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PART 1 - GENERAL
1.1 Scope: The work covered in this section includes furnishing
all labor, material, equipment and incidents to install complete and
ready for operation, a polymer feed system device as shown on drawings
and as specified herein.
1.2 APPLICABLE PUBLICATIONS: The publications listed below form a
part of this specification to the extent referenced. The publications
are referred to in the text by the basic designation only.
American National Standards Institute (ANSI) Publication:
Pipe Flanges and Flanged Fittings, Class 25, 125, 250 and 800
American Society for Testing and Materials (ASTM) Publications:
ASTM D 1785 Polyvinyl Chloride (PVC) Plastic Pipe, Schedules 40, 80, and 120
A-240 304L Stainless Steel Plate A-249 Stainless Tubing A-276 304L Stainless Rounds, Squares, Flats 1.3 SUBMITTALS:
1.3.1 Contracting officer will review and approve all submittals.
1.3.2. Submit the following before fabrication
1.3.2.1 Shop Drawings: Shop drawings for polymer feed system and
accessory equipment including principle dimensions and location of
fittings.
1.3.2.2 Calculations to prove that the mixing turbulence is at least G=10,000 sec-1 as well as calculations to prove that the aging chamber is non-turbulent and not mechanically agitated.
1.3.2.3 Calculations to prove the mechanical mixing section does
not exceed 30 seconds plug flow at a flow rate of 1.5 gallons per
minute.
1.3.2.4 Calculations to prove that the non-turbulent aging chamber
has a plug flow retention time of 10 minutes at a flow rate of 1.5
gallons per minute.
1.3.2.5 Design details proving the diluted polymer is not
subjected to mechanical agitation after leaving the initial high
turbulent mixing section.
1.4 DELIVERY, STORAGE, AND HANDLING MATERIALS:
1.4.1 Delivery and Storage: Inspect materials delivered to site
for damage; unload and store with minimum handling. Store materials on
site in enclosures or under protective coverings. Protect materials not
suitable for outdoor storage to prevent damage during periods of
inclement weather, including subfreezing temperatures, precipitation,
and high winds. Store materials susceptible to deterioration by direct
sunlight under cover and avoid damage due to high temperatures. Do not
store materials on ground. Store and protect materials according to
manufacturer recommendations.
1.4.2 Handling: Handle polymer feed system in such a manner as to
ensure delivery to final location in sound, undamaged condition. Take
special care not to damage surfaces of the polymer feed system. Make
satisfactory repairs to damaged material(s) at no cost. Carry and do
not drag materials. Handle polymer feed system according to
manufacturers information.
1.5 QUALITY ASSURANCE:
1.5.1 Inspection: Examine each component of polymer feed system
for compliance with requirements specified. Redesign or modification of
equipment to comply with specified requirements, or necessary redesign
or modification following failure to meet specified requirements, shall
receive particular attention for adequacy and suitability. This element
of inspection shall encompass visual examinations and dimensional
measurements. Noncompliance with specified requirements, or presence of
one or more defects preventing or lessening maximum efficiency of
polymer feed system operation, shall constitute cause for rejection.
PART 2 - POLYMER FEED SYSTEM DESIGN CRITERIA AND MANUFACTURING SPECIFICATIONS
2.1 POLYMER FEED SYSTEM - APPLICATIONS & PERFORMANCE
2.1.1 Applications: The automated polymer dilution/feed system
shall consist of an integrated equipment package capable of
automatically metering, diluting, aging, activating, and pumping liquid
polymer and water. After leaving the initial mixing chamber, the
polymer solution shall pass through a non turbulent aging chamber.
After initial dilution, the dispersed polymer in water shall not be
subjected to shear.
2.1.2 Performance: The system shall have the capability of
handling emulsion and solution polyelectrolytes. The system shall be
designed to mix a 20 - 50 percent concentrated liquid polymer solution
with viscosities up to 60,000 CPS with water, automatically produce a
diluted and aged polymer solution and to convey the aged polymer
solution to the application point. The system shall be an integrated
package, prepiped, and prewired. The configuration shall provide for a
complete integral polymer feed system, mixing and aging the polymer,
and occupying the smallest possible space. The feed system input range
shall be up to A* USGPH dilution water and up to
B* USGPH polymer.
2.2 POLYMER FEED SYSTEM - Manufacturing specification
2.2.1 Mixing Requirements: Mixing energy shall be provided by a
motor driven stainless steel multi-bladed impeller. Mixing chamber
impeller shall be powered by a heavy duty direct drive 1725 rpm motor
of at least 3/4 HP with manually resettable thermal overload
protection; belt drives and static mixers shall not be acceptable.
Impeller shall rotate on a stainless steel shaft supported by stainless
steel bearings and seals. Mixing chamber shall be transparent acrylic
and shall be capable of 100 psig working pressure.
To prevent vortexing and induce uniform back mixing throughout,
the mixing chamber shall contain at least four (4) stainless steel
baffles rigidly mounted near the mixing chamber’s internal wall.
The polymer mixing/dilution chamber shall provide high speed high
turbulent mixing conditions for a short period to rapidly disperse the
polymer, then to prohibit the destruction of the fragile long chained
freshly activated polymer, the polymer solution shall not be subjected
to mechanical agitation in the aging chamber.
Per the Camp-Steen equation, the mixing chamber will have a minimum turbulence of G=10,000 sec-1.
The retention time in the mixing chamber shall not exceed 30 seconds at a flow rate of 1.5 gallons per minute.
Polymer mixing system shall be specifically designed to invert,
disperse, age, and activate solution, emulsion and dispersion polymers
with viscosities from 200 - 60,000 CPS.
2.2.2 Aging Chamber: A non-turbulent aging chamber shall form the
base of the polymer mixing device with the high turbulent mixing
chamber integrally attached to the top of the aging chamber. The aging
chamber shall not be subjected to any mechanical agitation and shall be
of non-metallic construction. The aging chamber shall have PVC internal
baffles to prohibit channeling or short circuit flows.
The aging chamber shall provide a retention time of at least 10 minutes at a flow rate of 1.5 gallons per minute.
2.2.3 Water Flow: The system shall have a switch to shut power off
to the unit in case of low water pressure, an electrically operated
solenoid valve for on/off control of dilution water supply, and a
rotameter type indicator equipped with an integral rate adjusting
valve. The flow indicator shall have a valve stop and guided float.
Water flow rate shall be adjustable to A* USGPH. Water supply input shall be
C* " FNPT and stock solution outlet fitting shall be
D* " FNPT. Polymer feed system shall be capable of operating with a water supply pressure of 30 PSIG.
2.2.4 Controls and Metering Pump: Components shall include but not
be limited to: solenoid valve and rotameter with rate valve on water;
water pressure regulator, and metering pump.
Metering pump shall have a variable stroke rate and stroke length. Output volume shall be adjustable while pump is in operation.
Metering pump shall be of the electronic solenoid operated type.
Pump shall be positive displacement with no mechanical linkage. Power
supply will be 115 volt, 60 Hz.
OPTIONAL 2.2.5 (Slave Pump) Metering Pump 4-20 mA Controllable:
Metering pump shall be upgraded to a model that is controllable by
means of either a 4 - 20 mA signal or manual control to automatically
proportion the polymer.
OPTIONAL 2.2.6 (Smart Pump) Low Flow Shutoff Switch: A low flow
shutoff switch is available as a replacement to the standard low
pressure shutoff switch. This option would be useful should the
solution flow exiting the polymer system be blocked (by a valve down
stream being in the wrong position).
OPTIONAL 2.2.7 Calibration Tube Assembly: The calibration tube
assembly is an 8 oz. tube mounted to the side of the aging chamber that
tees into the polymer line leading to the metering pump. The standpipe
shall allow convenient observation of maximum speed settings. The tube
is used to isolate a precise amount of polymer (8 oz.), allowing for
observation of seconds elapsed during use of the precise amount. With
this information, the operator can calculate gph of polymer use and,
with knowledge of the wastewater stream flow, can also calculate dosage
in ppm.
2.3 CONTROL PANEL
2.3.1 Central Controls: The central controls shall be housed in a
NEMA 4 enclosure. Controls requiring operator adjustment shall be
surface mounted. Control panel shall be mounted on the polymer mixing
and aging unit.
2.4 TESTING
2.4.1 The entire unit shall be shop hydrostatically tested. Documentation of hydrostatic test shall be provided.
PART 3 - DELIVERY, STORAGE AND HANDLING MATERIALS
3.1 Delivery and Storage: Inspect materials delivered to site for
damage; unload and store with minimum handling. Store materials on-site
in enclosures or under protective coverings. Protect materials not
suitable for outdoor storage to prevent damage during periods of
inclement weather, including subfreezing temperatures, precipitation
and high winds. Store material susceptible to deterioration by direct
sunlight under cover and avoid damage due to high temperatures. Do not
store materials directly on ground. If special precautions are
required, prominently and legibly stencil instruction for such
precautions on outside of equipment or its crating. Store and protect
materials according to manufacturers recommendations.
3.2 Handling: Handle polymer feed system in such a manner as to
ensure delivery to final location in sound, undamaged condition. Take
special care not to damage surfaces of polymer feed system. Make
satisfactory repairs to damaged material(s) at no cost. Carry and do
not drag materials. Handle polymer feed system according to
manufacturers information.
PART 4 - EXECUTION
4.1 Installation: Polymer feed system to be installed as indicated
and as recommended by the manufacturer. Equipment delivered to the site
in advance of installation to be stored per the manufacturer’s
requirements. Make all connections as required to make polymer feed
system fully operational.
PART 5 - SUGGESTED MANUFACTURER:
The polymer feed system shall be model number #
* manufactured by:
Hoffland Environmental, Inc.
10391 Silver Springs Road Conroe, Texas 77303-1602 (936) 856-4515 phone / (936) 856-4589 fax
e-mail: [email protected] *Model Number
*
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