V- n V- hi
hi hi , I
L
i /-~ \}
Induced Draft Aerlltor with PVC Slllt
bltemllLs
DISTRIBUTOR TRAY
4
Aluminum Distributor TrllY
EFFECTIVE, EFFICIENT AERATION
No other positive draft Aerator is as maintenance-free as the General Filter Aerator.
Reliability, convenience and economy are engineered into every Aerator. Common
features o/every induced draft Aerator include:
. Exceptionally high-quality induction
blower, constructed of aluminum and
stainless steel, is corrosion-resistant
and maintenance-free. It mounts atop
the Aerator housing, saving space.
. Aluminum is used to provide low
maintenance and corrosion resistance
for long life.
. Gravity distribution of water reduces
long-term pumping costs and
eliminates troublesome spray distribution
nozzles.
. Special contour of round PVC slats
supported on stainless steel reduces
clogging. Slats can easily be removed
for cleaning.
. Induced draft design is the most
common. Forced draft is also available
for specific applications.
The distributor tray assures dispersed
water reaches every corner of the Aerator.
Incoming water enters at atmospheric
pressure and is released through a velocity
breaker. Then, gravity target nozzles
evenly distribute the water over the
Aerator's cross section.
The aluminum distributor tray IS
The General Filter standard positive
draft Aerator uses an induced draft
design to minimize O&M costs.
Water is first distributed by gravity
across the area of the Aerator by a
disrributor tray, which then disperses the
water into droplets. As the droplets fall
through a series of trays or media, they
divide and regroup repeatedly, exposing
more surfaces to the air.
A counter-current flow of air continuously
sweeps upward through the water droplets,
absorbing and carrying away released gases
and supplying oxygen for oxidation.
The air is drawn through inlet ports at
the base of rhe Aerator, is discharged
rhrough internal air sracks into rhe
moisture separator, and expelled by a
blower on top of the housing.
corrosion-resisrant. Aluminum an
exhaust stacks in rhe tray provide uniform
collecrion of rhe upward flow of air.
The bell mouthed entrances of the
plasric disrribution rarger nozzles minimize
clogging. Integral targer distriburors
provide even warer dropler disrriburion
in rhe aerarion zone.
.., --
___u'
n
"ii'oo"" t-j ilI-.-' ._.. .~,.,,:..," I
......."'...;, "'. "... ~ I ~ .. . . . .. I' .. r I' "t' .r. "".. ~ oJ..
~"',",,""'\- ~~ .~~..~~.~...........
....,M.,J.........~...... .. f ..,.j. ~ ~ "
___'M,," >. I... .. _ ._
.......-...-..__c... .. .' _...... .,..
-~..,...',. ...-....
._--,.."...~,... ~ .. .. .....-.-
____.... '-"" " . '~" ~"''I'",.,....
,.~.'~"T'''''''.'''~' \' ................
""r.',' ,.._, '.' .. .-. .,...., ",'
:1
..
i .......
Aerator with EZ Clean stats
HOUSING
BLOWER MOTOR
Maintenance-Free Blower Motor
,.
J
Round EZ clean slats continually break
up water droplets. The EZ clean slats can
be individually removed for periodic
cleaning, unlike mesh or redwood trays
which require replacement.
These efficient, round PVC slats are
The corrosion-resistant, all-aluminum
housing is a chamber for the counter-
current flow of water and air. Standard
housings are available for capacities
ranging from 40 to 5,000 gpm. Larger
custom sizes are also available.
A hinged and bolted removable side
is furnished for internal access. All
General Filter Aerators have a media
inspection port.
Inlet and exhaust alf ducts are
screened and baffled to prevent water loss
An induced draft blower of exceptional
quality virtually eliminates the need to
access the only moving mechanical part
of an Aerator.
It is designed to run maintenance-free
for long, reliable service.
The housing IS aluminum for
complete corrosIOn resistance. The
blades are cast aluminum and balanced
for smooth operation. Sealed bearings
designed to handle high loadings and
minimize plugging. Slats are spaced
vertically, either 2, 4, or 6 inches apart,
depending upon performance require-
ments. These slats can easily be
retrofitted to existing units.
or debris entrance. The moisture
separator at the top provides three
changes
direction
for
In
air
minimal moisture carryover.
A collector pan normally is furnished as
a base for the housing, or it may be built
with an open bottom for mounting on a
steel, aluminum or concrete retention
tank.
The aluminum construction permits
the Aerator to retain its like-new
appearance for the life of the installation.
and the motor shaft are wear-resistant
stainless steel. An aluminum vent line
between the motor frame and enclosure
relieves condensation accumulation.
Every induced draft blower is factory
tested to ensure quality performance.
No other blower is as dependable,
durable or maintenance-free.
5
QUALITY IS BUILT INTO EVERY AERATOR
A review of our Aerators shows the quality and added value. All seams in the housing
are internally welded with a fillet the same size as the plates to be welded. A dye
penetrant is put on each weld, assuring watertight construction.
Slats are cut to length and custom-fit to
the housing. The blower is operated
before it leaves the shop floor as a final
quality check.
All General Filter Aerators are
completely factory assembled and
thoroughly inspected, ensunng proper
fit-up, thus simplifying field installation.
Aerator tvlaterials
Housing Aluminum Stainless Steel
Distributor Tray Aluminum Stainless Steel
Media PVC Loose Fill
Blowet Induced Draft, Forced Draft,
Permanently Sealed Explosion- Proof
Design Shape Square Round
Rectangular
For most applications, standard con-
struction features are suitable. Certain
applications may call for other materials.
Consult US Filter for additional options.
I
...~: . .._,~ ,. ., -,' ':/~~'~.:",..
,~_"~" _ _ __~l
=.r,---
Partially Assembled Aerator
6
Round Forced Draft Aerator
COMBINATION UNITS
PRESSURE AERATORS
Atomerator with PresStlre Filters
COKE TRAY AERATORS
CASCADE AERATORS
General Pilters AERALATE~ designs can do a number ofjobs such as removing radon
while removmg Iron. lJpically, the AERALATER units aerate the water
supply, provide detention time and then filter to provide effective Iron,
manganese and arsenic removal. The AERALATER system is also selfbackwashing.
Other integral, combination units
provide aeration/degasification, chemical
feed through a static mixer and then
retention time for the chemical reaction
to occur.
For information on a specific need,
contact USFilter or your local sales
representative for details on the complete
line of engineered package units.
The compact and economical General Filter
Atomerator system was first introduced to the
market in 1935, and its reliability is assured.
Compressed air is diffused into the
pressurized water stream ahead of the
pressure filter to oxidize ferrous iron.
General Filter coke tray natural draft
Aerators are used to a limited extent for
oxidation of iron and manganese. These
units contribute to the reduction of odors
and other dissolved gases, but are not as
efficient as positive draft Aerators.
A distribution tray equipped with
orifices evenly spreads the incoming water
Aluminum cascade Aerators are a cost-
effective method of aerating. Corrosion-
resistant construction and absence of
moving parts provides for a maintenance-
free installation. Typical uses include iron
oxidation and wastewater aeration.
, ..' 4 ~';':
Combination Unit jor NIethane and Iron Removal
Excess air is released to the atmosphere at
the top of the filter.
The Atomerator system can eliminate
double pumping in applications where the
pH is above 6.9, and organic iron or
dissolved gases are not a treatment problem.
over the top of successive tiers of redwood
slats, non-corrosive screens or coke. Splash
skirts reduce water drift loss and potential
lcmg.
A protective housing may be provided
separately or as an integral part of the Aerator.
7
Aluminum Cascade Aerator
PUT OUR EXPERIENCE TO WORK
Our design database includes thousands of Aerator installations. From this database, a
working model has been developed that helps determine the right size Aerator to
achieve the required level of perfOrmance. A predictive model for stripping of gases or
volatile organic compounds has been developed. we look forward to working with you
on your next project. Please contact your local sales representative to have your
application reviewed.
Other Water Treatment Products
!fits in the water, our engineered processes and equipment can take it out, economically
and dependably. Our comprehensive line includes solutions to simple and complex water
treatment and conditioning needs, all backed by working installations and years of
experience. Our line includes:
. GFH'" arsenic removal systems
. ACTIFLOC''' packaged water systems
. CONTRAFLO'" solids contact clarifiers
. SPIRACONE'" sludge blanket clarifiers
. Sludge Sucker'" sludge removal system
. Sludge thickeners
. Vertical and horizontal pressure filters
. CenTROL'" gravity fIIrers
. AERALATER'" packaged treatment
Horizontal pressure jilters
Trident Trimite'" package water plallts
. Microfloc" Trident" packaged surface
water treatment plants
To find out more about how [0 put
USFilter [0 work for you,
contact us at
. MULTIWASH" Filtration Process
u.~----
- =-=----
-------
i!J!J!S~5
. Gravity filtration equipment
. Memcor'" CMF microfilrrarion system
. MULTICRETE II''' monolithic under.
drain system
Memcor, Microfloc, and
General Filter Products
600 Arrasmith Trail
Ames, IA 50010
515.232.4 1 2 1 phone
515.232.2571 fizx
. MULTIBLOCK" underdrain
. ESSD'" filter washtroughs and launder
systems
441 Main Street
P.O. Box 36
Sturbridge, MA 01566
508.347.7344 phone
508.347.7049 fizx
~~,
..... ~.'.'-. '.1.. ".
1',' Ill'~
~.-:..'.'..'...'.'.".."";"...:"'..'.~. ..' .1J4........_~Ji ~'., }......._......I
.. t.. . .,:- . !....-.
--- ":l ':;:;...;---1"_1/ ~
.)~. ,...,;
;: :
.. j . . ..'~.jj
725 Wooten Road
Colorado Springs, CO 80915
71 9.570.9600 phone
719.597.3782 fizx
CONTRAFLO' clarifiers
1 104 Kenilworrh Drive
Fifth Floor
Towson, MD 21204
410.307.6540 phone
410.307.6542 fizx
For more information,
visit our web site at
www.usfilter.com
rD 2002 USFiltcr
Memcoro:. microjiltration systems
a viVENDI
USFilrer reserves the right to change the specificarions referred to in this literature at any time, without
prior notice. CONTRAFLO,''' Trident Trimite, "'and Memcor" are trademarks of Unired States Filter
Corporation or its affiliates,
GF-AER-BR-0702
Environnement company
IB-B STAJNLESS
STEEL BLOWER
MOUNTING HARDWARE
@:8
f2o\
~ TWO AlUMINUM AND STAINLESS
STEEL BLOWERS TO DEVELOP 10BOO
SCFM AT 3/B' STATIC PRESSURE.
460 VOLT. 1750 RPU. 60 HZ., 3
PHASE SEE DRAWING 1612714101
ALU...,NU'" "'OISTURE SEPARATOR
ALUMINU'" VELOCITY BREAKER
6" DIAMETER AlUMINUM
AIR STACKS
FIXED DISTRIBUTOR BOX
W'TH TAJRGET NOZZLES
NSF APPROVED 1 1/4- SDR-21 PVC
PIPE INTERNAlS SUPPORTED ON 2-
TYPE 304 STAJNLESS STEEL GRIDS
WITH 6'" YERTICAL CENTER SPACING
13" X IS" SIDE
INSPECTION PORT
24' FLANGED EFFlUENT
PIPE WITH 125/150' DRILL
sm, BORDER-1101-22X340
~z
12'.0'
SOUARE
INSIDE
PLAN
FRONT ELEVATION
REMOVABLE SIDE NOT SHOWN
INTL REF, 1611214001
16- flANGED INFLUENT PIPE WITH
125/1501 DRIlliNG
1\' THICK COVER
1 B- DIAMETER INSPECTION PORT
r THICK SHELL
j' THICK HiNGED ~ BOLTED
REMOVABLE SlDE WITH
3/B- I 6NC2 X ,- STAINLESS
STEEL BOLTS ON 6 - CENTERS
10'-0' 12'-ei'"
11'-9"
11'-3)'
SHELL STIFFENER
ANGLES
@
AlU""NUM INDUCED
DRAFT AERATOR
I" DlA"'ETER HOLES FOR
ANCHOR BOLTS. SEE
AERATOR FOOT LAYOUT
BAR = 1 - AT PLOT SCALE
REV
ALL INr:uR,,"no~ CONTAINED ON THIS DOCUlolENT DESIGNER DATE
~~J~R~~~.OFTH~ED~~~~'b~f~RJ.N~ FJT 9-23-04
INFOR.....TlQN CONTAINED HEREIN ARE PRQPRlETAAY
TO USfC ANO A.Il[ SVBWrTTfJ) IN COHf1DENC(. 1'};(y CHECKER DATE
ARE NOT TRAHSfERABU AI-lD lolusr BE USED ONLY
f'"Ofl. THE PVRPOS[ FOR WHICH THE DOClJl.fENT IS
OPRBSlY SUBIMTlED. lHE'f wsr NOT BE OIStlosm,
REPROOUCEO, LCl.'.NED OR USED IN ANY OTHER
MANNER wrTHOVT niE D:PRESS W!'lt1T[N CONSENT
OF VSF. UST ASSlJ\lES hlO RESPONSIIllJTT' OR l.IIBI..m'
FUR THE: USE OF THIS 00CU/0ID'0It OR T)lE OESICN
CONCEPTS AND INFORMATlO'" CONTAINED HEREIN
FOR .-.NOTHER PROJ(ct, OR IN A loWiNER ~T DOES
NOT RElATE TO THE F1TNESS OR PURPOSE Of THIS
DOCINENT. JH NO EVOfT Sl-W.l. THIS OOCVWEHT OR ~
:S~~~~AL~~~ flLE:
Of VSf. All J>ATOO RK;HTS ARE RESOMD. AC:CEPTAHCE:
~R~~~gr~ES~~~ gg=~ SCALE' 1/2" := l'-O~
4
n"-3l'
,.-.P?
~
I
,
I
,
I
,
I
,
I
,
I
----- - - -- -- ---+---- --- - - - -- --
I
,
I
,
I
,
I
,
I
,
I
I
~
I
5' -9" TYP
6' .ol' TYP
AERATOR FOOT LAYOUT
SCALE
SIDE ELEVATION
DESCRIPTION
DATE
OWN
CHKD AP'VO
EeN
OPERATING WEIGHT:
~
SIDES OF LEGS
SHOULD BE FULLY
SUPPORTED
___'~.2l.~j.llLn_
SHIPPING WEIGHT
__~23_!&S-,--__
UNIT CAPACITY:
__~QQ.Q.._G.E:~____
D
c
B
2',2','/4"
INTAKE DUCT FRAME
~
1. ONE ASSEMBLY PROVIDED
2. AERATOR IS SHIPPED FULLY ASSEMBLED EXCEPT FOR SOME AIR HANDLING EQUIP"'ENT. REFER TO
PACKING LISTS FOR 10ENTIFlCATlON OF FIELD ASSEMBLED ITEMS.
3. ALL AERATOR PLATE IS TO BE 3003 ALU...,NU.... STRUCTURALS TO BE 6061 ALU""NUM,
4, THE AERATOR SHAlL BE WELDED INSIDE AND OUTSIDE WITH FILLET WELDS EOUAL TO THE
THICKNESS OF THE PLATES, ALL MAIN HOUSING SEAM WELDS SHALL BE DYE PENETRANT CHECKED AT
THE FACTORY BEFORE SHIP...ENT TO INSURE THEY ME WATERTIGHT.
5, THE MAXI"'UM ANCHOR BOLT D'AMETER is 7/B'. THE MINIMUM WASHER DIlAMETER IS 2- FOR ALL
ANCHOR SIZES, ANCHORAGE IS NOT BY USFlL TER,
6, FlANGE BOLT HOLE PATTERN IS TO STRADDLE UNIT CENTERLINE.
7. AERATOR INLET AND EFFLUENT PIPE STUBS ARE NOT DESIGNED TO SUPPORT INLET AND EFFLUENT
PIPING, ADDITIONAL P'PE SUPPORTS SHOULD BE USED BUT ARE NOT SUPPLIED BY usnLTER,
B, INFLUENT AND EFFLUENT PIPE MOUNTING HARDWARE AND GASKETS ARE NOT PROVIDED BY USFlLTER,
9. IF INSTALLATION INSTRUCTIONS ARE NOT CLEARLY UNDERSTOOD, CONSULT USFlLTER FOR ADDITIONAL
INFOR...ATlON BEFORE COMMENCING ERECTION,
10. IMPROPER STORAGE, HANDLING, INSTALLATION. OR FIELD MODIFICATIONS OF EQUIPMENT MAY RESULT
IN DAMAGE AND LOSS OF WARRANTY PROTECTION
11 THE BLOWER MOTOR MUST BE WIRED CORRECTLY TO THE VOLTAGE LISTED ON THE UNIT
12, REMOVE THE DRAIN PLUG ON THE BLOWER CONDENSATION DRAIN BEFORE START UP
13. INTAKE AND EXHAUST DUCTlNG ARE NOT BY USFll TER.
A
TITLE
INDUCED DRAFT AERATDR
144" SOUARE, 10' ~O" HIGH
UNIT NUMBER 2
CLIENT
J~P.O, 2004-08-11850
:~PROJ, M21 ~34957~SPEC, 11230
U~----
----
- -- - --
------ -
-------
- -- - --
- -----
- -- ---
WTC - GENERAL FiLTER PRODUCTS
AMES, IA
(515) 232-4121 FAX (515) 232-2571
DRAWING REV
PROJECT
100615
o
1612714002
Underdrain System
UNIVERSAL@TYPE S@ UNDERDRAIN
O-RING
SUPPORT RIBS
RECOVERY CHANNEL
GROUT LUGS
BOTTOM RIBS
AIR ORIFICES
WATER ORIFICES
BELL END
ALIGNMENT TABS
SNAP LUG RECEPTORS
TONGUE & GROOVE CONNECTION
with LEOFLEX SEALER
PETSUOO
02/95
.A,I
I
) ri.
Il h
(SA1) (SA1)
II
I 1====== I======~ I::" ---- M!
---:0" ------ -::.-=.-=.-=.":::::
------ ------ ------ ------
~" _=.0; ------ ------
I II
~) ~
(SAl)
It
()
U (9
z
~ II
@) 0- I II
CJ) I~~:: ~====== ====== 1====== ------ 1="---- ~====== I l-
I ------ ------ ------ -----
en --- ------ ----- I W
UJ (9 I II ..I
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<( 0 ..I
0- a: ::::I "'
en l- N
...J C>>
<(
::> W
0
UJ l-
N U)
~ ~ cr
(SAl) (SAl) ~
I II
I::=.-::.-=.-=.-=.: ~-::.-::.-=.-=.-=.-::. II
.=:: ------ 1------ I
!'"- ------ ------ ------ ------ ------ 1====== ----- II
I II
,
~,} ~,}
/ ~
~ A-.J I
)
WASH TROUGH STABILIZER
~
PLAN VIEW
4. ARRANGEMENTS REQUIRED
SCALE: 112" " 1'.0"
~
N
~
SECTION "B-B"
i
~
2'.2""
:.,
~
'"
+
....
GUllET WALL
STIFFENING EAR
J . REOUlREO
2'.3'
6'
OPENING IN GULLET WAll TO BE FILLED
WITH GROUT AFTER TROUGH IS POSITIONED
& lEVELED. WAll MUST BE BRIDGED
OVER TROUGH FOR PURPOse OF HOlD DOYVN
INTEGRALLY MOlDED
WATER STOP
HEX. NUT 518~.11,FlATWASHER
AND LOCK WASHER
~
t-
18"w x 23"d WASH TROUGH
STABILIZER ANGLE wf3l8"-16 x 1-LG
HEX HD. MACH, SCR, HEX NUTS, FLAT AND
lOCK WASHERS, (STABILIZED ANGLE TO BE ST.
STL TYPE 304.)
<J
(SA2)
,ISA11
(SA2)
Ll
SECTION "A-A"
SCALE. 3/4"" 1'-0"
TROUGH BRACKET wf3/8'-16 x 1114'LG. HEX HD
MACH. SCR. HEX NUTS. FLAT AND LOCK WASHERS.
(ALL ST, STl.1 TROUGH TO BE FiElD DRILLED (13/32'
OIA. DRIll) TO SUIT
<T
,ISA1)
<1
~
l'
4
~
-B"
_ B.JI
(6) HOLES - 9116" OIA.
1- OIA "ASS" SPREADER
10. REQUIRED
8 EQUAL SPACES@
SPREADERS SPACING
(TROUGH LENGTH)
(WALL OPENING)
HEX. HD. MACH. SCR
318-.16 x 11M" &
FLAT WASHER
WASH TROUGH
12 - TOTAL REQ'D.
SCALE: NONE
191f4"
~
on
M
:'
"23/B"'
~
"21/16"
"21/16"
REAR TROUGH MOUNTING ASSEMBLY & DRILLING
MArl STN.STl, TYPE 316 (WELDED CONSTRUCTION)
. . DIMENSIONS FROM INSIDE OF TROUGH
12 - REQ'O, FOR 18" WIDE TROUGH
WAll BRACKET w/J/8"-16 x 3"LG ANCHOR UNITS.
HEX NUTS, FLAT AND LOCK WASHERS. (WALL ANGLE
To BE ST. STL TYPE 304.)
(20) . 13132- DIA. HOlES REau.
INTEGRALLY MOlDED
END CLOSURE, 318" THK
518".11 x S"LG. ANCHOR UNIT WI
HEX NUT, FLAT WASHER AND lOCK WASHER.
( 3. SETS REQUIRED)
1/2--13 xl 1(2" LG. HEX. HD.
MACH. SCR. HEX. NUT. FLAT WASHER
AND LOCK WASHER
NOTES:
I
I
:::::~
I
I
. :
23"
1"
S 11T
H.
HEV: 946.06
_....!
,~
1. TROUGH IS DESIGNED FOR A MAXIMUM CARRY.OFF CAPACITY
OF 257B G.P,M. WITH 2"" OF FREEBaARD,
2, WASH TROUGHS TO BE FIBERGLASS REINFORCED POl YESTER
RESIN, COLOR BLUE.GREEN (LEO-LITE 1187) GENERAL
PURPOSE RESIN, ALL CUT EDGES TO BE RESIN SEAlED.
3 FIELD DRillING OR FIELD CUTTING OF LEOpoLD'S F.R.P
PRODUCTS IS NOT DONE BY LEOPOLD COMPANY. A SUITABLE RESIN
SEAL KIT WILL BE SUPPLIED BY LEOPOLD Co. FOR ANY FIELD
DRILLING OR FIELD CUTIlNG DONE BY THE CONTRACTOR
4, ALL MOUNTING BRACKETS & ST ABIUZERS TO BE STN STl. TYPE 304
UNLESS OTHERWISE NOTED
ALL HAROWARE TO BE STAINLESS STEEL. TYPE 18-8
REVISION
THIS ORAWJl'oIG IS Sl:~T TO YOU SI..tiJECT TO RETURN UPO~ DEMANO. ANa wrrn THE
UNOERSTNtOlNG THAT IT IS NOT TO BE REPRODUCED. COPIED OR: USfD DIRECT\. Y OR
INOIRECl1.Y. IN />J'l'f WAY OfT'RIMENTAL TOOUA INTERESTS AU P"TENTAIG.IfTS RESERVED
WASH WATER
TROUGH
ARRANGEMENT
MTP
SCALE
AS NOTED
High Service Pumps
~
6 WARNING
DISCH COL
SIZE SIZE
8 C EFFlGH
K
L
00 NOT OPERATE THIS MACHINE WITHOUT PROTECTIVE GUARD
IN PLAce:. ANY OPERATION OF THIS MACHINE WITHOUT
PROTECTIVE GUARD CAN RESULT IN SEVERE BODILY INJURY.
12 12
1 7 12 V2 16 V4 1 1 32 718
14
2
A
Bl
=;H
r-~T
~. .GE CONN
It. 1501 DISCHARGE
t FLANGE (FLA T FACE)
C
J L RDTTOU OF !;nt FPI A TF
~~,:.: '(5)'[1" MINIMUM GROUT
RECOMMENDED
(4)
~ PUMP
42.69
(6)
8" THRU 20. DISCH,
(4) H DIA HOLES
PLAN VIEW OF SOLEPLATE (2)
x
;-1
/ . .
. ...... : .,....:. ,.fII: '. ~ ....~.. ,"
Sump Floor
.
.,
/
/
1. THIS DRAWING NOT FOR CONSTRUCTION OR
INSTALLATION UNLESS CERTIFIED. DIMENSIONS
SHOWN ARE TYPICAL AND MAY VARY DUE TO
VARIOUS TOLERANCES,
2. SOLEPLATE MUST BE SUPPORTED ON ALL
4 SIDES AND GROUTED IN PLACE.
3. MINIMUM SUBMERGENCE REQUIRED AT
MAXIMUM flOW.
4. MINIMUM DIAMETER REQUIRED TO REMOVE
BOWL ASSEMBLY
5. DET AlL SHOWN FOR ILLUSTRA TION ONLY AND IS
NOT INTENDED TO REPRESENT THE ACTUAL
INSTALLATION.
6. CUSTOMER TO VERIFY OR ADVISE OVERALL
LENGTH PRIOR TO OR AT RELEASE.
.... ".'.
Flanged Column
BOWL First Stage Each
Open lineshoft, Flanged Column Additional W X Y Z BY MB
SIZE Single Stage Multi-Stage Stage
14F 29.88 29.88 13.38 8 18 17 30 14.0 18
CUSTOMER
W W GOETSCH ASSOCIATES
JOB NAME
P.O.
10258
[ffiJFairbanks Morse
PUMP SIZE & MODEL
14F 7100AW
MOTOR
U SELECTRIC
CERTIFIED FOR
PROJECT NO. 0878.39
SERVICE PUMPS
ROT
CCW
PENTAIP. PUMP GP.OUP
SETTING PLAN
MODEL 7000/7100 PUMP
ENCL TYPE"LS"SURF ACE HEAD
WP-1 WITH SOLEPLATE
DATE
9/2.3/04~~~' S-087839
REV
~ '0' ~ '!:! ~~ .~, ~~~ OUMO
IN PLACE. ANY OPERA nON OF THIS MACHINE WITHOUT
PROTECllVE GUARD CAN RESULT IN SEVERE BOOIL Y IN.AJRY.
DISCH COL
SIZE SIZE
B C E F F1 G H
K L
16 16
19 5-l'4 1911211/2 11/2 44 1
20 2
--
A
--
MIN. WATER
LEVEL
( PUMP
B. THRU 20. DISCH.
(4) H DIA HOLES
PLAN VIEw OF SOLEPLATE (2)
... ,,-. ... ..:'4..,' '
"
1. THIS DRAWING NOT FOR CONSTRUCTION OR
INSTALl" TlON UNLESS CERTIFIED. DIMENSIONS
SHOWN ARE TYPICAL AND MAY VARY DUE TO
VARIOUS TOLERANCES.
2. SOLEPLATE MUST BE SUPPORTED ON ALL
4 SIDES AND GROUTED IN PLACE.
3, MINIMUM SUBMERGENCE REOUIRED AT
MAXlMUM FLOW,
4. MINIMUM DIAMETER REQUIRED TO REMOVE
BOWL ASSEMBLY
5. DETAIL SHOWN FOR ILLUSTRATION ONLY AND IS
NOT INTENDED TO REPRESENT THE ACTUAL
INST ALL A TlON.
6. CUSTOMER TO VERIFY OR ADVISE OVERALL
LENGTH PRIOR TO OR AT RELEASE.
42.50.
Sump Floor
--
Flanged Column
BOWL First Stage Each
SIZE Open lineshaft. Flanged Column Additional W X Y Z BY MB
-- Single Stage Multi-Stage Stage
22A 42.50 42.50 20.50 6.25 18 22.50 30 21.50 24
CUSTOMER
W W GOETSCH ASSOCIATES
JOB NAME
P.O.
10259
iii Fairbanks Morse
PUMP SIZE & MODEL
PENT A I ~ PUMP GROUP
22A 71 OOA W
MOTOR
U SELECTRIC
CERTIFIED FOR
PROJECT NO. 087840
CCW
ENCL
WP-1
SETTING PLAN
MODEL 7000/7100 PUMP
TYPE"LS"SURF ACE HEAD
WITH SOLEPLATE
DWG. S- 087840 REV
NO.
Submersible Pumps
ITT FLYGT
Submersible Solids Handling
Pumps
Engineers and operators appreciate the compact,
heavy,duty design of Flygl submersible pumps.
It's a fact, that much of our replltation results
from years of successful operation in difficult
application~, often after replacing equipment which
didn't live up to expectations. With over 50 years
of experience in the design and application of
heavy-duty submersible pumps, we don't mind the
challenge Today, nearly 2 million Flygt installations
around the world give testimony to the dependability
of our products.
In new Installations, compact Flygt units can be
Installed directly on the floor of the wet pit uSing a
simple ilutomiltic dischilrge connection and guide
bars. The wet pit "P" style mount eitmlnates the need
for a separate dry pit, which reduces construction
costs by 60% in concrete and excavation work alone.
With Its "T" stand, the pump mounts in the vertical
centrifugal dry pit configuration. in-line With the
piping system The inherpnt flood-proof design and
close coupling of motor to wet end makes this the
ideal replacement chOice for vertically mounted,
close coupled or long shaft pumps IOLaled in
existing dry pits The pump can also be provided
for in-air operation in the "Z" configuration,
mounted in the hOrIZontal dry pit configuration for
easy "back pull-out" inspection and maintenance,
The "S" portable style mount, utilizes a heavy duty
stand and elbow for easy hose or pipe connection,
making it perfect for emergency bypass and other
temporary pumping applications,
Flygt offers the most broad and complete range
of heavy duty submersible pumps available
pumps with the size, capacity and characteristics
to fit any solids handling application
Fi,'gt IS a reg's:ere-c ~f5d~rr,aro( f:;f !'TT >=L ~~t AB
CcP)"rgrt 2005 ! :"'!~/g! ~(:...tjn,!lh_Y' ':j~D'..l' '-
jJrinted () :J~4
F!ygt re-serve5 the [-9'1: tc cr-ar-:g€ tne .sp~!f(3'.!()r~;
contair:ea :r> :"1is. brC-crJre 1,..'dl0J~ r,ctcc
. SIX different impeller types:
1. Semi-open, self cleaning, non-clog solids
handling (N)
2 C!osed, non-clog solids handling (e),
3. Closed or semi.open for abrasive slurry (H).
4. Vortex for abrasive and difficult solids
handling (D).
5. Open, chopper for fibrous waste/difficult
applications (F)
6. Semi-open grinder impeller with hardened
cutter (M).
. Cast iron, stainless steel or aluminum bronz models.
. Capacities to 50,000 GPM, heads to 575 ft,
. Discharge sizes: 1,5".36", motors to 1 ,250 lIP
. Voltages from 11 5V to 4,1 60V
. Class H motor insuldlion.
. Factory Mutual approval for USe in hazardous
locations.
. Standard operation to 105' F (40' () ambient or
warm !iquld option to 195'F (90'CI.
All major components of every Flygt pump" seals.
electric motor, impeller, ete. arc milnufactured
by Flygt to our own rigid standards. 'vVhen long
term dependability and total evaluated costs are
important, specify the best... specify Flygt
2
F us Cat
Page 1 of 1
PRODUCT: CP 3085 LT - SLUO'-E PUMP; PeKaR.l.JUCE W11>
Product picture
Curves (~, Enlarge
w
..
P_r - [Hp]
'4
, 'l'
_.._~_ 1 L--
3
3
"
I
==F=
,i
:2
,2
,
I ;-.1'1,
....~,.~'
: ,_,,:,=, ,'-
o
o
100 200 :300 4:00 500
Flow . [USgpm)
" I Pem,rmance
., I NCSHre
" I Shaft Power
Pump Data
Curve ld: 63-414-00-5301
Impeller: 414 Poles: 4 - pOle
Motor: 15-10-4AL
Frequency: 60 Hz
Motor Data
Rated output Nominal
power 0 voltage
Hp (kW) (V)
3 (2.2) 3 230
3 (2.2) 3 460
Pump
motor
Hp 100~ load
3 78
Full load Locked rotor Locked rotor Locked rotor
current current kVA code letter Poles/rpm
(A) (A) kV A/H P
8.7 44 18 G 4/1700
4,3 22 18 G 4/1700
EffiCiency Power factor
75~ load 50% load 100% load 75% load 50% load
79 77 0.83 0.77 0.66
Cable Data
HP Cables Volts Max. length (Ft)
1
230
460
165
675
#14/7
O.75"-(19.0mm)
Conductors (In one cable)
(3) 14 AWG (PWR)
(2) 14 AWG (CTRL)
(1) 14 AWG (GND)
(1) 14 AWG (GC)
Warm Uquld Data
De-rated
Rtd. Amh. Temp. Rtd. Curr.(l) Rtd. Curr.(2) Shaft Power
700 C / 1580 F 4.3 A 8.5 A 2.9 Hp
Type Part number
Cable size/Nominal 00.
3
STD 942102
Available Discharge Connection Outlet Size
Outlet Drilled Flange 4'
file:IID:\catalog\common\applications\FUSCat\ProdOverViewData\CP3085\STDC... 11/8/2006
I ~ 20
I~
I
I
I
I
I
i
I
......,
-I
~I
~I
&J
~I
g:i
iil
I NPSHre = NPSH3% .. min. operational margin
Performance with clear water and ambient temp 40 DC
FL~
PRODUCT
TYPE I
LT I
I
PERFORMANCE CURVE
CP3085.183
DATE
2006-11-08
3
22
4.3
1700
0.023
1
CURVE NO
63-414"()()"530 1
IMPELLER DIAMETER
hp I 183 mm
: r~O~~~~AL --..--
[FREQ, ,PHASES VOlTAGE
rpm I 60 Hz l 3 i 460 V
kgm2! GEARTYPE RATIO
1-
ISSUE
1
e Pum Prior Lake WTP
112-LOAO RATED
I POWER ..
0.77 I 0.66 I STARTING
79.0 %! 77 0 % I CURRENT.
I . iRATED
I I RACURRETED NT ,..
IINLETIOUTlET
i -I 4 inch TSJiijg.:iOF
,IMP. THROUGHLET INERTIA ,.
I 3.1 inch I~S
POWER FACTOR
EFFICIENCY
MOTOR DATA
COMMENTS
POLES:
4
[hp]
a:: a::
~ ~
o 0
Q.. 0.
..... .....
::J ....
. Q. ~
! ~ (/)
'0.
2,8
L.L
~
.... ....
-' l1.
-' W
~ Q..
W :;
E; ~
0..
0:: 2.4
W
~ 2.0
Q.
1.6
OUTY-POINT
HEAo[fll
25.3
14,3
NPSHrellIJ
16.2
11.3
POWER lhP)
2..81 (2.21)
2.93 (2.29)
EFF.I%)
23.4 (30.0)
37.3 (477)
FLOW(vsgpm1
101
302
1
B.EP
NPSHre
I [ft]
--r
i
.....
z
o
0.
L.L
U.
UJ
.....
V)
W
III
[ft]
30
.-.t --.. 30
I
I
r
25
EFF.
[%]
40
15
30
10
20
10
5
o
o
o
350 400 [USgpm]
50
150
100
200
250 300
FLOW
~
HI B Curve
+
~-<t 1 nt"<t.
L() i 0 i
~ i ;- i
t-=--.1
.....
i, c.l
_,04
25~
6~
.'
04"
STD. CLASS 125
C.!. FLANGE
(NOM. 5! ZE)
(TO FURTHEST POINT)
...
REF. LINE. I .
!
_.
'- r-r.l-<t
. . l1J ,
~t1
i i ~I"<tl.
i '8" n[
3.3
8
I. ... -
i,
25'~
16"
--r" ....
18" i 1 ~
REr. UN[
....,. .
4r;t -
16
;.....
10"
.. ~
L_ GUIDE BARS
&
~,
('-J
I"":!'<t
('.j
.,
2~
REF. UNE
.... ! ~ .....
i .
;~r------0
:x: .-' --;- CO !
U i -+--+ _ ~ -=.I
U) i ." .3')
0; Qgl ", BOLT ~4 (4x
u..' ~
o ~
d VIEW W-W
EQUIPPED WITH IMPELLER: 412, 414, 612 OR 614.
* DIMENSION TO ENOS OF GUIDE BARS
~ :OrDi~ensjonal drwg
.:.- CP 3085 L Tl
S'-UDc.E PU,",9 : ~'C)cz. ~kE WTp
k...:~, .3' ;JiJ
.:.
4"
Fus Cat
Page 1 of 1
PRODUCT: NP 3102 MT - ~C.lAl~ PufWtP : PI2,c.2 LAKE WT'P
Product picture
Curves @ Enlarge
Head - [Ft]
t;;;1;
't
o_,oW--' I
i
,
,I .
I ~.
~.
Powt!r - [Hp]
-6
5
..:
3
.,
4
----- -----"
/'
o
200
400
600
o
900
" I Performance
Flow - [USgpm)
"I r-.PSHre
" I Shaft ;lo"'E'r
Pump Data
Curve id: 63-463-00-3703
Impeller: 463
Poles: 4 - pole
Motor: 18-11-4AL
Frequency: 60 Hz
Motor Data
Rated output Nominal
power 0 voltage
Hp (kW) (V)
5 (3.7) 3 230
5 (3.7) 3 460
Pump
motor
Hp 100o~ load
5 85
Full load Locl<ed rotor Locked rotor Locked rotor
cu rrent current kVA cOde letter Poles/rpm
(A) (A) kVA/Hp
14 83 33 H 4/1745
6.8 42 33 H 4/1745
Efficiency Power factor
75% load 50% load 100% load 75% load 50% load
85 83.5 0.81 0.75 0.63
Cable Data
HP Cables Volts Max. length (Ft)
1
230
460
165
690
# 12/7
0.83"-{21.0mm)
Conductors (In one cable)
(3) 12 AWG (PWR)
(2) 12 AWG (CTRL)
(1) 12 AWG (GND)
(I) 12 AWG (GC)
Warm Uquld Data
De-rated
Rtd. Amb. Temp. Rtd. Curr.(I) Rtd. Curr.(2) Shaft Power
70oC/1580F 6.8A 14A 4.9Hp
Type Part number
Cable size/Nominal 00.
5
STD 942104
Available Discharge Connection Outlet 51%e
Outlet Drilled Flange 4"
file:/ID:\catalog\common\applications\FU SCat\ProdOverViewData\NP31 02\STDN.. . 11/8/2006
n.~ !PRODUCT TYPE
PERFORMANCE CURVE I NP3102.181 MT
DATE PROJECT CURVE NO II~UE
2006-11-08 Reclaim Pump - Prior Lake \NTP 63-463-00-3703
111-lOAD 3J4.LOAD II2-lOAD I =R ..... IIMPELLER DIAMETER
5 hp I 172 mm
POWER FACTOR 0.81 0.75 0.63 STARTING I
EFFICIENCY 85.0% 85.0% 83 5 % I CURRENT.. 42 A i MOTOR # STATOR REV
. RATED i 18-11-4AL i 01YSER! 11
MOTOR DATA - - - CURRENT 6.8 A
COMMENTS ; INLETIOUTlET RATED 1745 ! FREQ. I PHASES! VOLTAGE iPOl.ES
I SPEED ..... !pm
I i _I 4 inch TOT.MOM.OF ' 60 Hz I 3 I 460 V 14
I ,IMP. THROUGHlET INERTIA ... 0.027 kgm2 GEARTYPE RAno I
,
I NO. OF i I
, - BLADES 2 - -
I .-----
[hp]
5
a::
w
~
a.
4
3
DUTY ..f>OlNT
HEADfftl
34.3
255
POWER [hpl
4.41 (3.81)
5.04 (4,31)
1
a.E.p.
lUS<x>ml
261
468
eft]
'''l l' I I tu+
45
I~ i Ii
i f".-... i i i
l, ~\ i\ 1,
: 1'-.... I I: _
: ; 1'1....---r :
/~ ' "I
--~ ~
I .........
: r::....
40
35
C 30
<(
W
:I: 25
:
....
..,
U"l
o
a:>
o
o
~I
uil
~i
a..
~I
i/
! /' /
1/1/
1'/
/
./
II
'/1'
Y
5 1/
I i
o II
o
I I
I i
I
i
I
j
- i
I
i
i
!
!
I
400
20
15
10
I
I
I
I
100
200
300
NPSHre = NPSH3% + min. operational margin
Performance with clear water and ambient temp 40'C
\
i /1 i EFF.
i V I 17.5 [%]
i' I
~ ,I
--f-.... I ~ ,50 60
/............1 " ~2.5 50
V ~"k'
t><' I f I j" ""-
0.0 40
--- "'- I I """
"-..
7.5 30
f'.-..J ,
N !
i "-1..5.0 20
[
: cr
800 [USgpm]
EFF.1%1
51,1 (59,7)
60.0 (70.2)
NPSHnlflll
9.5
9.4
I
I
I ! '-'
!
1 I
I I
!
I I
I I I
i i
t ! I
\
! i
i I----
!
.........
500
600
FLOW
a:: rr:
w w
! 3: ~
i &: n.
i I- i
i;:,
,0-
I ~ Ul
0..
u.:
u.
. ~ "-
i ~ tt
; ~ Co
i ~ ~
o 0-
0..
NPSHre
i I [ft]
,
i i / ~~,5
i
i / I
I ~.O
I /
\ \
...
2
o
c.
U.
LL
W
....
Ul
w
m
r
i
700
JP'L~ HI B Curve
"77'
...J 4
~--.__._--------_._----_._-
I
REF. UNE
(TO FURTHEST POINT)
__ ___ ~__~.___ .________m__._____~___.._.
..!..
26d
...
I 72
W~
I . ~~' ~~.
! I . to r--....
1 . ~._. ,'.: .,..~. ',f.. '
. ,r<":j"<t I
. / " I ' . 1'- i
, ..--+
,/.-' ; r-K'.,l' &
<' 7" : 7.1 . !
..... .;:' 4 ~
~,~..o ~ ; '"~-
"---- .
-.c
REF.
j;2
8., ..
i
LINE
.... ....
1 >:<
!u
-!
i 11
'.'4
16
"""<t
L[)
10
..... ..
2" GUIDE BAR (2x)
(SCHEDULE 40 PIPEJ.___
(NOT BY ITT FL YGT, CUT
TO LENGTH AT ASS'Y)
4" DIA STQ,
CLASS 125
C.I. iLANG[
r"J"<tr
or
,. ,
~~.
t"l
-
N
<:" ,
J ,;
--------'"-+--
2 ~ REF. LINE
.! ...
-.t-
, .
---.- ~ - - - +- ----.
-'-- --4 - :.-- - CX) .
I. " . ,
fIl' -t-,--, .--
_ . "t
o 9/" t DIA ANCHOR
~ .~,~., BOLT ( 4-;;T"-
...J
U VIEW W - (I]
ALL DIMENSIONS IN INCHES
* DIMENSION TO ENDS OF GUIDE BARS
t( Ra\.AII'l'\ P~p . Prz\~2. lrw:E. w rp
,
rr~
AUTiJCA[;
DR.AW~G
Oeo-~-""et'~
Dimensional drwq
NP 3102 MT -
~:~.>\ ~.,:" ::
~I/
-1 -1
Wei ht (L8S)
Purr.::) ) Disch
24 C 8~=,
l~:~~~~Ll~~@~::: oj -~'J 5
:~...~ :..3g9
0F.i.: -::. '7 ;;1
Valves
,.~.....,...
PILlTT
Henry Pratt Canpany
t
INPUT ROTATION OPEN
LEFT (01.) UNLESS
OTHERWISE NOl[!)
F - NO. '" SIZE OF BOLTS
125# STANDARD LAYOUT
STRADDLE CENTERUNE
INCLUDES TAPPED HOLES
EACH FlANGE.
TAPPED -HOLES:
"r SIZE UNC-2B X "~ DEEP
24' VALVE 4 HOlES
2 TOP '" 2 BOTTOM
30' '" UP 8 HOLES
4 TOP '" 4 BOTTOM
EACH FlANGE
HENRY PRATT COMPANY
401 5 HIGHLAND
AURORA, IL 60506
PHONE: (877) 436-7977
www.henrypratt.com
GENERAL ARRANGEMENT DRAWING
TRITON-XR BUTTERFLY VALVE
FLANGED ENDS MDT MANUAL ACTUATOR
W/REPLACEABLE PACKING BONNET
BY APP.
MJH aJ~
ORA'MNO NO.
S- 2068
OAlE
05-07-01
~
I
I
FOR BI-DIRECTIONAL SERVICE
ACTUATOR IS SUITABLE FOR
FlOW IN EITHER DIRECTION
HANDWHEa
FOR UNI-DIRECTIONAL SERVICE
ACTUATOR IS SIZED FOR FlOW
IN THIS DIRECTION ONLY
~sj-Q
T " SEAT
SIDE
N
P
ACTUA TOR POSI110N 1
NOTES:
1. ALL DIMENSIONS SHOWN IN INCHES.
2. "D' Dlt.lENSlON :1:1/8'.
3. FOR BOlTS SMALLER THAN "1-3/4. BOLT HOLES WILL
BE 1/8' LARGER THAN DIAl.tETER OF BOLT.
,FOR BOlTS .1-3/4 OR LARGER. BOLT HOlES WILL
BE 1/4' LARGER THAN DIAl.tETER OF BOLT.
4. DIMENSIONS ANDORIWNG OF END FlANGES
CONFOR'" TO THE AMERICAN CAST IRON FlANGE
STANDARDS. ClASS 125 (B16.1).
5. VALVES MANUFACTURED ac TESTED IN
ACCORDANCE WITH AWWA SPECIFICATION C-504
LA TEST REVISION. CLASS 150B.
6. RECO......ENDA TlON FOR MATING FlANGES: WHERE
INSULATING BUSHINGS ARE USED. IT IS NECESSARY
THAT BOlT HOlES BE DRlliED OVERSIZE BY AN
Al.tOUNT EQUAL ,.0 TWO TIMES THE INSULATING
SlEEVE THICKNESS TO MAINTAIN THE SAl.tE MINIMUM
ClEARANCE FOR BOlTS. .
7. CAUTION: IT IS RECOMMENDED THAT VALVES
BE INSTALLED INTO PIPING SYSlnI IN
ACCORDANCE WITH AWWA 101-11 TO PREVENT ANY
UNDUE PIPING S1RESS. DEFl...ECTlON OR BENDING
THAT MAY EFFECT THE PERFORMANCE OF THE
VALVE.
4 1/2 MAX
3 1/2 SPACE
REQUIRED FOR
THRUST BEARING
COVER REJ.IOV AL
1fC=
FlANGE O. D.
..6, JJ DIMENSION FOR 36" 150# VALVE IS 10
JJ DIMENSION FOR 36' 25# ac 75# VALVE'IS 9
25 '" 75 PSI 150 PSI
VALVE A B A B C 0 E F G "JJ
SIZE
24 -- -- 18-5/8 18-3/8 32 8 1-7 8 20 1-1 4 29-1 12 7
- ~30 21-9 16 22-3 4 21-1/2 24-1/8 38-3/4 12 2-1 8 28 1-1 4 36 9
36 25-1 16 26-1 2 25-7/16 28 46 t2 2 3 8 32 1-1 2 4?-3/4 ..
42 29-1 16 30-3 8 29- 7 8 32-11 16 53 12 2-5 8 36 1-1 '2 49-1 /2 10
48 32-5 16 34-5 8 34-1 16 36- 7 8 59-1/2 15 2-3 4 ~ 1-1 2 56 10
54 36 1 8 38-1 2 37-1 2 40-11 16 66-1/4 15 3 ~ 1-3/4 62-3/4 10
60 39-5 8 42-1/16 41-3 4 45 3 16 73 15 3 1/8 2-1-3/4 69 1/4 10
66 43-<11 1fl 4fl-3/4 46-1, '16 4<1-1 I? 80 18 ,1-:~/R ~?-1-,1/4 76 11
72 46-15 16 55-5/8 50 53-1 /8 86-1 /2 18 3-1/2 60-1-3/4 82-1/2 11
ACTUATOR J L M P Q R S W NUMBER
SIZE N T V OF TURNS
MDT -45 12 9-1 8 40
t.lDT-5 18 16-7 16 44-
MDT-55 24 22-1 4 136
MDT-65 24 22-1 4 215
~-DATE
REVISION
REVlSION
REV. -DA TE
HENRY PRATT COMPANY
401 S HIGHLAND
AURORA, IL 60506
PHONE: (877) 436':"7977
www.henrypratt.com
GENERAL ARRANGEMENT DRAWING
MODEL 2FII FLANGED BUTTERFLY VALVE
MDT MANUAL ACTUATOR
ORAWlNG NO.
S- 2011
01. TE:
05-07-01
. BY I APP.
MJH {)u(j
~;
ACTIJATOR PosrnON 1
NOlE: INPUT ROTAnON OPEN LEFT
(Ol) UNLESS OlHERWlSE NOTED.
F '" NO. dt SIZE OF BOLTS
125# STANDARD LAYOUT
SlRADDLECEN~NE
INCLUDES TAPPED HOLES
EACH FLANGE
--1~
7t I~
'-1'
/~ -L ~'.
I ~ \ A
? +
I
~. ~ j
!~ ~Wl cfl
',...T~/
- ~
CAST S1Ea BODIES 4" lHRU 20"
.t CAST IRON BODIES 18" dt 20"
HA~ 4 TAPPED HOLES
"r SIZE UNC-2B X "E" DEEP -
PER FLANGE. 2 HOLES AT
TOP AND 2 HOLES AT BOTTOM
G-
BOLT CIRCLE
Coo
FLANGE 0.0.
j
NOTES:
1. ALL DIMENSIONS SHO~ IN INCHES.
2.. "0" DIMENSION :1:1/16" FOR 3" THRU 10H VALVES.
."D" DIMENSION :1:1/8" FOR 12" THRU 20'" VALVES.
3. FOR BOLTS Sl.lAU..ER lHAN '1-3/4, BOLT HOLES WILL
BE 1/8" LARGER THAN DIAMETER OF BOLT.
FOR BOLTS '1-3/4 OR LARGER, BOLT HOLES WILL
BE 1/~" LARGER lHAN DIAMETER OF BOLT.
4. DIMENSIONS AND DRILUNG OF END FlANGES
CONFORM TO lHE AMERICAN CAST IRON FLANGE
STANDARDS, CLASS ~25 (B16.1).
5. VALVES MANUFACruRED dt TESTED IN
ACCORDANCE W1lH AWWA SPECIFlCA110N C-504
LA TEST REVISION, CLASS 150B.
6. RECOMMENDA 110N FOR MA 11NG FLANGES: 'M-iERE
INSULA 11NG BUSHINGS ARE USED, IT IS NECESSARY
"THA T BOLT HOLES BE DRILlED OVERSIZE BY AN
AMOUNT EQUAL TO lWO TIMES lHE INSULATING
SLEEV1:: lHlCKNESS TO MAINTAIN "THE SAME MINIMUM
CLEARANCE FOR BOI, TS.
VAl~ A B C 0 E 'f G
SIZE
3 4-3 4 3-1 4 7-1/2 5 3/4 4--5 8 6
4 5-1 2 3-1 2 9 5 15/16 8--5 8 7-1h'
~6 6-1 2 5-1 8 11 5 1 8--3 4 9-1/2
8 7-3 4 6-1 2 13-1/2 6 1-1 8 8--3 4 11-3/4
10 9 9-7 8 18 8 1-3 16 12--7/8 14-1/4
_-+ 12 10-1 2 11-3 8 19 8 1-1 4 12--7/8 17
14 11-7 8 12-3 4 21 8 1-3 8 12--1 18-3 4
-~16 23-1/2 I
13-1 2 14-3 8 8 1-7/16 16--1 21-1 4
18 14-3 8 15-1 4 25 8 1-9/16 16--1-1/8 22-3 4
_~20 16 16-7 8 27-1/2 8 1-11/16 20--1-1/8 25
AcruATOR J NUMBER
SIZE L M N P Q R S T V W Of ruRNS
- ~MOT-2S 4-11 16 2 218 2 4-1/2 4-1/4 8 1/4 7 7 8 7-7/8 8 918 32
- ~MDT -3S 5 5 8 2- 7/16 314 3-5/32 5-5/8 5 3/8 10 3/8 10-1 2 10-1/8 12 9-1 8 30
- ~MDT-4S 6-3 8 2 27/32 3-3 8 4 7 5/16 6 3/4 11 5/16 11 1 2 11 12 918 40
MOT 5 7 9/16 3 15/32 4- 1 2 5 1/2 8 3/4- 10 17 17 3/16 17 3/16 18 16-7 16 44
I I I Lt-, I I I
I I I IILi I I I
. DAn: I BY r APP. I RE'v1SION II REV, DATE I BY I APP. I RE'v1SION
PRATT
Henry Pratt Company
HENRY PRATT COMPANY
401 S HIGHLAND
AURORA, IL 60506
PHONE: (877) 436-7977
www.henryprott.com
GENERAL ARRANGEMENT DRAWING
MODEL 2FII FLANGED BUTTERFLY VALVE
HANDLEVER ACTUATOR
DATE
05-07-01
1 3/4
rt~
l,t
K
"hr'.
=dt
1 3/4'
I" = NO. &< SIZE or BOLTS
125, STANDARD LAYOUT
SiRADDLE CENTERLINE
INCLUDES TAPPED HOLES
EACH rLANGE
CAST STEEL BOOIES 4. THRU 20.
&< CAST IRON BODIES 18. &< 20.
HAVE 4 TAPPED HOLES
'I". SIZE UNC- 2B X 'C DEEP
PER rLANGE. 2 HOLES AT
TOP AND 2 HOLES AT BOTTOM
C =
rLANGE O. D.
DRAWING NO.
5-2012
BY APP,
MJH
NOTES:
1. ALL DIMENSIONS SHOWN IN INCHES.
2. .0. DIMENSION :tl/1S' rOR 3" THRU 10'; VALVES.
.0. DIMENSION :tl/8' rOR 12" THRU 20" VALVES.
3. rOR BOLTS SMALLER THAN .1-3/4, BOLT HOLES WILL'
BE 1/8. LARGER THAN DIAMETER or BOL T.
f"OR BOLTS .1-3/4 OR LARGER, BOLT HOLES WILL
BE 1/4. LARGER THAN DIAMETER OF BOLT.
4. DIMENSIONS AND DRILLING or END rLANGES
CONrORM TO THE AMERICAN CAST IRON rLANGE
STANDARDS, CLASS 125 (BI6.1).
-5. VALVES MANurACTURED &< TESTED IN
ACCORDANCE WITH AWWA SPECIf'ICATION C-5Q4
LA TEST REVISION, CLASS 150B.
6. RECOMMEND A TlON f'OR MATING f'LANGES: WHERE .
INSULA TlNG BUSHINGS ARE USED, IT IS NECESSARY
THA T BOLT HOLES BE DRILLED OVERSIZE BY AN
AMOUNT EOUAL TO TWO TIMES THE INSULATING
SLEEVE THICKNESS TO MAINTAIN THE SAME MINIMUM
CLEARANCE f'OR BOL TS.
VAL VE B C 0 E F" G
SIZE A
3 4-3 4 3-1 4 7-1
VALVE 4 5-1 2 3-1 2 9
K SIZE 6 6-1 2 5-1 8 11
3-6 B 7-3 4 6-1 2 13-1
8-10 10 9 9-7 8 16
~Ev, -OA TE
REVISION
REVISION
RNATE FOR MOT
UAL OVERRIOE
1/2" CONOUrr
CONNECTION
ffi
ELECTRICAL CHARECTERISnCS (UNLESS OTHERWISE NTED)
120 V AC
20 WATTS
N.P.T.
EXHAUST
1/2" CONOUrr
CONNECTlON
CLOSE
SUPPLY
PIPING SCHEMATIC J.
HoP.T.
SUPPLY
rOIRECTION
0'
CONTROL
V/Io!.VE
ALTERNATE FOR MDT
W /MANUAL OVERRIDE
~
CLOSE
SUPPLY
PIPING SCHEMA"T1C B
~H~~~ V~~ (~~I~~" ~NgP~9 'W':~'S~~'fir~
SHOWN IN PIPING SCHEMATIC "II" (II' REQUIRED)
BZ IlEJoIO'>m OPDI SPEc.
BY OESCRIP110N P
HfNR'I' PIlATT COMP
AURORA. Ill.
PRATT'"
lolDT WITH CYUNDER ACTUATOR
"-WAY SOLENOID VALVE
WITH I'LOW COmROLS AND
MANUAL OVERRIDE
~-2-0J
APPROVED
ORWG. NO.
.-
'* WITH VACUUM CHECK '*
COMBINATION AIR VALVE
A
ci
u
a.:
- lJ-J
;::) _ " 0'1
ej ~ <:t
I.U ,; "
c
I '
c )
,
c.~ "".. ")"
~
':::J j
,.., .-- ~
S
Q,.
B
1"-143C DETAIL
DEl DESCRIPTION MATERIAL AVAILABLE WITH 125 LB. OR 250 LB. FLANGE INLET
1 BODY CAST IRON ASTM A126 GR. B SPECIFY WORKING PRESSURE "2. PSI
2 COVER CAST IRON ASTM A126 GR. B
3 COVER GASKET LEXIDE (non-asbestos) DESIGN FOR 300 PSI MAX. NON-SHOCK SERVICE
4 COVER BOLTS STEEL ASTM A307 GR. B
5 LEVERAGE FRAME CAST IRON ASTM A126 GR. B
6 SEAT BUNA-N SIZES MODEL 10 A B C D WIDTH LARGE SMALL APPROX
7 NEEDLE BUNA-N ORIFICE ORIFICE WT. LB
NEEDLE PIN 2 STAINLESS STEEL ASTM A581 1416 H.T. 1" 143C 11 10 2!. 1 7 . 35
8 2 54
10 LEVER PIN STAINLESS STEEL ASTM A581 T303 2" 12f. 2 8 3 75
145C 14 3 2 :i2
11 RETAINING RING STAINLESS STEEL PHI5-7Mo 1516 3!. 3
13 FLOAT LEVER BRASS ASTM B16 3" 147C 16 3 10 3 32 100
.
14 FLOAT STAINLESS STEEL ASTM A240 T304 4" 149C 18 17~ 3! 4 11 4 3 170
32
18 LEVERAGE FRAME SCREW STAINLESS STEEL 18-8 ,
26 GUIDE BUSHING BRASS ASTM B16
40 BUMPER ASSEMBLY BUNA-N CERTIFIED BY;
42 PLUG BRASS ASTM B124
53 FLOAT RETAINING SCREW STAINLESS STEEL 18-8
t STA.NDA.RD MATERI,4,l ON SIZE ," AND 2" IS DHRIN ASTM 02133 DATE:
-, AND GUIDE BUSHING IS NOT ReQUIRED ON THE FRAME.
2 NEEDLE PIN IS NOT REQUIRED ON SIZES 1" AND 2".
DATE
11-4-88
Ipl~n VALVE AND PRIMER CORP.
H UU@ SCHAUMBURG, fL.
DRWG. NO.
S-140C
0T"'\roroTT"""Tr"Ol\f'nTr\'\.lr nrpWl=''R ~TnF
AIR & VACUUM VALVE (WITH WATER DIFFUSER)
A DIA
B
DET DESCRIPTION
1 BODY
2 COVER
3 COVER GASKET
4' COVER BOLT
6 SEAT
14 FLOAT
24 BAFFLE 1
25 COVER PIPE PLUG'
26 FLOAT BUSHING3
33 FLOAT GUIDE
34 BAFFLE SCREWS
41 BAFFLE PLUG 4
44 WATER DIFFUSER
MATERIAL
CAST IRON ASTM A126 GR. B
CAST IRON ASTM A126 GR. B
LEXIDE (non-asbestos)
STEEL ASTM A307 GR. B
BUNA-N
STAINLESS STEEL ASTM A240 T304
DELRIN ASTM D2133
MALLEABLE IRON
BRASS ASTM B16 C36000
BRASS AS1M 816
STAINLESS STEEL 18-8
BRASS ASTM 816
BRASS (commercial>
1 STANDARD MATERIAL ON SIZE 3" IS CAST IRON ASTM A4B CL. 30.
2 COVER PIPE PLUG IS NOT AVAILABLE ON SIZE ~".
3 FLOAT STEM BUSHING IS REQUIRED QN SIZE 3",
4 BAFFLE PLUG IS NOT REQUIRED QN SIZE 3",
DATE
1 0-20-95
PLArJT [) FloANC:':D EQUIP. CO.
1 .'::1 ):y:,:] S1. NE
Blaine, Mi\J 55449
3" 146WD DETAIL
DESIGN FOR:
125 LB. CLASS RATING
200 PSI MAX. NON-SHOCK SERVICE
300 PSI SHELL TEST
. ': SPECIFY WORKING PRESSURE PSI
AVAILABLE WITH 125 LB. FLANGE INLET.
\JOTE: FOR 150 LB., 250 LB., 300 LB.,
600 LB., AND 900 LB., CLASS RATINGS
llSE SERIES 140H AIR & VACUUM VALVE.
SIZE t" 1" 2" 3"
MODEL No. 141WD 142WD!144WD 146WD
1 1 9!
A 58 7 9'2 2
, 1
B 71; 9; 122" 13
C t 2 3
APPROX. SHIPPING 11
WEIGHT, LB.
60
21
43
CERTIFIED BY:
DATE:
DRWG. NO.
An~n VALVEANoPRIMER CORP.
MJ-'Uu@ SCHAUMBURG,IL.
S-140WD
SPECIFICATIONS OTHER SIDE
[".,.....
ci
Co)
a.:
=Wcn
az""
&&1+01;1;
QCI.l\t)
tI.~z 0
~~~
...CD
0.5
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~...CO
S
a.
0,"'\\
',.P c
J
(~t
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, " :)~
-, " ~
'.7
SERIES 250 SWING CHECK VALVE-125LB. CLASS
14
A
DET
DESCRIPTION
MATERIAL
1 BODY
2 COVER
3 COVER GASKET
4 COYER SCREW
6 BODY SEAT RING
. DISC SEAT
. DISC PIN
9 DISC ARM
10 DISC
11 PIVOT SHAFT BUSHING
12 PIVOT SHAFT BUSHING
13 PIVOT SHAFT
14 OISC ARM SET SCREW
15 PACKING GlAND
16 GLAND STUD
17 PACKING
18 PIVOT SHAFT RETAINING PIN
20 CUSHION CYLINDER
21 CYLINDER MOUNTING SCREW
22 CUSHION PISTON
23 PISTON SEAL
24 PLUNGER SLEEVE
25 PLUNGER SLEEVE LOCK NUT
26 PISTON LINK
CAST IRON ASnI A 128 GR. B
CAST IRON ASnI A128 GR. B
FIBER RU8BER
STEEL ASTM A307 GR. B
BRONZE ASTM B82
BUNA-N
STEEL AISI 1018
DUCTILE IRON ASTM A538
CAST IRON ASTM Al28 GR. 8
BRONZE
BRONZE
STAINLESS STEEL ASTM A278 T303
STAINLESS STEEL 18-8
CAST IRON ASTM A 12& GR. 8
STEEL ASTM A307 GR. B
GRAPHITE FIBER RUBBER
BRASS ASTM B 16
BRONZE ASTM B62
STEEL ASTM A307 GR. B
BRONZE ASTM B62
BUNA-N
BRASS ASTM BI&
STEEL ASTM A307 GR, B
STEEL AISI 1018
DATE
VALVE SIZE 2" 2}' 3" 4" 6" 8" 10" 12" I~"
MODEL NO. 250-2 250-2.5 250-3 250-4 250-8 250-8 250-10 250-12 ~$"O.1li
A 12 12 12 13 17~ 18 23 28 ~
B 7 7 7 81 9 12 14 16 :10
2
C 5 5 5 5 6 9 9 11 .'t'la
D 10 10 10 11 12 14 15 17 ;l~
E 5 5 5 5 7 8 9 11 114>
F 6 7 71 9 11 13~ 16 19 ~~v~
2
G 41 51 6 7 91 11~ 14t 17 ~I '/~
. 2 2
H 5 11 3 ~ 1 11 1~ 11 1~'tII
i ii i 11 8 4
J 3 3 3 ! L 7 1 I Y15
i .. .. 4 8 i 1
K 4 4 4 8 8 8 12 12 I"
i i f
.1
~
c
w
ii:
i=
0::
W
()
~
o
DET
DESCRIPTION
MATERIAL
27 CUSHION LEVER CAST IRON ASTM A12& GR. B
29 COUNTER WEIGHT CAST IRON ASTM A.8
30 AIR CHECK VALVE BRASS '...9,C1!ol..',4,ERCIAh.!..-_, .._.
31 DISC SEAT RETAINING RING BRONZE ASnI 862
---.-.--.--
32 _~S~.B."I"I,NING,~REW ___ STAINLESS STEEL 18-&
33 PIVOT SHAFT..~E!..___ STAINLESS STEEL AsiMA29~fio3
,~. PISTON PIN STAINLESS STEEL ASrM A296 T303
35 cusHl6NiivER-ARM-SCREW--u- "STEEL ASTM-AJ07 GR. a-"
36 --WNDS.TUO'NUT-..----.-.--- - STEEL ASTM A307 GR:ii--'-- --
--.'-.-------
37 , PISTON LINK I'IN__.___._,____ ____ STAINLESS STEEL ASTM A296 T303
36 PISTON LINK COTTER PIN -STEEl}]pMMERCIAl.I'-=--===
.0 BOOY_ SEAT RING~~_,____ STAINLESS STEEL 1&-& __
41 DISC PIN NUT STAINLES~.~~~~_~,!::"-_,____ ..,_..'
.3 _!l.OOY_S!,~T RIN~_S~."~-:------- _.!'~"'-~_u__..
.. PIVOT SHAFT COVER _!TEEL .__,_...______~.__
'5 ,..!'_I,'{.OI SHAFT COV~I'l_~ffll:~___ STEEL ASTM A307 GR. B
46 PIVOT SHAFT COVER SEAL BUNA-N
47 THRUST COLLAR ,--, ---- -BRONZESAE~--
48 COUNTER ~1~tIT~FiM=---==-":""_ ....!~N!STEEL__-=~===.::
.9 COUNTER WEIGHT ARM SET SCREW
50 DISC PIN WASHER
51 COTTER~______~
52 COUNTER WEIGHT KEY
--- ,---~._---
53 COUNTER WEIGHT SCREW
,STEEL AST~~307 G'!:...!I.._________
BRONZE SAE 660
_ STAINLESS ,STEEL..I CoMMEFicl'AL )
STEEL AISI 1016
- -_.._~_...__.
STEEL ASTM A307 GR. B
DRWG. NO.
7 -12-96
In~n VALVE AND PRIMER CORP.
"f'Uu@ SCHAUMBURG,IL.
S-250
SPECIFICATIONS OTHER SIDE
10101 Xylite St. NE
Blaine, MN 55449
RUBBER FLAPPER SWING CHECK VALVE
c
--t
B
l.D~
/
/ '
"""" '. // /' //..- .
~ /...' /
" 'J~
/-
'" , ' OPTIONAL
"'" // MOUNTING FOR HOLD-OPEN
,/ DEVICE AT EXTRA COST.
A
.1
APPLlCA liON INFORMATION REQUIRED:
CERTIFIED BY:
OPERATING PRESSURE
psi.
MEDIA
DATE:
TEMPERATURE
MODEL No. 102 102~ 103 104 104P 10S 110 112 114 116 118 120 124 DETNo. DESCRIPTION MATERIAL
SIZE 2" 2t" 3" 4" 4" 5" 6" S" 10" 12" 14" 16" IS" 20" 24 I BODY CAST IRON ASJ:A~I26
at 9t II~ 13f 13l 19r 241 27t 2 COVER CAST IRON AS GRAOi. 86
A 8 15 31 32 36 40 48 3 GASKET LEXIDE
B 6 7 71- 9 9 10 II 131 16 19 21 231 25 274- 32 COVER BOLTS STEEL ASTM A 30
4 G ADE 8
2 ASTM A 307
C 42 50l 6 70l 71- a.1. 9.1. 11* 14t 17 lat 21t 22~ 25 29t 5 COVER BOLTS STEE-,=---- GRADE 8
4 2 2 2 2 2
5 U 3 15 15 15 11. I~ I!. I~ liG Ii\ III IL 6 PIN HHS AISI 1018
D 8' "4 ii ii i6 ~-~~
16 8 4 8 16 8 METAL PLATE STEEL AS TM A 36
8
SIZE of HOLES 3 3 3 3 3 7 7 I 11- ,1. 11. ,1. I~
4" 4" "4 4 "4 8 8 8 8 8 4 4 8 10 RUBBER FLAPPER BUNA-N
No. of HOLES 4 4 4 8 8 8 8 8 12 12 12 16 16 20 20 NOTE: PIN #6 & METAL PLATE #8 ARE
TOTALLY ENCAPSULATED IN BUNA-N.
DATE J
3-20-90 nGOVALVEANoPRIMER CORP.
"~ @ SCHAUMBURG,IL.
DRWG. NO.
5-100
covrT~Trh~TnN~ n~HER SIDE
Air Compressor
(lij) Ingersollftand.
Industrial Systems-light
Davidson, NC 28036
2545
Ref:
Sheet:
Date:
Cancels:
9820.00
109
23 Aug 2004
7 May 2004
Engineering Data
1--.:-, -.=_____~BO~!~.1 ~~':.~2~~_~-':_.:
i Stroke: :3.5"
f- ,-.--...-,... -,...---..---,..+...--.--...-.-
! Inlet Size: ! 1.25" NPT
i.!~i~~~~i~e_~!~~~:J(tt~_pt_
- -:--_-:~~:.:~.~~]~oT ~'~-~~l~:::~;:~L~~iT {~~f ~.---J
. ~r;i~~1~~" 1 .. .......~it~zJ .. .
_ __ _ ____.L______L ._____._________~___._ _-_I
Performance
-------~
!
I
! i I I , .
, ,. I ; I
, i Motor f ! I
L_.~.!!._.__.L--H.~--J~~..J---R.!'.~_J~~~l-~~_
1--- 254~__~__~_~_ 125 i _Ji~_p 6.4 +-_~
I 2545 ! 5 i 175 : 500 :. 16.1: 5.2
[=:~.?~~:.==:L=-~~~==i __!_5~J~82(.r27.:_4.1 6T=
~ 2545 i 7.5 i 125 i 825 i 27.1; 7.8
~'...l------.---._--._-._-,-------,--.l..--.----~-.--.-,---.'-----,---..-.-I---.~-~
i 2545 i 7.5 i 175 ! 825 '26.6 [ 8.2
F~--~~~~~_~E=1~~-=L~1~~F1~;~..I}~II~~;:r=
! 2545 i 10 : 125 ! 1050 : 35.2 i 10.0
i.-__.___._-j_______~.....-__L__-.-..;-~--!........-~
i 2545 i 10 ! 175 ! 1050 I 35.0 i 11.0
_ ,. ,..',__ .,_m_,.,:n.".,..:,.._,'.',._
kDuPlex units '!l ultipl}' capacity by two. .-T---t---L-.-~_- I
i ~250~SIG ~per~!!'JlPres~ure 1_..-_. L_.__L__~....l____J_.___.
--j
i
FRAME-The 100% cast iron frame is designed to support the overhung crankshaft. cylinders bolt directly to the cast iron
frame. Frame is completely sealed yet allows for maximum accessibility.
CRANKSHAFT -A unique overhung design supported by two heavy duty ball bearings with replaceable crankpin
bushing. Entire shaft is balanced with an integral counterweight to insure smooth operation.
CONNECTING RODS-Solid one-piece design. These simple, easy to maintain rods can be used only with an overhung
crankshaft. Crankpin bushing inside the rod is precision ground requiring no alignment.
CYLINDERS-These are 100% cast iron, separately cast and individually bolted to the frame in a V-type configuration.
The cylinders are precision honed for low oil carryover. Radial fins on the cylinders help remove heat and ensure 360
degree cooling of the cylinders.
PISTONS-Precision balanced low pressure aluminum and high pressure cast iron pistons provide smooth operation.
RINGS-There are three piston rings for sealing compression and oil control. The taper faced compression ring and
beveled oil scraper ring provide quick seating. One, three-piece oil control ring maintains proper lubrication on cylinder
wall. Precision honing used in conjunction with the ring stack up means low oil carryover.
FLYWHEEL-The cast iron fan type flywheel forces a .cyclone" air blast to provide cooling for the deep finned cylinders
and finned copper tube intercooler. The flywheel is balanced to keep vibration to a minimum.
INTERCOOLER-Two stage compressors use an intercooler. The intercooler between stages is of finned copper tube
construction to provide maximum cooling area. It is located directly in the flywheel air blast to remove the heat of
compression between stages keeping running temperatures and power needs to a minimum, ensuring high air delivery for
horsepower expended. The intercooler is provided with a relief valve to prevent over-pressurization.
LUBRICATION-Splash lubrication of running parts is simple and reliable. Lubrication dippers are integral with
connecting rods and cannot come loose,
'NOTE The 2545 Bare is supplied with a single groove beltguard, Two-groove beltwheels should be reserved for replacements
requiring the older style, Please contact Product Support for pricing on two-groove beltwheels,
(/jj) Ingersollland.
Industrial Systems-Light
Davidson, NC 28036
2545
Ref:
Sheet:
Date:
Cancels:
9820.00
110
23 Aug 2004
7 May 2004
INLET FILTER-The filter has a durable canister with a dry type 10 micron inlet filter/silencer as standard.
VALVES-Efficient valve design is utilized. Inlet and discharge valves consist of finger valves which allow maximum air
flow. Valve plate is easily removed for maintenance.
CENTRIFUGAL UNLOADER- The centrifugal unloader automatically bleeds the air from intercoolers and cylinders,
preventing the compressor from starting against full load. This protects the motor from premature wear.
LOW OIL LEVEL SWITCH-Low oil level switch prevents the unit from operating when oil level is low.
r'~:r-;''''~-{r:'':'''.;.~'j'",;.s:<.',t" I~"~:'~;:'~ f'}~ l"~~J,"~'''7~~r~ ~ ~-r~' '?f:'"J.'!~r,~-<< P!'r,r,"l?"~1, "'7~"?';!~:;r..~-:~ ;...:tl<'l1'i7'r!;~U~~~~1;::!J-~'~"';-"';?ri7'rp.;'-~1'~":~~"""~~~~'~~1s:<'''lY~~
~f j ~, ,','1 (::: ~.- I ) (::.f ~ jl (' 0~_. ''';-1'' (::r.:-:{1 r(::~:~ .j(. r'i:'~':< .
,'. _ __ _... _~ ~ ~ -' .__.. __ ~ _ ___ "c_ +_ ~~_ .-'"...._ __ _~_. ...::._. _~_y __ _____~ _ _ _ "- __' _ ~ __~ ~......._,""",~....~<-__,,,,....., _~T....__._
BASE-The compressor and motor are aligned on a heavy steel base.
RECEIVER-Receiver mounted units are ASME, National Board coded, and include pressure gauge, drain valve, service
valve, and relief valve.
DRIVE-The drive is V-belt type with an easily removed, totally enclosed beltguard.
MOTOR-Standard AC motors are 1800 rpm, NEMA T frame with drip-proof enclosure, Class B insulation, 1.15 Service
Factor, and grease lubricated ball bearings. Standard single phase motor voltage is 230 volt. Standard three phase motor
voltages are 200,230/460 and 575.
CONTROLS-Units are equipped for both automatic start and stop operation with NEMA 1 pressure switch with on/off
lever and constant speed control with suction unloading on compressor inlet.
..-~
,--' - . -~-'C~~ '~~~~:;~~~" ~?~'~~1I11ri:-lffi: ~i:-- -f!'~\~AY~l'";\1f7~~tt~~~ff;;;:~~~=":"~~t;!~~~~~'~~~~'~"~~~~~"'7J ,
RECEIVER MOUNTED-All duplex units include two bare compressors with two motors mounted on a single-receiver.
Each compressor/motor configuration is designed to run as an independent compression unit; however, both units can run
simultaneously should system demand require.
1~~'T;i~3I-"<"~""m~--;"l~(%?l~~~5?"~~~..:;;~~tf.-1" "t?i ,.~h T -~"'"i<~ "'!..r~-~i~:':--:-'::;;">'y"~-"',.':'1~ -I;',""" >0;" ';,~ :!:r"~~o;.-<;. .<' ,,"-~1.~~~~.~='-""'~ ~1i"~:::'i'~~~'T:--g.,.".-~ ~"''1f~"''{:r 'i.:.~fl"'\?3?,<~~.u;,~'ij~","O~-"'qJp~~,,">:>t-:i1""';";;C]
"",1;[fJCJ&'.'E:c:Jf"'il;,,';';:rl'\'i'r~~'j )"', .~ 'j ~~""f{rr;;L;J'rr-'f:'"'\i ,;" <r~;-;> 'd'1'";~";::"fl ':f'Y" -~..f;:~';'4j:':j1'~~"ffr,1~" '.' " , ' 'c ." \1
~~:~~}~~.~ ~E ~~:,)-.: 1~~:~ ~~..~$. ::~;J ~o ~:~~_ ~~: ~~,-7~;: v: ~lg ~~ ~~ ~_~:~~ ~~~ lJ~~:~ _~ ~~ -:-w :.r~~J ~~~~~lli~dl, !:~~~_~:::;~"A~~~~. ~..1~~S~ .d~~~-A ,~ h~ 0'
RECEIVER MOUNTED-Duplex value packages include two (2) bare compressors with oil site glass and two (2) ODP
motors mounted on a single horizontal A.S.M.E. coded receiver tank. Standard controls are automatic start/stop with
unloading pressure switch. These packages include an E-Series alternator, mounted and wired, in a NEMA-1 enclosure.
Panel is both U.L. and CSA approved. The alternator panel allows both compressor units to operate in response to
system air pressure demand. For example, if system pressure dips below the preset lower pressure limit, compressor "A"
will automatically start. If pressure rises to the upper set point limit, compressor "A" will shut down. Next time system
pressure drops below the preset lower pressure limit, compressor "B" will automatically start. Should system demand
require, both compressor units will start automatically to meet and maintain system air pressure demand. Alternator
includes (2) duty rated starters with overload protection, (1) control relay for alternation, (1) on/off switch, fused control
circuit, (2) reset buttons through the cover. Package features a totally enclosed belt guard, no aftercooler, with manual
tank drain. Standard voltage is 230-3-60 with optional voltages available to meet specific site needs. Duplex value
package options include install kit, start-up kit, and electric automatic tank drain with power cord. No other options are
available with these packages.
RECEIVER MOUNTED-"Fully Packaged" duplex value packages include two (2) bare compressors with oil site glass
and two (2) ODP motors mounted on a single horizontal A.S.M,E. coded receiver tank. Standard controls are automatic
starUstop with unloading pressure switch. These packages include an E-Series alternator, mounted and wired, in a
NEMA-1 enclosure, Panel is both U,L. and CSA approved, The alternator panel allows both compressor units to operate
in response to system air pressure demand, For example, if system pressure dips below the preset lower pressure limit,
compressor "Au will automatically start, If pressure rises to the upper set point limit, compressor "AU will shut down, Next
(lIP Ingersollfland.
Industrial Systems-Light
Davidson, NC 28036
2545
Ref: 9820.00
Sheet: 111
Date: 23 Aug 2004
Cancels: 7 May 2004
time system pressure drops below the preset lower pressure limit, compressor "B" will automatically start. Should system
demand require, both compressor units will start automatically to meet and maintain system air pressure demand.
Alternator includes (2) duty rated starters with overload protection, (1) control relay for alternation, (1) on/off switch, fused
control circuit, (2) reset buttons through the cover. Package features a totally enclosed belt guard with air-cooled
aftercooler, mounted and piped, and electric automatic tank drain with power cord (115-volt). Standard voltage is 230-3-
60 with optional voltages available to meet specific site needs. "Fully Packaged" duplex value package options include
install kit and start-up kit only. No other options are available with these packages.
~, " '~':" . :. "iJ'if;fIJe-r:r,.f~8'{;r~0 ()-(:,::h-;'fJr;(;.01';"::~~1'fr(~(:rr>'Jel~~'" .': ".'
,. .~.'.~ ~ "'~ ~(.) .' " , _ ~~. ___ ~ ~.., ,~.....~_ p. J.';:'I'''"' ~_..-'-. .J J!':;:;\ ,\......,. ~~,'JJ_~J'" --:::1::r:......~. 'l.-~....-':".,..<::.. f " .~. - , . ~ '
~:.o...._\C_"'~""'/.,,_ 1.i:.:._4~r'.uz.;.~,~ ..."..Ac....."~"'-"_ ,_ "..............."'__..,_ ...". -'::......._.:.>.~ ,""DI.:.!~~...~_.....I,,,,,",~~_~~........L_ '~~~"'-"!"'_ ~,i{I;;:l:.eL~~~_ , ",. ~:fo,';;.-~....... ""',l...",....~~i<,f~~:~:.r.:.lI.:tl<:..,.i). ,.J:~~,~ ~-" -, I
TOTALLY PACKAGED RECEIVER MOUNTED MODELS (10 HP)-The totally packaged model is a simplex compressor
configuration which comes standard with a 120-gallon ASME coded horizontal receiver tank (includes pressure gauge,
service valve, and relief valve), an "E"-Series starter (mounted and wired), aircooled aftercooler, and electric (115-volt)
automatic drain valve. No modifications or options are available with this package. Prewired NEMA-1 electrics will be for
230/3/60 voltage; however the compressor starter is equipped with a dual-voltage coil which is capable of operating with
230/3/60 voltage or 460/3/60 voltage with minor field-wiring modifications. An additional set of heaters, decal, and
instructions to convert the unit from 230 volts to 460 volts are supplied with each unit. The totally packaged 10HP model
is also available in 200/3/60 electrics.
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OUTDOOR MODI FICA TION-Compressor package is furnished with TEFC (1.15 SF) motor, NEMA 4 pressure switch,
and NEMA 4 low oil level switch. This configuration can be used for outdoor installation.
~ AIRCOOLED AFTERCOOLER-An optional aircooled aftercooler lowers package discharge air to within 250F of ambient
temperature. A relief valve is provided to protect against over-pressurization.
. .. AUTOMATIC DRAIN VALVE-As air cools in the receiver, moisture drops out and accumulates in the tank. An automatic
drain valve provides unattended, automatic draining of the moisture from the receiver tank. Either electric or pneumatic
drain valves are available. Fully packaged models are standard with electric drain valve. Electric drain valve is prewired
on units with deluxe starters and is supplied with a six foot heavy duty power cord with AC adapter with "F -Series
starters.
"E"-SERIES STARTER (MTD. & WIRED)-SIMPLEX UNITS-"E"-Series starters provide full voltage control of electric
motors. They include thermal relays which protect the motor windings from harmful currents and resultant temperature
rise caused by overloaded motor, low line voltage or stalled rotor. Reset button and NEMA 1 enclosure (UL & CSA
approved) included.
NEMA 4 DELUXE STARTER (MTD. & WIRED)-Simplex Units-NEMA 4 Deluxe starters provide full voltage control of
electric motors. They include NEMA 4 enclosure, manual reset button, on/off switch, 120 volt control transformer, and
thermal relays which provide overload protection. Fused control circuit complies with National Electric Code (UL & CSA
approved).
"E"-SERIES NON-COMBINATION ALTERNATOR (MTD. & WIRED)-DUPLEX UNITS-This optional panel enables
both compression units to operate in response to system demand. For example, if system pressure dips below preset
lower limit, compressor A will start. If pressure rises to upper limit set point,' compressor A will shut down. Next time
system pressure falls below lower limit, compressor B will start. Should system air demand require, both compression
units will run simultaneously. Alternator panel includes (2) Definite Purpose (DP) starters with overloads, (1) control relay
for alternation, (1) on/off switch, fused control circuit, (2) reset buttons through cover, and NEMA 1 enclosure (UL & CSA
approved).
~ COMBINATION DELUXE ALTERNATOR (MTD. & WIRED)-DUPLEX UNITS-This optional panel enables both
compression units to operate in response to system demand. For example, if system pressure dips below preset lower
limit, compressor A will start. If pressure rises to upper limit set point, compressor A will shut down. Next time system
pressure falls below lower limit, compressor B will start. Should system air demand require, both compression units will
run simultaneously. Alternator panel includes (2) Definite Purpose (DP) starters with overloads, (1) control relay for
alternation, (2) on/off switches, fused control circuit. (2) fused disconnect switches with door interlock, (2) 120 volt control
transformers, (2) reset buttons, and NEMA 1 or NEMA 4 enclosure (UL & CSA approved).
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GAUGE ' "
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OIL FllL____.... IV ~ ~
- Ii, 0 L MOUNTED
LOW all / ALTERNATOR
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~~8rf'RvG,iVE------ If -- L --1
OIL ORAlN I/~' ........ I
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RECEIVER a IJt, I
RELIEF VALVE - i ._. . - I
~~ I
U-At~216[:J ~\:---'~U~:::~~OENSATE
'/ . DRAIN VALVE-l/6"
! l ! NPT ORAJN PORT (OPTIONAL)
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AUlO CONDENSATE
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NPT DRAIN PORT
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MODEL
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2 -2545E5/7.5/' 0
2-25'5A5/7,5/' 0
APPROVED FOR: SIZE:
MODEL.:
PISTON DISPLACEMENT:
SPEED RPM:
DISCHARGE PRESSURE
ACTUAL DELIVERY:
REGULATION:
IR ORDE.R NO.
CUSTOMER:
CUSTOMER ORDER NO.
PER: DATE:
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5
NET WT.
LBS [kg]
1560
[709]
1665
(657)
SIZE
24"X 67"
610X 1702
3O"X 84"
[762 X 213.
RATING:
5
-
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4
3
NOTES:
1. FOUNOAT'ON OR FLOOR MUST BE LEVEL AND SUPPORT
ALL FEET EOUALLY; IF NECESSAlRY SHIM OR GROUT
THE FOURTH FOOT.
2, THE COMPRESSOR ARRANGEMENT SHOWN IS
REPRESENTATIVE OF ALl THE UNITS USTED.
SPECIFIED ACCESSORY ITEMS ARE NOT NECESSARILY
SHOWN BUT WILL NOT INCREASE THE OI"ENSION,
J. FOUNDATION BOLlS SHOULD PROJECT IHRU NuTS
AT lEAST 1/2"[13] TO ALLOW FOR lEVEliNG,
I
., ALLOW AT LEAST '2.00[305] ClEARANCE MIN, ON ALl
SIDES FOR PROPER AIR CIRCuu.TION,
5. "" _ AOD "'Y" WHEN AUiD CONDo DRAIN VALVE
IS SUPPLIED,
6. ALL UNSPECiFiED TQlfAANCES:
XXX - :U 2[3]
xx - %.25 6
x - :%.5013)
5. DIMENSIONS IN [ ) .t.RE MilLIMETER DlUENS1QNS
UNLESS OTHERWISE SPECIFrEO,
AIR INLEl
FILTERS
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A1RCOOLEO
AFTERCOOLERS
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AIR OUTLET
SERVICE VALVE
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1\ FOR e.62[16) UTe. BOLTS
1 '- MANUAL DFWN VAL V[
(LOCATION WHEN NOT SUPPliED
WITH AUTO DRAIN VALVE)
A
-M
RECEIIIER
GAL LITER
'20
[454]
240
[908]
JOB:
O""ENSIONS IN INCHES
CDEFGHJ Kl~NNN
42,50 50.00 17,25 6Z.0 15,9 56.7 17,0. 75.6 76.18 8,00 1.25 11.50
['080J ('270] ['36) ['575 [404][''''0 ['34 [1920 ['935 (203] [32] [29ZJ
42,50 64.00 19,25 67.0 lB.4 61.7 ,5.5j B4.6 85.2 10,00 1.25 13,00
[1080J ('626 ('89] [1702 (467)['567 (396 [2149 216' [2~) (32) [:3(0)
-~
A B BB
'2,000 20,000 3.62
[1067] [SOB] [9Z]
54,OOC 20.000 2,88
(1372) [SOB] (73]
SPEC:
CONTRACTOR:
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"" GENERAL ARRANGEMENT
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ARCH,ENGR,:
MTR. H,P,jkW
MTR. VOL 15:
5TARTER TYPE:
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Air Wash Blower
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Setting
The Industry
Standard For
Over 60 Years
The Sutorbilt@ Legend™ line of rotary positive
displacement lobe blowers and vacuum pumps is the
result of more than sixty years experience in the design,
manufacture and support of superior industrial
equipment. Backed by one of the largest distributor
networks in the industry, every Sutorbilt Legend
blower/vacuum pump is built under rigid ISO 9001
quality standards and individually tested to meet
rigorous performance standards. Sutorbilt Legends are
specified by leading Original Equipment Manufacturers
worldwide for a wide range of applications. Many
OEMs prefer the Sutorbilt Legend design because it,
can be easily customized to their specifications while
meeting strict performance requirements. We take
pride in the fact that a Legend is at the heart of an
ever-expanding variety of air solutions working every
minute of every day around the globe. With a
variety of models to choose from, 20 sizes each
available in 4 different configurations, the Legend
Series delivers pressure to 15 psig, vacuum to
16 "Hg and flows to 3,015 scfm.
Compare us to the competition and you'll
find out why this blower/vacuum pump earned
the name "Legend", ;
rtII Suforb,ilt'j ',:
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Proven Performance. Global Applications. Local Support.
Below are just a few examples of the industries that.
over the decades. have depended upon the Sutorbilt~
LegendT.\l to ddiver dean. oil-&ee air to a wide range
of global applications.
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Industry
Aquaculture
Cement and Lime
Chemical
COal Bed/landnll
Dairy
Dry Bulk Hauling
Environmental Services
Industrial
Milling and Baking
011 and Gas
Power Generation
Process Gas
Pulp and Paper
Resin and Plastic
Soli Remediation
Vacuum Excavation
Wastewater
Application
Aerallon
Fluidization and COnveying OJ
Vacuum Processing and Conveying ~
Methane Gas Recovery
Automated Milking
Trailer Unloading and Aeration
Sewer Cleaning and
Portable Restroom Services
Material Vacuuming
Blending and COnveying
Gas COllection and Sparglng
Fly Ash COnveying and Aeration
Gas Boosting
Chip COnveying and
Process Vacuum
Processing and COnveying
Vacuum Extraction and Sparglng
Pothollng and Slurry Recovery
Aeration and Backwashlng
50% Less
Operating Noise
_ 5UJ'OIiIll1lalllll
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The sound data shown compares
the Legend and a comparably sized
blower operating at 3.275 rpm and
12 psig. An improved blower design
significantly reduces the sound
pressure output of the Legend
blower. The typical reduction is
3 dBA which represents 50% less
noise than the competition.
Superior Local Sales and
Service
Our extensive network of authorized
Sutorbilt distributors off'crs the most
convenient local sales and service sup-
port of anyone in the industry today.
These factory trained professionals
are cxperts in blower/vacuum pump
technology providing system installation guidance. troubleshooting and
optimization recommendations of your new or existing applications.
Even a Legendary Warranty
Every Sutorbilt Legend Series blower/ vacuum pump is covered byan
unconditional warranty for 24 months from the date of shipment
or 18 months from the date of installation on all blower materials
and workmanship. Replacement or repair costs will be at no charge.
Contact your Local Sutorbilt Representative for written details.
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High-strength impeller case is heavily
ribbed and machined from a single
piece 01 cast iron and features oversized
dowel pins for precise mounting and
alignment of head plates.
These features result in reduced noise and
more stable, vibration-free operation.
Head plates, machined Irom cast iron,
are ground on the interior surface to
precise operating tolerances. Bearing
lits are machined into head plates to
assure exact bearing positioning.
This ensures accurate, fixed-dimension
clearances through all blower operating
conditions and temperature ranges.
Impellers are machined from cast iron
to an exact profile and are permanently
fastened to steel shafts. They are
dynamically balanced for smooth
operation in any assembled position.
This provides extra strength and rigidity
to handle continuous maximum loads
without fatigue or deflection.
O Anti-friction bearings are used exclusively.
Smaller models are fitted with single-row
ball bearings and cylindrical roller
bearings; large models have double-row
ball bearings and spherical roller bearings.
Optimum bearing selection provides longer
blower I~e and added overhung shaft load
capacity.
€>> Timing gears, precision machined from
alloy steel forgings, are permanently
pinned to the shafts.
This assures non-slip timing even under
the most strenuous loading conditions.
o High temperature Viton~ oil seals.
These maximize the seall~e in continuous,
severe-duty applications to provide
leak-free operation.
O Flex-MountTM design is adaptable to
either vertical or horizontal installation.
The feet are precisely machined and match
the footprints of many
competitive units.
Legendary
Design
Features
e
Timing gears and gear end bearings
are splash lubricated utilizing an
abundant oil reservoir. A graphite
gasketed, oil-tight housing encloses the
timing gears. Drive end bearings are
grease lubricated through fittings. lip,type
seals prevent oil and grease from entering
the impeller chamber.
Superior gear and bearing lubrication is
assured at all operating conditions with mini-
mal maintenance.
High strength steel drive shaft is extended
for V-belt drive or direct connection.
This feature provides greater blower
durability and installation flexibility.
CD
The Legend design accommodates mechanical
gas seals for critical gas applications with
proven results based on a large installed base.
This field proven seal design allows trouble- free
operation in critical gas applications.
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State-Of-The-Art
Quality
Smorbilt Legend blowers and vacuum
pumps are engineered and produced
in Gardner Denver's state-of-the-art
manufacturing facility in Sedalia, Missouri.
This 330,000 sq. ft. plant is ISO 9001
certified and produces hundreds of
different blower and compressor models.
Over the years Gardner Denver has made
significant investments in people and
modern precision machinery. Gardner
Denver's Flexible Machining System
(FMS) assures consistent production of
the highest quality Legend components.
Extra attention to detail is found
throughout the manufacturing process
like the use of advanced coordinate
measuring equipment. Legend compo-
nents are subjected to numerous quality
inspections before they are assembled.
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Prior to leaving the factory,
every Legend is run tested against
rigid standards using our advanced
computer automated testing
equipment.
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The Sutorbilt@ Positive Displacement Cycle
@
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DISCHARGE
A constant volume
of air or gas Is
forced out through
the discharge port.
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INTAKE
A constant volume
of air or gas is drawn
Into the cylinder by
the acllon of the
turning Impellers.
TRANSFER
A constant volume of trapped air
or gas Is transferred around the
cylinder to the discharge porI.
Two specially designed figure-eight impellers turn in opposite directions within a machined
housing, transferring a constant volume of air or gas from the inlet to the discharge with every
rotation of the blower drive shaft. No lubrication within the cylinder is required as the rotating
components are held in close tolerance to each other and do not make contact. The impeller
positioning is maintained by precision timing gears affixed to each impeller shaft. All essential
gear and bearing lubrication occurs externally to the cylinder assuring clean, oil-free gas delivery
under all operating conditions. Compression occurs after the gas leaves the blower and
encounters system resistance in performing its intended work.
Flex-MountTM Design Provides Maximum
Installation Versatility
Horizontal
Contlguralion,
Right Hand Drive
Flex-Mount™ design gives the Legend positive displacement blower and vacuum pump total
application flexibility. It also assures complete interchangeability on existing and new applications
and compatibility as replacements for most competitive installations.
Vertical
Configuration,
BoUom Hand Drive
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Sutorbilt@ LegendH1 Pressure Performance Data
I
2 PSIG
7 PSIG
3 PSIG
4 PSIG
6 PSIG
: : : : :
76 1.1 71 1.6 67 2.1 63 2.5 59 3,0 56 3.5
2".S 91 1.3 86 1.8 82 2.4 79 2.9 75 3.4 72 4.0
102 1.4 97 2.0 93 2.6 78 3.2 86 3.7 83 4.3
162 2,0 157 2,8 153 3.7 149 4,6 146 5,3 1 6.1
14Q l.Q 142 2,8 135 3.7 130 4,5 124 5.2 120 6,1
3LP 2W.S 0.104 202 2.4 194 3.5 188 4.7 182 5,6 177 6.7 172 7.8
3LVP 254 2.9 247 4.3 240 5.5 235 6.8 230 8,2 225 9.6
341 3.7 333 5.3 327 7.1 321 8.9 316 10,6 311 12,4
253 3.0 243 4.5 234 5.7 227 7.1 220 8.5 213 9.9
4LP 3".S 0.170 326 3.7 316 5.3 307 7.1 300 8.8 293 10.6 286 12.4
4LVP 400 4.4 389 6.3 381 8.4 373 10.6 366 12.7 360 14.8
566 5.8 556 8.7 547 11.6 539 14.5 533 17.4 526 20.3
463 5.2 449 7.5 438 10.0 427 12.4 418 14.9 409 17.4
5LP 4".S 0.350 554 5.8 540 8.8 529 11.7 518 14.6 509 17.5 500 20.4
5LVP 673 7.0 659 10.5 648 13.9 637 17.4 628 20.9 619 24.4
6LP 6".F 0.718
6LVP
1,170 1,277 13.3 1,248 20.0 1,224 16.6 1,203 1,184 39.9
7LP 8".F 1.200 1.465 1,631 16.7 1,602 25.0 1,578 33.3 1,557 1,538 50.0
7LVP 1,760 1,985 20.0 1,956 30.0 1,932 40.0 1,911 1,892 60.1
2050 2333 23.3 2304 35.0 2280 46.6 2259 2240 70.0
880 1,366 14.5 1,329 21.8 1,298 29.0 1.271 1,246 43.5
8LP 10",F 1.740 1,170 1,871 19.3 1,834 28.9 1,803 38.6 1,775 1,750 57.9
8LVP 1,375 2,228 22.7 2,191 34.0 2,159 45.4 2,132 2,107 68.0
1,800 2,967 29.7 2,930 44.5 2,899 59.4 2,871 2,847 89.1
9 PSIG
2,800 25 1.7 22 2.1
2MP 1".8 0.017 3,250 33 1.9 30 2.5 28 2.7
2MVP 3,560 38 2,1 35 2.7 34 3.0
5275 67 3.1 64 3,9 63 4,4 60 5.1
1.760 64 3.6 59 4.6
3MP 2".S 0,060 2,265 95 4.6 89 5.8 87 6.4
3MVP 2,770 125 5.5 119 7.1 117 7.9 112 9,5
3600 175 7.2 169 9.2 167 10.2 162 12.3
1,760 144 6.8 136 8.8 132 9.8
4MP 2W-S 0.117 2,190 194 8.5 186 10.9 182 12.1
4MVP 2,620 245 10,2 . 236 13.1 233 14.5
3.600 359 14.0 351 18.0 347 20,0
1.500 237 10.5 227 13.4 222 14.9 19.4
5MP 4",8 0.210 1,760 292 12.3 281 15.8 277 17.5 22.8
5MVP 2,100 363 14.6 353 18.8 348 20.9 27.2
2850 2 1 .9 51 2, 506 28.4 ,9
1,170 332 14.9 316 19.1 309 21.2 27.6 283 29.7
6MP 5",8 0.383 1,760 558 22.4 542 28,8 535 32.0 41.5 509 44.7
6MVP 1,930 622 24.5 607 31.5 600 35.0 45.5 574 49.1
2 0 784 29.9 768 38.4 761 42,7 55.5 735 59.7
1,170 693 28.5 671 36.6 661 40.7
7MP 6".F 0.733 1,465 909 35.6 887 45.8 877 50.9
7MVP 1,760 1,125 42.8 1,103 55.0 1,093 61.1
2.050 1,338 49.9 1,316 64.1 1,306 71.2
8BO 709 30.4 681 39.0 669 43.4
8MP 8".F 1.040 1,170 1,011 40.4 983 51.9 970 57.7
8MVP 1,375 1,224 47.4 1,196 61.0 1,183 67.8
1.800 1.666 62.1 1,638 79.9 1.625 88.7
8 PSIG
lX"-S 0.045
117 10.0 113 11.5
4HP lW-S 0.069
4HVP 124 11.1
192 15.3 188 17.7
5HP 2)o",S 0.140 165 17.5
5HVP 213 20.9
318 28.4
6HP 3".S 0,227 1,760 321 13.3 316 15.1 311 17.0 302 20.8 293 24.6 285 28.4
6HVP 1,930 360 14.5 355 16.6 350 18.7 340 22.8 332 27.0 324 31.1
2350 455 17.7 450 20.2 445 22.8 436 27.8 427 32.9 419 37.9
1,170 332 14.2 326 16.3 319 18.3 308 22.4 297 26.5 287 30.5
7HP 4".S 0.367 1,465 441 17.8 434 20.4 428 22.9 416 28,0 405 33.1 396 38.2
7HVP 1,760 549 21.4 542 24.5 536 27.6 524 33.7 514 39.8 504 45.9
2,050 655 25.0 649 28.5 642 32.1 631 39.2 620 46.4 610 53.5
880 363 16.5 354 18.9 345 21.2 329 26.0 315 30.7 301 35.4
8HP 4".S 0.566 1,170 528 22.0 518 25.1 509 28.3 493 34.5 479 40.8 465 47.1
8HVP 1,375 644 25,8 634 29.5 626 33.2 609 40.6 595 48.0 581 55.3
1.800 884 33.8 875 38,6 866 43.5 850 53.1 B35 62.8 822 72.4
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Sutorbilt@ Legendn1 Vacuum Performance Data
,
2LP 2".S
2LVP 0.035
3LP 211".S 0.104
3LVP
4LP 3".S 0.170
4LVP
5LP 4"-S 0.350
5LVP
6LP 6".F 0.718
6LVP
7LP 8".F 1.200
7LVP
10".F 1.740
2MP l".S 0,017
2MVP
3MP 2".S 0,060
3MVP
4MP 211".S 0,117
4MVP
5MP 4",S 0.210
5MVP
6MP 5".S 0.383
6MVP
7MP 6".F 0.733
7MVP
8".F 1.040
571
690
953
766
1,190
1,312
1,614
1,312
1,666
2,020
2.368
12B 6.0
288 12.2
329 14.5
495 20.0
3.1 17.2 459 20.1
3,6 20.5 578 24.0
4.8 27.9 B40 32,5
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5.9 35.3 1,005 41.2
6.5 38.7 1,127 45.2
7.9 47.2 1,429 55.0
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9.8 59.0
11.5 68.7
9.5 1,860 19,0 1,766 37.9 1,719 47.4 1,670 56.9
11.1 2,217 22,3 2,122 44,6 2,076 55.7 2,026 66.9
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4HP l11".S 0.069 2,190 2.B 95 4,9 91 5.3
4HVP 2,620 3.4 124 5.9 120 6.3
3600 4.6 192 B.l 188 B.7 184 9.3
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5HP 211",S 0.140 1,760 4.6 171 8.0
5HVP 2,100 5.5 218 9.6
2850 7.4 323 13.0 312 14.9
1,170 4.8 159 8.7
6HP 3".S 0.227 1,760 7.4 293 13.0 14.9
6HVP 1,930 8.2 332 14.3 16.3
7HP 4".S 0.367
7HVP
8HP 4".S 0.566 453 24.7
8HVP 569 29.0
809 38.0
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S=Threaded connections sId. NPT. F=f1ange connections. Inlake and outlet connections are same type and size. Dimensions
in inches, weight in pounds. Dimensions for inslallation purposes will be furnished upon request
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Protect your Sutorbilt investment with AEOW PD,
the only lubricant specially formulated for all blowers
. .
m any enVlfonment.
. 100% synthetic for matchless service life.
. Retains its superior lubricating properties a minimum of four times
longer than a premium grade mineral oil at most operating conditions.
. Eliminates seasonal oil viscosity grade changes.
. Superior lubrication in severe, high temperature applications.
. Available from your local authorized Sutorbilt distributor in
convenient sizes to meet your needs.
. Food grade lubricant available.
Retain your Sutorbilt advantage with Genuine Gardner
Denver Replacement Pans.
. Gardner Denver guarantees to supply the proper parts for your specific blower
every time. Replacement pans incorporate the most recent design upgrades.
. All pans meet Gardner Denver original manufacturing specifications and
tolerances for guaranteed fit and function.
. Pre-packaged overhaul kits with detailed service manuals are available from
your local authorized Sutorbilt distributor.
o
Contact Your Sutorbilt Representative
Other Gardner Denver Brochures Available
o
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Gardner
Denver
o
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CVcloBlower XP Series DuroFlow Industrial Series Sutorbllt Methane Gas
Blowers/Vacuum Pumps Blowers/Vacuum Pumps Blowers/Vacuum Pumps
For additional information, contact your local representative or
Gardner Denver Blower Division
100 Gardner Park, Peachtree City, GA 30269
Toll Free 80o-543-n36 ext. 486
Phone 770-632-5000 · Fax 770-486-5629
E-mail: blowersmktg@gardnerdenver.com
Visit our web site: www.gardnerdenver.com
For Parts Information, Contact:
Gardner Denver Blower Division Customer Service
Phone 770-632-5000 · Fax 770-486-5629
Kalwall Panels
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Kalwall", developed and manufactured
in the U.S.A. for over fifty years, is
a highly insulating, diffuse-light-
transmitting material. A matrix of glass
prisms inherent in Kalwall absorbs
external light levels and redistributes an
interior Museum-quality Daylighting™
that virtually eliminates glare, hot spots
and shadows, and by encouraging
natural daylight into the building is
beneficial to health, productivity and
general well-being.
able building component because of
the way it is manufactured and its
material composition. It reduces both
the environmental impact of the build-
ing process and the building's energy
consumption. Importantly, it makes a
substantial contribution to providing a
safer and healthier indoor climate.
No other fenestration or system
matches the performance of Kalwall.
Powerful Advantages
· Maximum Environmental Benefits
. Proven Structural Integrity
· Demanding Fire Code Compliance
· Design and Aesthetic Flexibility
· System Reliability and Integrity...
for over 50 years!
Kalwall's unique composite construc-
tion reduces solar gain, while at the
same time maximizing thermal insula-
tion, with the resultant cost and
environmental benefits.
Kalwall is rated a green and sustain-
Farm Bureau Credit Union, Goshen. IN: Leedy/Cripe Architects
DesignBuilder; DJ Construction Co.. Inc.: Photo by Michael Dailey, Dailey Photo
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The most highly insulating daylighting system in the world!
What Kalwall Is...
The primary element of the Kalwall System is a flat or curved,
structural composite sandwich panel formed by permanently
bonding specially formulated, fiberglass-reinforced translu-
cent faces to a grid core constructed of interlocked, structural
aluminum/composite, thermally broken I-beams.
The natural thermal properties of the sandwich panel can
deliver even greater energy performance by the inclusion of
translucent fiberglass "batts" during the manufacturing
process and by specifying a fully thermally broken grid core.
U-factor options range from .29 to .05 (1.57 to .28 W/m2k)
by NFRC for the 2 '/.' (70 mm) panels.
Kalwall panels are installed with the efficient. proven Clamp-
tite™ aluminum system.
Calpine Corporation:S Metcalf Energy Center; San Jose. CA
Hillier Architecture
Milwaukee Zoo Primate House. Milwaukee, WI
the Zimmerman Design Group. Architects
~' ~A true sandwich panel
Insulation U~value I. for permanency,
options from .53 to .0"5---. ~ ',I," "', "..", ". backed by over 50 years
(2.8 to ,28 W/m2k)- ~ . , II ~" of experience
Light transmission ranges ~~.",lo : ':",I~';;Z: .." ,'I'~I~~,':~I Permanent glass veil
from 3% to 50% '~ -- erosion barrier architec~
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Solar Heal Gain coefficients '---' needs little upkeep
from 1.0 to under ,Q4 .......l.--~
R= Grid core of precision
Fiberglass. aerogel or other ' interiocked l,beams may
insulation in various optional I be thermally broken
densities for extraordinary
insulation Inlerior shatterproof
, faces formulated to meet
Lightweight panel and time. inlerior finish, flame and
proven Clamp-lite installation, smoke requirements of
system installs rapidly lhe toughest codes
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SUPERIOR LOAD CAPACITY
When the wind starts to howl or rain and snow start to accu-
mulate... or if someone walks across a skylight or skyroof. enor-
mous loads push delicate poly-plastic panels far beyond their
limit. Warping, buckling and collapsing result, followed by
extensive interior damage and even bodily harm. Kalwall's
composite panel delivers miraculous performance which can
stand up to hurricane-force winds and other loads with ease.
WEATHERING/COLOR CHANGE: Kalwall's exterior face is
made with innovative super-weathering and colorfast resins
the full thickness... not a low-grade substrate overlaid with thin
plastic film or gel to simulate weatherability. All standard
exterior faces include a permanent glass veil erosion barrier to
prevent "fiber bloom"!..~
Kalwa" Structural Thermal Break Composite
Kalwall's Competing technology
Thermal Break does NOT 7
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. Stronger than aluminum. Passes fire testing to 12000F
. Superior insulation in panels - U-values as low as .05 (.30w/m'k)
. Stops condensation - CRF 80+
www.kalwall.com
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Fletcher Priest Architects
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Hardy Holzman Pfeiffer Associates. LLP. NY
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Knox County Health Department. Mt. Vernon. OH
Manley Architecture Group
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C urtainwalls
Window Replacements
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BCWH Architects: Chris Cunningham Photography
. Rapidly and economically enclose space
- totally pre-finished when in place.
. Epitomizes the original Kalwall
translucent sandwich panel concept.
. Controlled, natural daylight combined with
finely tuned thermal and solar controls.
. May be either flat or curved
sandwich panels.
. Structural Sandwich Panels up to 5'
x 20' (1500 mm x 6000 mm), 2X"
(70 mm) or 4" (100 mm) thick are
secured to building with simple,
Clamp-titen, aluminum extrusions.
System seals panel/panel and build-
ing, allowing for expansion/contraction
and proper weepage to channel any
moisture to building exterior.
. Factory-assembled 2'X" (70 mm)
sandwich panels, operating/fixed
windows, louvers, even opaque panels.
. Provide rapid installation and
permanent weather seal, unlike
mqst stick-built, "frame and glaze"
components which are all field-
assembled.
. Kalwall prefabricated Curtainwall
Systems, like our Panel Wall Systems,
are totally pre-finished inside and out.
. Delivered to the job site in large
preassembled units up to 5' x 35'
(1500 mm x 10700 mm) and larger.
. Kalwall heavy-duty Window
Replacement Systems - like our
prefabricated Curtainwall Systems -
are factory-assembled into easily
managed building units.
. Kalwall provides optimum performance-
controlled daylighting and still allows
for fulfillment of vision/ventilation
requirements.
. Vandal, graffiti, and impact resistance
add up to minimal maintenance
expenses with Kalwal!.
Wall Systems
Urban Peak. Denver, CO
Florin Group, Architects
C urtairiwall
Systems
Central Library - University of
Southern Maine. Portland. ME
]SA. Inc.. Architects
Replacement
Window Systems
Beach Park Elementary School
Beach Park. IL
www.kalwall.com 5
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Building. Beverly Hills. CA
Gwathmey Siegel & Associates
Architects; Tom Bonner
Photography
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. 2Y." (70 mm) thick flat Skylights up to
5'0" x 20'0" (1500 mm x 6000 mm).
. Pyramids from 4' (1.2 m) square up to
60' (18 m) square.
. Geo-Roof'" units in 21 standard-sized
units from 8' to 24' diameter
(2440 mm to 7315 mm).
. Available knocked down or
prefabricated.
. Centerline self-supporting ridges with
20', 2T, 33',45', slope to 24'.
. Kalcurve™ 180', Low-Profile 90' in l'
(300 mm) curb width increments.
. Lightweight - less than 3 Ibs. per
square foot (145 Palm') means sub-
structure may be minimized. Only
thrust-bearing curbs designed to
accommodate local live, snow and
wind load designs are required.
. Sandwich Panel Systems over sub-
structure designed and installed by
others.
. Flat, curved or combination for design
versatility and consistent with all
Kalwall Systems.
. Easy, fast installation, coupled with
large-sized panels to eliminate
troublesome joints.
Savannah High Schooi. Savannah. Georgia
Hussey Gay Bell & DeYoung Architects
John F. Nuner Elementary School. South Bend. IN
Hebard & Hebard Architects; hilliardphoto.com. Photography
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Photo @ Richard Sexton
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Structures
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. Combinations of sandwich panels.
glass and framing components.
. Standard modular walkways.
1\1 EVIl!
· Fully pre-engineered canopies
and walkways, including
aluminum structure, are now
available!
. Taking Kalwall sandwich panel tech-
nology to another dimension... the
marriage of aluminum box beams and
Kalwall panels into a monolithic,
structural space enclosure.
. Variety of designs, unequaled by any
other daylighting system.
. Design control, fabrication, delivery
and complete installation for the ulti-
mate in single-source responsibility!
. Installations completed in weeks - not
months - due to component standard-
izations and CAD technology.
. Complete buildings, including Pool
Enclosures, featuring non-corrosion
and moisture resistance built-in.
. Thermal break technology for the
ultimate condensation control.
Walkways
& Canopi~s
VA Medical Center Walkway
Little Rock, AK; Cromwell
Truemper Levy Thompson
Woodsmall. Inc.. Architects
Gary W Stone. Photography
Structures
& Large Systems
Life Time Fitness Centers
Don Pitlik. Photography
Kalwalr
Structures Unlimited
Kalwall, with strategic partner Structures Unlimited,
Inc., offers a single-source solution to self-supporting
systems with clears pans over 150 feet.
Pre-engineered, custom-fabricated aluminum box
beam structures are combined with Kalwall panels to
create a total composite Skyroof™ System or even an
entire building.
www.kalwall.com 7
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For 20/4" (70 mm) vertically oriented panels.
These are standard Clamp-tite™ details. Systems for other
conditions, e.g., horizontally oriented, concealed fastener,
Kalcurve™, Explosion Venting or Blast Resisting, are similar,
but do contact Kalwall for specifics. High,performance coat-
ings in Kalwall Corrosion Resistant Finish are standard, CAD
versions of these details and more available at
www.kalwall.com.
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KALWALL SPAN TABLE - 4' (1200 mm) MODULE
Maximum Allowable Clearspan
Translucent Panel Unit Nominal
Panel Wall Grid Size
2" (51 mm) Batten
2'1" (70 mm) ST. #4SSSE
3'1" (83 mm) IS-H
Silhouette Stiffener
12'-8" (3860 mm) 12'-5" (3785 mm) 12" x 24" (300 mm x 600 mm)
16',7" (5055 mm) 16',5" (5005 mm) 12" x 24" (300 mm x 600 mm)
20'-11" (6375 mm)20'-9" (6325 mm) 12" x 24" (300 mm x 600 mm)
25'-0" (7620 mm) 24'-11" (7595 mm) 12" x 24" (300 mm x 600 mm)
Clearspan at 25 p.s.f. (1.2 kPa) wind pressure, L16D minimum. Spans based on
engineering data and tests. Others possible. CAUTION! Spans will vary with panel
internal grid core size and orientation. Above based on grid oriented the panel length.
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CAD Details!
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thermally broken options.
All Kalwall windows are
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Blue items are
field-installed
and may require
trimming.
WALL ELEVATION
1(!It~)1
KAlWALL SEALING
TAPES TYPICAL
ALL JOINTS
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3/4"
(19 mm)
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Shed/Supported Ridge Skyroof™ Details
For 20/." (70 mm) vertically
and horizontally oriented
flat panels.
SUPPORT AS
REQUIRED BY
OTHERS
SKYROOF PLAN A SKYROOF PLAN 8
PANELS ON SLOPE - 2. BATTEN PANELS ACROSS SLOPE - OVERlAP SYSTEtJ
Details for other conditions, e.g.,
Kalcurve™, self-supporting ridge,
pyramid, hurricane or blast resistant,
are similar, but not identical so be
sure to contact Kalwal!.
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Factory-sealed
perimeter frames.
3 38
4
MAX B'-O" MAX B'-O"
(243Bmm) (243Bmm)
OPENIN SUPPORT
G-OUTSIDE CURB
OPTIONAL THERMALLY
BROKEN HALF RIDGE
AVAIlABLE
SPAN GUIDE CHART: 2'1." (70 mm) Skyroof
5' (1500 mm) module: B" x 20" (200 mm x 500 mm) grid
Live Load I 30 Ib.lfl.' (1.44 kPa) I 40 Ib.lfl.' (1.92 kPa)
Clearspan 111'-9" (3581 mm) I 10'-9" (3277 mm)
5' (1500 mm) module: 12" x 24" (300 mm x 600 mm) grid
Clearspan 110'-3" (3124 mm) I 9'-1" (2769 mm)
....!E
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Clearspan @ 25 p.sJ. (1.2 kPa) wind pressure, U60 minimum.
Note: Longer clears pans possible. Contact factory.
RECOMMENDED MINIMUM PITCH Skyroofs (field-installed
panels) 2":12" (1:6)
Note: Exposed metal systems available in mill finish or Kalwall
Corrosion Resistant Finish per AAMA 2604. Special finishes
available as options.
IX" COUNTER FlASHING
\!Y NOT BY KALWALL
'0 SUPPORT NOT
\V BY KALWALL
191 STANDARD
\b FlASHING BY
KAlWAll
5/B"
(16mm)
,{ANEL DIM I I PANEL DIMt-
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NOTE:
PLEASE CHECK WITH
FACTORY FOR
ALLOWABLE SPANS
IN YOUR LOCALE
USING THIS 3W I.S.
www.kalwa/l.com 9
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Designing
PANEL-UNIT WALL:
COMPONENTS
[
Factory-preassembled in any combination up to 5' wide x 35' high
(1500 mm x 10700 mm). Panel-units ready for installation with no addi-
tional finishing. Panel-units eliminate superfluous structure required with
most other systems.
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LOUVERS - WALL SYSTEMS
Specify Kalwalllouver as required.
[
THERMAL BREAK SASH
Kalwall-manufactured, AAMA C-lO or HC-70 tested projecting sash for
top performance up to 5' wide x 4'6" high (1500 mm x 1400 mm). Fixed
and egress units also available. Glazing of all types, including 5/a"
(16 mm) and 1" (25 mm) thick glazing panels available; factory-
installed, if specified.
[
[
OPAQUE PANELS
Sandwich panel construction with fiberglass, aluminum or other faces
can be combined in the same system for aesthetic value or to fine-tune
energy performance.
[
PANEL OPTIONS
STANDARD PANEL SIZES
Width - 4' and 5' (1200 mm
and 1500 mm), other widths up
to 5'0" (1524 mm) are optional.
Length - 3' to 20' (914 mm
to 6096 mm) standard, 16' (4880
mm) maximum for skyroofs.
Thickness - 4" (100mm), 2W'
(70 mm). 19/16" (40 mm) and 1"
(25mm) for window glazing only.
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STANDARD GRID DESIGNS
Nominal grid size - 12" x 24"
(300 mm x 600 mm) standard;
8" x 20" (200 mm x 500 mm)
optional for flat and curved panels.
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OPTIONAL GRID DESIGNS
Other designs and grid sizes
available. Please note that
spans will vary with different grid
patterns. Consult factory.
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TRANSLUCENT COLORS
White and Crystal are standard
but other colors are available.
The Kal-tint series and pebble
finish are options. Colored
translucent insulation inserts are
available in an endless palette
of colors.
[
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METAL FINISHES
The installation system is avail-
able in mill finish or Kalwall
Corrosion Resistant Finish, a
high-performance coating that
meets AAMA 2604, 2605 option-
al. The finish is highly resistant to
acids. alkalis, salt, industrial and
moisture-laden atmospheres.
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STANDARD GRIDS
REVERSE SHOJI
OPTIONAL GRIDS
VERTI-KAL
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Installation
QUICK, LOW-COST
Kalwall interconnected structural compo-
nents form rigid. modular units which
replace the heavy mullions and floating
panels of other curtainwalls. The unique
construction and extreme structural
strength of the components permit the
largest panel-unit wall sections to be
installed quickly and efficiently.
DaD and GSA
ANTI-TERRORISM
TESTED AND APPROVED!
UFC 4-010-01
BLAST-RESISTANT CONSTRUCTION
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Merry Hill Centre. West Midlands. UK
TNC Design Associates. Architects
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Technical Summary
Kalwall is a composite sandwich; various combinations are pos-
sible and test data should be interpreted from this point of view.
Consult Sales Service Department for further clarification.
HEAT & LIGHT TRANSMISSION: Listed below are the light
transmissions, solar heat gain coefficients, and U-factors for some
23f4" (70mm) thick Kalwall panel face sheet combinations. Others
are available. Highlighted values indicate thermally broken panels.
FACE SHEET % LIGHT TRANSMISSION note 1 SKYROOF SOLAR HEAT GAIN WALL SOLAR HEAT GAIN
COMBINATIONS COEFFICIENT @Oo L. note 3 COEFFICIENT @350 L. nole 3
EXTERIOR INTERIOR .53 'U. .29/.23 .22 1.14 .18/.10 l&~ .53 'U' .291.23 .22/.14 .18/.10 .05 .53 "U" .29 1.23 .221.14 .18/.10 .05
COLOR COLOR "U' "U" "U' "U. 'U' 'U" "U. 'U' "U' "U" 'U"
note 2 note 2 note 2 "ole.2 note 2 note 2 note 2 nole 2 note 2 note 2 note 2 note 2
Greenish Blue White 25 14 5 3 I 10 0.37 0.18 0.10 0.07 0.11 0.36 0.17 0.10 0.06 0.11
Aqua White 29 17 6 4 12 0.37 0.19 0.10 0.07 0.11 0.36 0.18 0.10 0.06 0.11
Rose White 30 18 6 4 I 12 0.38 0.19 0.10 0.07 0.11 0.37 0.18 0.10 0.06 0.11
Ice Blue White 35 20 8 6 I 15" 0.44 0.22 0.11 om 0.12 0.44 0.21 0.10 0.06 0.12
Greenish Blue Crystal 37 20 7 4 I 15 0.47 0.21 0.13 0.08 0.13 0.45 0.21 0.12 0.08 0.13
!
White White 20 15 8 5 I '12 0.30 0.16 0.09 0.06 0.09 0.30 0.15 0.08 0.05 0.09
Crystal White 35 20 12 8 I 15 0.42 0.23 0.11 0.07 0.11 0.39 0.19 0.10 0.06 0.11
Crystal Crystal 50 30 15 10 20 0.55 0.27 0.14 0.09 0.12 0.51 0.23 0.13 0.08 0.12
~ ~~~~.
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De Ferrers Specialist Technology College, Burton upon Trent, UK
Aedas Architects Limited
SPECIAL APPROVALS & LISTINGS:
. FM Explosion Venting Walls standard 4440
. FM Wall and Roof Systems standards 4881 and 4471
. Hurricane-Resistant Systems
. NFRC Certified Products Listing
. UL Listings for Class A Roof System and Faces
. UFC 4-010-01 000 Anti-Terrorism Specifications
Kalwall-188-
NEW Kalwall4" (100 mm) thick panels for even greater energy and structural performance I
FACE SHEET O/OUGHT WALL SOLAR HEAT ROOF SOLAR HEAT
COMBINATIONS TRANSMISSION GAIN COEFFICIENT GAIN COEFFICIENT
EXTERIOR INTERIOR .08 .15 ,55 .08 .15 .55 ,08 .15 ,55
COLOR COLOR 'U. .U. 'U. 'U" 'U. 'U' "U. 'U. "U.
Crystal Cryslal 8 17 50 0.08 0.18 0.50 0.09 0.21 0.56
Crystal White 7 . 14 35 0.08 0.15 0.39 0.08 0.18 0.43
White White 5 ' 12 20 0.05 0.12 0.29 0.06 0.14 0.33
U.value SI conversion: 1.0 w/m'k = 0.176 BTU/(hrfl"'F)
1. Approximate vatues by ASTM E.972. Light transmission values over 30% not
recommended for most applications.
2. U-values determined by NFRC test method (ASTM C.236, E.1423 and C.1199 at certified
lab). Expressed as BTU/(hrlt""F) for atuminum grid I thermally broken grid, nominal 120 x
240 (300 mm X 600 mm). Perimeter aluminum excluded. Test temperature at 15 mph wind
(6.7 mls): O"F (.la'C) cold side & 70"F (21"C) warm side.
3, Shading Coefficient (SC) is equal to 1.15 times the Solar Heat Gain Coefficient (SHGC).
NFRC CERTIFIED SYSTEMS: Kalwall systems provide
the best overall U-values as low as .10 (.56W/m'K)!
BOND STRENGTH: Panels and adhesives are tested accord-
ing to the stringent requirements of "Criteria for Sandwich
Panels" issued by ICC (International Code Council). Before
specifying an alternate, insist on actual field proof of bond
integrity over a 20-year period. Caution is urged in accepting'
look-alikes as equivalents.
WEIGHT: Most panels and systems weigh under 3 p.s.f. (14.65
kg/m2).
FIRE TESTS: Although some Kalwall panels contain com- __ '
bustible binder resins (ignition temperature greater than 8000F),~.~<:!
they will withstand a 12000F flame for one hour with no flame ',',. ,
penetration; pass the Class "A" Burning Brand Test (ASTM E-'
108), or UL 790 listed Class A Roof system. All interior faces
are CC-1 by ASTM 0-635. Optional flame-spread/smoke devel-
oped ratings by UL 723 tunnel tests, including Class A, are
available. Kalwall is listed by: lCC #PFC-1705; British Standard
476, Parts 3, 6, 7. NFPA 268 - Radiant Panel Test-Exterior Walls.
Whenever reference is made to fire tests, the numerical rating is not
intended to reflect hazards presented by this or any other material
under actual fire conditions.
IMPACT: The shatterproof exterior face will withstand 70 ft.-Ibs.
(81J) impact. Optional extra-hi-impact faces will withstand 230
ft.-Ibs. (311J) impact by UL 972; also small and large missile.
www.kalwall.com 11
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Davis PE & DiJ~ StudiO f11~~Mmpton, University. London, UK.
Inset: New,york Hall o($!:I~!#. "Queens, NY; Polshek Partnership Architects
-
1111 Candia Road. P.O. Box 237, Manchester, NH 03105
Phone: 603-627-3861 Fax: 603-627-7905
www.kalwall.com
For immediate assistance call: 1-800-258-9777 (N.America)
or e-mail: info@kalwall.com
Inguires for the UKlEU. contact www.stoakes.co.uk
KalwaIl Corporation Is engaged In continuing research to Improve Its products.
Therefore. the right Is re5elVed to modify or change matertal In this brochure
without notice. This Is descriptive literature and does not constitute warranties.
expressed or implied. For statement of warranty contact KalwalI Corporation.
U.S. Pat Nos. 2,931.468 - 2.981.382 - 3.082.848 - 3,082,849 - 0196,778 -
0198,259 - 0199,524 - 0199,525 - 4,129,973 - 4,557,090 and Pats. Pend.
www.kalwall.com
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Reclaim
0.7 Feet
1.0' Feet
()
o
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From Filters
o
P-SL-2 P-VVVVR-2
P-Sl-3 P-VVVVR-3
Reclaim Tank 2
Reclaim Tank 3
V-NP-2
V-VVW-5
North
From Distribution
t><l
V-NP-l
-----.-~~~~,J]'
~--~~---
~- ---- --
Reclaim
Setpoints
~_.. "
Reclaim
.~_~t:~__
Reclaim
Process Values
Reclaim
Process T irners
Recl5n
AI!rm Config
1:~~~~Iii\,.. ,}i~i~'._:%.~'..,~~.~__,.} =~ ~ ~~_~ -..f
II ... ...-- Potassium Perrnanganate
I M-PPM-1 M-PPM-2 To Aerator
Effluent
1
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550 Gallon
Mix Tank
I ~j'Gall
T-PPM-1
Ruoride
Transfer Pump
360 Gallon
Storage
Tank
550'Gallon
Feed tank
r.4 't..~~
,I 55 Gall
T -PPM-2
165 Gallon
Tank
L
P-PPM-1
''.1.;-
P-PPM-2
Break Tank
P-FL-2
Sodium Hypochlorite Feed System
G
1700 Gallon
Storage Tank
1700 GallOn
Sta"age Tank
, ""'d
11375 Gall
P-CL -1
P-CL-2
P-CL-3
P-CL -4
To Detention Tank
Effluent
To Finished
Water
To Distribution System
To Infuent For Filters
To Aerator Effluent
To Filter Infllent
To Reclaim RetLm
To Filter EfftJent
..
ldr~~
Polyphosphate Feed System
To Distribution
System
155
Gallon
Tank
Polymer Feed System
Polymer Mix / Feed Unit
o'~
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To Filter
Influent
55
Gallon
Tank
f Chemical Feed
Device Status
Chemical Feed
Process Values
-----
Chemical Feed
Process Setpoints
.. .-
Chemical Feed
I Process Timers
Chemical Feed
Alarm Config
'1"~~."......,; ~,... .-'IWllll......-. ~,~,' .JIIr......."1..~._.._"QlIlW..... "'L"jVst.er-' ~ ~ l.
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Flter 1 Backwash Sequence Flter 2 Backwash Se~e
IsemlAu~1 ,ISem~1 ,',', ,
~_[BJ~_~
Flter 3 Backwash Secpmce
ISem~1
8_~
Flter " Baclcwash Sequence
ISemlAutol
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Process
, , Units Value lXllts
! Reclaim Purrp 1 RLIl Time I-b.rs 57. Slldge Disposal Pump 3 Run Time Today Min.rtB
I
), Reclaim Purrp 1 RLIl Time Today Mlrute O. RetIrn Flow FE-5 GPM
,. Reclaim Purrp 2 RLIl Time Hours RetIrn Flow FE-5 Total kGaI
j:
': Reclaim Purrp 2 Run Time Today RetIrn Flow FE-5 Total Today
Mirute O. kGaI 0.0.
Reclaim Purrp 3 RLIl Time Holrs
1! Reclaim Pump 3 Run Time Today Minute O.
Reclaim Tank 1 Level Feet
~eclaim Tali< 1 Nurrber ofSkJdge Disposal Purrp Starts
! Reclaim Tcrk 1 Settling RLIl Time Hours
Reclaim Tcrk 2 Level Feet
Reclaim Tcrk 2 Number OfSlldge Disposal Pump Starts
Reclaim Tcrk 2 Settling Rl.I"l Time Hours
I Reclaim Tarl< 3 Level Feet
Reclaim Tn 3 Number Of Sludge Disposal Pump Starts
Reclaim Tcrk 3 Settling RlI'l Time Holrs
SkJCIge Disposal Purrp 1 Run Time Hours
SkJdge Disposal Purrp 1 RlI1 Time Today Minute
Sk.Idge Disposal Purrp 2 RlI1 Time Hotrs 95.
Sludge Disposal Purrp 2 RLIl Time Today Mlrute
Sludge Disposal Pump 3 RlI1 Time Holrs 158.0
~ LJ ["J r:J r-J rJ ::-J r:-:J r-:J r::J r:J r-1 r-1 ~ :---J iJ r:J c-1 ~]
1
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FIIt!i 1 Ai"wam VaNe V-AW-5 Open Fail To Cbse
Filter 1 Airwash Valve V-AW-5 Open Fail To Open
Filt!!r 1 Bad<wash Valve V-eW-5 Open Fall To Close
Filter 1 Backwash Valve V-BW-5 Open Fail To Open
Filter 1 Eff\Jent; 'laM! V-FE-l Open Fall To Close
Filter 1 Eff\Jent Valve V-FE-l Open Fail To Open
Filter 1 Infllent Valve V-FI-l Close Fail To Close
Filter 1 tlftJent Va~ V--FI-l Close Fatl To Open
--
Filter 1 Level Hkil Limit
Filter 1 Level Low Limit
Flbr 1 [)rain Valve V-f'O-32 Open fail To Close
Filter 1 Drain Valve V-PD-32 Open Fail To Open
Filter 1 Waste Vl!h! V-'mJ-l Open Fa~ To Close
Filter 1 Waste Valve V-WW-l Open Fail To Open
Flh!lr 2 Arwam Valve V-AW-(i Open FaM To Clo6e
Filter 2 Airwash Valve V-AW-6 Open Fail To Open
Fllt:1r 2 8ad<wash Vahle V-aW-6 ~ Fall To Cbse
Filter 2 Backwash Valve V-BW-6 Open Fail To Open
Fllt!r 2 Effl.Jent Valve v-FE-2 Open Fall To Close
Filter 2 Effi.J8nt Valve V-FE-2 Open Fall To Open
II
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Filter 2 Infk.Jent Valve V-FI-2 Close Fall To Close
Filtsr 2lntUiint Villve V-fl-2 CIoie Filll To ~
Filter 2 Level Hkj'l Limit
Filter 2 Level Low Limit
filtar :2 Crain V~ V..po..33 0pQn Fad To Close
Ftlter 2 Drain Valve V-PD-33 Open Fail To Open
Filtar 2 Wasts Va!VQ V-WtN-2 0pQn FilN To Close
~-~
Filter 2 Waste Valve V-lMN-2 Open Fail To Open
- ---..-.. -.- --
Alarm Auto Dialer Alarm I
Enable Charnel Dela
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8:30:54 AM 8:45:54 AM 9:00:54 AM 9: 15:54 AM,
~.........~~ ,11/9/2006 ~ 11/9/2006 1<'1/9/2006
'Filter 2'leveL{f1let}
FIlte!r;.,~teveL{feet}'
,CFllter4 L:evel{feet}.
Reclaim Ta('k :t-itevel {~t}
Racial m T ani<. 2 Level {Feet}
'P,eel.:=ii ro Tarilk-3:1h:~iiei {Fe~l;}
11 9 2006
8: 15:54 AM
11/9/2006
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tr~tleal- n Clear Ad
Chemical Feed System
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page
03
Consistent and Reliable Chemical
Storage for Versatile Applications!
· Maximum Corrosion
Protection
· Seamless, One-Piece
Design
· Impact Resilient
· Maintenance Free
· Improved Product
Life Cycle
Molecular Bonding Makes the Difference:
Crosslinked
Polyethylene
Linear
Polyethylene
--
..---
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--
Poly Processing Company... Providing Solutions Through Innovation
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Vertical Tanks
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Vertical Tanks
F.O.B. Approx.
Stock Nominal Approx. Overall Lid Size Ladder
LA VA CA Number Capacity 0,0, Height Height
. 1 1014950 14,950 14'-0" 16'-10" 24" 14'
L . 4 1012250 12,250 11'-11" 17'-1 " 24" 17'
. 1 1012150 12,150 12'-0- 10'-8- 24" 10'
L . 4 1010300 10,300 11'-11" 14'-6" 24" 14'
. 1 1010300 10,300 12'-0" 14'-4" 24" 13'
. 1 1009200 9,200 10'-0" 17'-8" 24" 17'
. 1 1009100 9,100 12'-0" 12'-11" 24" 12'
L . 4 1008500 8,500 10'-0" 16'-9" 24" 16'
L . 4 1008200 8,200 11'-11" 11'-11" 24" 12'
. 1 1008050 8,050 10'-0" 15'-8" 24" 15'
L . 4 1008000 8,000 9'-2" 18'-6" 24" 18'
. 1 1007900 7,900 12'-0" 11'-11" 24" 11 '
L . 4 1007300 7,300 10'-2" 14'-2" 24" 14'
. 1 1007100 7,100 12'-0" 10'-11" 24" 10'
. 1 1007000 7,000 10'-0" 13'-9" 24" 13'
L . 4 1006600 6,600 11'-11" 10'-1" 24" 10'
L . 1 1006600 6,600 14'-0" 9'-1" 24" 6'
L . 4 7 1006150 6,150 10'-2" 12'-4" 24" 12'
L . 4 1006100 6,100 8'-6" 16'-4" 24" 16'
L . 1 1006100 6,100 10'-0" 12'-8" 24" 12'
L . 4 7 1005300 5,300 9'-2" 12'-10" 24" 13'
L . 1 1005100 5,100 10'-0" 10'-10" 24" 10'
L . 4 1005050 5,050 7'-10" 16'-0" 24" 16'
1 1004925 4,925 9'-0" 11'-11" 24" 11'
. 1 1004900 4,900 12'-0" 8'-1" 24" 6'
. 1 1004400 4,400 9'-0" 11'-4" 24" 11'
L . 4 1004250 4,250 11'-11" 7'-0" 24" 7'
L . 7 1004150 4,150 8'-6" 12'-6" 24" 12'
. 1 1004050 4,050 8'-2" 12'-10" 24" 12'
L . 4 1004050 4,050 8'-6" 11'-5" 19" 11 '
L . 4 7 1003900 3,900 7'-10" 12'-9" 24" 12'
L . 7 1003850 3,850 10'-2" 8'-6" 24" 8'
. 1 1003650 3,650 10'-2" 8'-5" 24" 6'
. 1 1003000 3,000 6'-1" 15'-7" 19" 15'
L . 4 7 1003000 3,000 7'-1 " 11'-8" 24" 12'
1 1002850 2,850 7'-6" 10'-7" 24" 10'
L . 1 1002800 2,800 10'-0" 6'-11" 24" 6'
. 1 1002750 2,750 8'-2" 9'-4" 24" 9'
L 4 7 1002650 2,650 8'-0" 8'-9" 24" 8'
L V 4 7 1002550 2,550 7'-1 " 10'-4" 24" 10'
1 1002500 2,500 8'-0" 8'-2" 24" 8'
. 1 1002400 2,400 6'-1" 12'-8" 19" 12'
L 4 7 1002250 2,250 8'-0" 7'-9" 24" 7'
1 1002000 2,000 7'-5" 7'-5" 19" 7'
L V 4 7 1002000 2,000 7'-1 " 8'-6" 24" 8'
7 1001950 1,950 5'-4" 13'-5" 10"/19"
1 1001700 1,700 6'-1" 9'-7" 17" 9'
4 7 1001700 1,700 8'-0" 6'-2" 24"
1 1001550 1,550 5'-1" 11'-9" 17"
High Density
Crosslinked (HDXLPE)
ranging from 30 to
14,950 gallons
Specify HDXLPE tanks
with OR-1000™ for
increased chemical
resistance and longer
tank life (page 6)
page
09
IMF01! for full drain
system (page 5)
SAFE-TANKe double-wall
containment system
(page 4)
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Molded-in Lifting Lugs
Tank Drawings available on website
L = Molded-in Ladder Attachment Lugs . = Moldecl-in Uftlng Lugs V = Molded In Uftlng Lugs - Virginia Only .= F.O.S. for 1.9 or > Specific Gravity
Poly Processing Company... Providing Solutions Through Innovation
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Vertical Tanks (continued)
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Flexible connections
required to preserve
warranty; allows for tank
expansion / contraction
and to reduce pump /
piping vibration stress
on the tank
(page 25)
Fittings & Accessories
(pages 21-27)
Vertical Tanks (continued)
F.O.B. Approx.
Stock Nominal Approx. Overall Lid Size Ladder
LA VA CA Number Capacity 0,0. Height Height
4 1001450 1,450 7'-2" 6'-2" 10/16/22"
1 1001400 1 ,400 7'-5" 6'-3" 17" 6'
4 7 1001400 1 ,400 5'-4" 10'-0" 1 0"/19"
1 1001350 1,350 7'-5" 5'-5" 19"
4 7 1001300 1,300 7'-1 " 5'-10" 10"/19"
1 1001300 1,300 7'-8" 5'-6" 17"
1 1001250 1,250 7'-0" 6'-0" 17" 6'
4 7 1001150 1,150 5'-4" 8'-2" 1 0"/19" 8'
1 1001100 1,100 6'-1" 6'-10" 17" 6'
1 1001090 1,090 5'-1" 8'-6" 17" 8'
1 1001080 1,080 7'-8" 5'-0" 17"
7 1001050 1,050 5'-1" 8'-6" 17" 7'
4 1001000 1,000 7'-2" 4'-8" 10"/19"
1 1000950 950 5'-4" 7'-3" 17" 6'
4 7 1000905 905 5'-4" 6'-9" 1 0"/19" 6'
4 7 1000805 805 4'-0" 9'-11 " 1 0"/19"
4 1000755 755 5'-4" 5'-9" 10"/24"
7 1 1000685 685 5'-1" 5'-4" 17"
1 1000680 680 4'-0" 8'-6" 17"
7 1 1000615 615 4'-0" 7'-9" 17" 7'
1 1000540 540 4'-0" 7'-0" 17" 6'
4 7 1000540 540 4'-0" 6'-9" 1 0"/19"
4 1 000495 495 5'-4" 4'-0" 1 0"/19"
7 1 1000475 475 4'-0" 6'-3" 17"
4 7 1000450 450 3'-10" 6'-1 " 7"
7 1000400 400 3'-9" 5'-3" 8"
1 1000385 385 4'-0" 5'-4" 17"
1 1000325 325 4'-0" 4'-8" 17"
7 1000320 320 4'-0" 4'-8" 1 0"/17"
7 1000300 300 3'-6" 4'-3" 8"
4 7 1000295 295 3'-10" 4'-5" 7"
4 7 1000281 281 2'-10" 7'-0" 7"/10"
4 1000280 280 2'-10" 7'-0" 7"
1 1000280 280 2'-10" 7'-0" 7"/10"
7 1000235 235 2'-10" 5'-11 " 10"/17"
1 1000235 235 2'-6" 7~4" 12"
1 1000230 230 3'-2" 4'-11" 17"
7 1000230 230 3'-2" 4'-11" 1 0"/17"
4 7 1000205 205 2'-7" 6'-2" 7"
7 1 1000175 175 3'-2" 4'-0" 17"
4 7 1000155 155 2'-7" 4'-9" 7"
4 7 1 1000115 115 2'-6" 3'-11" 12"
7 1000110 110 2'-9" 2'-9" 12"
4 7 1000100 100 1 '-11" 5'-7" 7"
1 1000095 95 1'-11 " 5'-4" 12"
4 1 1000070 70 1 '-11" 4'-1" 12"
4 7 1000060 60 1'-11 " 3'-6" 7"
1 1000055 55 1'-11 " 3'-5" 12"
4 1 1000030 30 1 '-11" 2'-2" 12"
1-866-590-6845 · www.polyprocessing.com
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The PULSAR HypoPump@ is
specifically designed to meter the full
range of concentrations of Sodium
Hypochlorite and its vapors. The
patent-pending design allows
pressurized process fluid to cyclically
flush liquid and vapors through the
pump's discharge check system while
maintaining high performance and
chemical dosing accuracy.
Sodium Hypochlorite Metering Pump
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KEY FEATURES:
. Automatically evacuates air and
vapors from the reagent head
. Completely integral to the pump
closed loop vapor-handling system
. Requires no external valves or
tubing for removal of vapors
. Self-priming feature aids in quicker
and more efficient start-ups
. No sacrificial parts like tubing or
stators to replace in frequent
intervals
Nominated numerous times for The
Most Innovative Product of the Year
Award and praised on many
occasions for it's gas handling
design, the PULSAR HypoPump@
has provided solutions for
customers with difficult gassing
problems. Time and again
PULSAR@ has stood apart from the
competition. When looking for
answers to your applications, go
green, go PULSAR@.
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Performance Specifications:
Pump Rated
Model & Maximum Capacity Range
Head Size Pressure
Includes all 60 HZ 60 HZ 50HZ 50 HZ PSIG BAR
stroking rates GPH LPH GPH LPH
25HJ
A Head 0,69 - 2.0 2.6 - 7.7 0.57 - 2.1 2.1-7.9 150 10.4
25HJ
B Head 1.1-7.3 4.3 - 27.9 0.9 - 7.5 3.S - 29.7 150 10.4
25HJ
C Head 6,1-32,7 23,4 - 123,8 5.1 - 33,6 19.3 -127.4 150 10.4
25HJ
D Head 17,1 - 51.1 64,9 - 193.5 14.1 - 52.6 53.7 - 199,1 150 10.4
25HL
B Head 1.4 - 7.2 5.4 - 27,3 1.1-7.4 4,4 - 28.1 150 10.4
25HL
C Head 5.1 - 38.5 15.5-145.7 4.2 - 29.6 16.2 - 149.9 150 10.4
25HL
D Head 22.9 -106.9 86,8 - 404.7 19.0 -110,0 71.9-411.4 87/56 6/4
55HL
B Head 1.4 - 7.2 5.4 - 27,3 1.1 - 7.4 4.4 - 28.1 150 10.4
55HL
C Head 5.1-38.5 15.5 -145.7 4.2 - 39.6 16.2 -149.9 150 10.4
55HL
D Head 22.9 -106.9 86.8 - 404.7 19.0 -110.0 71.9 -416.4 150 10.4
These pumps are available with PTFElelastomer comoosite, PTFE solid, and leak detection diaohraoms,
Standard Features:
. Three component valves
. Four bolt tie bar design
. Stainless steel hardware on liquid end
. Steady-state accuracy of +/- 2%
. NEMA 4X & IP65 enclosure rating
. Manual stroke length adjustment
. 115 or 230 V AC, single phase power
Optional Features:
. Microprocessor based controllers
. MODBUS serial communication
. PULSAlarm@ leak detection system
. Multiplex systems for Chloramination
. Stainless steel base
IIIIMUIIL ENlDIIIIl
.,.- -""-----
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rl.....~
Approximate Overall Dimensions:
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The closed-loop vapor handling system utilizes a pressure balanced flapper valve
which opens periodically to allow fluid from the discharge line to bypass the
discharge check valve and flow back into the reagent head forcing the vapor and air
out of the head to keep it from losing prime, The flapper valve is actuated by a
solenoid, which is controlled by a solid-state timer. The flapper valve can also be
manually actuated,
Liquid End Materials of Construction:
IlODEL 25 IlODEL "
OIH INCH ... INCH ...
L Zl., 542.1 22.0 5".1
W 10,6 269.' 10.6 269.'
H '2, , 116.2 '2. I "6,2
.-ox 63,51(1
SHIP Wi. %SL" 56,7Kg 160LIS
Canst. Reagent Check Valves Cap&
Ref. Head Diaphragm Guide
Ball Seat Gasket
PVC PVC TFE Faced ALA PVC VTN PVC
PVDF PVDF TFE Faced ALA PVDF VTN PVDF
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A Unit of IDEX Corporation
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Engineered Pump Operations
2883 Brighton-Henrietta Town Line Road
Rochester, New York 14623 USA
Telephone: 585-292-8000
Fax: 585-424-5619
http://www.pulsa.com - Email;pulsa@idexcorp.com
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HYP- TS 09/03
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_ _ _ _____- 1520 NEMA 4X WASHDOWN PUMPS I
I
The hot new process technology
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The hot new technology ...
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Physically rugged
and chemically
resistant, 520 series
industrial pumps are NEMA
4X Washdown. They are the
ideal choice for chemical metering in
harsh, humid and corrosive
environments.
Wt:t'tSCTf1v-Mt:trlaw frrtdel ...
With 60% fewer roller passes than our competitors,
our pumps deliver 2'12 times the tube life.
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Why peristaltics?
Compared with other positive displacement pumps, peristaltic pumps
win on every count. They handle difficult fluids and suspended solids
with ease, and provide precision dosing and metering, without vapor
locking or crystallization problems. Cleaning and maintenance are quick
and easy. They self-prime, can run dry and have no valves or seals to
leak, corrode or clog, and the process fluid is totally contained within the
tube. That's why Watson-Marlow Bredel pumps outperform piston,
progressive cavity, lobe, gear and diaphragm pumps.
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. Pump and tubing last longer
. Less downtime, fewer failures, "one-minute" maintenance
. Hit a problem, next-day replacement keeps your production rolling
. Industry-leading warranty
So the best pump really does cost less.
Call us for the proof.
It all adds up to - V fit lue ffJr [ufe
Accurate metering of sodium hypochlorite, ferric
chloride, polymers and other chemicals is vital for water
and wastewater treatment. Watson-Marlow Bredel
pumps avoid salt settlement, vapor locking, abrasive
wear and clogging.
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Feature
Manual control
Speed adjustment; run and stop; forward/reverse;
"max" key for rapid priming and purging. Keypad
lock prevents tampering and accidental change
Auto-restart for mains failure recovery
Remote auto control
Digitally controlled with contact closure, 5V TTL
or 24V industrial standard logic inputs for: run/stop,
direction, auto/manual toggle, liquid detection and
MemoDose trigger
Analog control
Software calibrated remote speed control (4-20mA)
Second analog or keypad speed scaling
Pump status outputs
0-10V or Q-1258Hz analog pump speed feedback,
four digital 5V TTL or 24V industrial logic pump
status outputs
4-20mA pump speed feedback
MemoDose
Accurate, easy, single-shot dosing
Calibration
Simple calibration to display the f10wrate
as well as the rotation speed
Password protection
Guard against any setup changes
. . .
for every process
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RS485 network control
Full industrial standard connectivity for process
control through PC, PLC or other plant controller
Comprehensive calibratiol1
For precise metering and dispensing choice
The options
52OSN1R2: Just plug in and switch on:
low cost of ownership, with manual
control, simple, accurate dosing anti
calibration.
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520UN/R2: Keypad or remote control:
the process workhorse with status
outpu1s, configurable in software, and
password protection,
520DuNlR2: Full industrial connectivity:
the ultimate process pump. with RS485
and speed scaling and comprehensive
calibration.
r- United States of America France Malaysia The information contained in this document is believed '"
l Telephone 800 282 8823 Telephone +33 (0) 2 37 38 92 03 Telephone +60 (3) 5635 3323 to be correct, but Watson-Marlow Bredel accepts no "
Fax: 9786580041 Fax: +33 (0) 2 37 38 92 04 Fax: +60 (3) 5635 7717 liabi~ty fOf any errors it contains, and reserves the right "
"
Email support@wmbpumps.com Email info@watson-marlow.fr Email safes@my.SpiraxSarco.com to atter specifications without notice. "
www.watson-marlow.com www.watson-mar/ow.fr Netherlands '"
Gennany Telephone +31 (0) 104621688 Watson-Marlow, Pumpsil, LaserTraceabi/ity. Bioprene '"
[ Brazil Telephone +49 (0) 2183 42040 Fax: +31 (0) 10 462 3486 and Ma1prene are registered trademSlks of Watson- ~
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Telephone +55 11 46160404 Fax: +49 (0) 2183 82592 Email info@Watson-mar/ow.nf Marlow Limited lD
Fax: +55 11 4616 0403 Emaif info@Walson-marlow.de South Africa :r:
Emaif inf04brazil@Watson-marfow.com ~.watson-marlow.de Telephone +27 11 794 1921 STA-PURE and CHEM-SURE are trademarks of WL
www.watson-marlow.com.br Fax: +27 1 t 794 1250 Gore & Associates inc. F1uore1 is a tractemarf< 01 3M.
Italy
[ Belgium Telephone +39 030 6871184 Email info@wmbpumps.co.za
Telephone +32 9 225 94 57 Fax: +39 030 6871352 Sweden I~'IJ. ,....--r.J 1"
Fax: +32 9 233 06 49 Emaif info@Watson-marfow.i1 Telephone +46 8 556 556 00
Emaif info@Watson-marlow.be www.watson.mar/ow.it Fax: +46 8 556 556 19 ~PUfVlPS
China Korea Emaif info@Watson-marfow.se
www.watson-marlow.se
l Telephone +86 21 6485 4898 Telephone +82 (0) 2 525 5755 United Kingdom
Fax: +86 21 6485 4899 Fax: +82 (0) 2 525 5764
Email info@Watson-mar/ow.cn Email supporl4k@Watson-marlow.co.uk Telephone +44 (0) 1326 370370
www.watson-marfow.com.cn www.watson.mar/ow.co.kr Fax: +44 (0) 1326 376009 www.watson-marlow.com
EmaiI suppxt@{vatson-martow.co.uk
www.watson-martow.co.uk Members of the Spirax-Sarco Engineering Group
Pump Specification Power Supply
520SNlR 220 rpm NEMA 4X 1.6mm wt tube 115/230V 1 ph 50160 Hz ETL
52OSNlR2 220 rpm NEMA 4X 2.4mm wt tube 115/230V 1 ph 50/60 Hz ETL
520UNIR 220 rpm NEMA4X 1.6mm wt tube 115/230V 1 ph 50160 Hz ETL .
520UN1R2 220 rpm NEMA 4X 2.4mm wt tube 115/230V 1 ph 50160 Hz ETL
520USIR 220rpm ~, NEMA 4X l,6mm wt tube .115/22fN,. lph 50/60 Hz ETL
520USIR2 220rpm NEMA 4X 2.4mm wt tube 115/230V 1 ph 50/60 Hz ETL
520DuNIR 220 rpm., -. NEMA 4X 1.6mm wt tube 115/230V lph 50160 Hz Ell
520DuN1R2 220 rpm NEMA 4X 2.4mm wt tube 115/230V 1 ph 50/60 Hz ETL
520DuSIR 220 rpm SCADA NEMA 4X 1.6mm WI tube 115123OV" 1 ph 50160 Hz Ell
520DuSlR2 220 rpm SCADA NEMA 4X 2.4mm wt tube 115/230V 1 ph 50160 Hz ElL
Drive only Specification Power Supply
520SN Drive 220 rpm NEMA 4X 1151230V lph 50160 Hz ETL
520UN Drive 220 rpm NEMA4X 1151230V 1 ph 50/60 Hz ETL
520US Drive 220 rpm ~SCADA NEMA 4X 1151230V ~1 ph 50/60 Hz ElL
520DuN Drive 220 rpm NEMA4X 115/230V 1 ph 50160 Hz ETL
'520DuS Drive 220 rpm SCADA NEMA 4X 1151230V 1 ph 50160 Hz ETL
Specification
Low pulse twin channel pumphead
Low pulse twin channei extension pumphead
Low putse twin channel pumphead lOf STA-PURE tubing
Three roller pumphead with adapter plate lor 500 selies
cased drives, for 1.6mm wall thickness tubin9
Three roIIeI' pumphead wnh adapter plate for 500 series
cased drives. lor 2.4mm wall thickness tubing..
Four roller pumphead with adapter plate lor 500 series
cased drives. for 1.6mm wall thickness tubing
Four roller pumphead with adapter plate lor 500 series "
caSed drives, lor 2:4mmwaD thickness tubiilg
Three roller exlension pumphead for 1.6mm wall thickness tubing
Four roIter extension pumphead lor 1.6mm wall thickness tubing
Three roller extension pumphead for 2.4mm wall thickness tubing
- Four roI1er e,xtension pumphead fOf 2.4mm wall thickness tubing
Pumphead options
505L'
505LX
505LG
313D/A
2.4mm wall thickness tubing for 520R2
Tube' Tube bore Bioprene Marprene
105 0.5mm 1150' , .
108 O.8mm 1132'
119 1.6mm 1/16' 903,0016.024 902.oo16.024~;
120 3.2mm 1/8' 903.0032.024 902.0032.024
15 4.6mm" 3116' 903.0048.024' c902.0048.024
24 6.4mm 1/4" 903.0064.024 902.0064.024
-.121 8.Omm 5116' 903.0080.024 902.0080.024'~
122 9.8mm 3/8" 903.0096.024 902.0096.024
1.6mm wall thickness tubing for 520R
Tuber Tube bore Bioprene Marprene
O.5mm 1150'
O.8mm 1132"
1.6mm 1116'
3.2mm 118"
4.8rnm 3116''''
6.4mm 114'
18 8.Omm 5116'
Tube# Tube bore
. 112' O.5mm '1/50"
13 0.8mm 1132'
14 1.8mm 1/16'
16 3.2mm 1/8"
.' 25 4.8rnm 3116"
17 6.4mm 1/4'
18 8.Omm 5116'
903.0005.Q16
903.0008.016
903.0016.016
903.0032.016
903.0048.016
903.0064.016
903.0080.Q16
Neopt'llne
'902.0005.016
902.0008.016
902.0016.016
902.0032.016
902.0048.016
902.0064.016
902.0080.016
PVC
Pumpsil.
'i913.A005.024
913.AOO8.024
913A016.024
913.A032.024
913.A048.024
913.A064.024
"913AOSO.024
913.A096.024
PumpsU'
913.A005.016
913.A008.016
913.A016.016
913.A032.016
913.A048.016
913.A064.016
913.A080.016
Fluorel
Sta-Pure
Product number
050.713N.l0A
050.713N.2LA
OSO.714N.l0A
050.714N.2LA
OSO,714S,10A
OSO.714S.2LA
OSO.715N.l0A
050.715N.2LA
OSO.715S.1OA
050.715S.2LA
Product number
,.,056.713N.ooA
056.714N.ooA
056.714S.00A
056.715N.ooA
056,715S.ooA
Product number
053.4001.000
053.4011.000
053.4010.00G
033.3401.000
...~ 033.3501.000
033.4401.000
033.4501.000
033.3431.000
: "033.4431.000,
033.3531.000
033.4531.000 ~.
"960.0016.024 .. 965.0016.024"
960.0032.024 965.0032.024
960.0048.024:,>;),,965.0048.024
960.0064.024 965.0064.024
960.0080_024 ' 965.0080.024
960.0096.024 965.0096.024
Sta-Pure
,p
960.0016.0.16
960.0032.016
960.0048.016
960.0064.016
960.oo60.Q16
Chem-Sure
t~
965.0016.016
965.0032.016
.<1 965.0048.016
965.0064.016
965.0080.016
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520 performance
4000~ - - --
rTypic; flOw rete:
3500 Flow rate varies with tube
material. discharge
3000 I~ pressure, suction
2500 '! and viscosity
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2000 3
1500 lr
1000 l~
500 ~~
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