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, an inclined plate clarification
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:
B16.1 Cast Iron Pipe Flanges and Flanged Fittings, Class
25, 125, 250 and 800
American Society for Testing and Materials (ASTM) Publications:
A-36 Structural Steel
A-53 Pipe, Steel, Black and Hot Dipped, Zinc Coated, Welded
Seamless
A283 Low and Intermediate Steel Plate of Structural Quality
American Welding Society (AWS) Publications:
D1.1-84 Structural Welding Code, Steel
A5.1 Mild Steel Arc-Welding Electrodes
Standard Welding Terms and Definitions
Standard Welding Symbols
Steel Structures Painting Council (SSPC) Publication:
SSPC-SP-10 Near White Blast Cleaning
American Institute of Steel Construction (AISC) Steel Construction
Manual, 8th Edition
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 clarification
and accessory equipment including principle dimensions and
location of fittings. Data shall include weight and distribution
of weight with the unit empty and filled with water.
1.3.2.2 Test results, signed by the manufacturer, which
indicate the clarifier is capable of handling specified
effluent concentration, pH, fluid temperature and concentration
of suspended solids. Tests on this model shall have been
done within the last 3 years.
1.3.2.3 Provide calculations of clarifier loading rate
at the design flow rate.
1.3.3 Submit the following after fabrication:
1.3.3.1 Verification:
- Written verification on the fabricator’s letterhead
that surface preparation and coating application were
performed in accordance with the specification and coating
specification and system manufacturer’s printed
recommendations;
- That the unit was hydraulically leak tested for a period
of at least 4 hours before further surface preparation
and coating;
- That the surface preparation and coating process was
performed at a facility owned and operated by the manufacturer;
1.4 MANUFACTURER’S SERVICE REPRESENTATIVE’S
REPORT AND CERTIFICATE: Submit service representative’s
complete signed report of results of the inspection, operation,
adjustment, and tests. Report shall include detailed descriptions
of points inspected, tests and adjustments made, quantitative
results obtained if such are specified, and suggestions
for precautions to be taken to ensure proper maintenance.
Include the manufacturer’s certificate that equipment
conforms to specified requirements and is ready for permanent
operation and that nothing in installation will render manufacturer’s
warranty null and void.
1.5 DELIVERY, STORAGE, AND HANDLING MATERIALS:
1.5.1 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.
1.5.2 Handling: Handle inclined plate clarifier in such
a manner as to ensure delivery to final location in sound,
undamaged condition. Take special care not to damage interior
and exterior surfaces of the inclined plate clarifier. Make
satisfactory repairs to damaged material(s) at no cost.
Carry and do not drag materials. Handle inclined plate clarifier
according to manufacturers information.
1.6 QUALITY ASSURANCE:
1.6.1 Inspection: Examine each component of clarifier 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 clarifier
operation, shall constitute cause for rejection.
1.7 WELDER QUALIFICATIONS:
1.7.1 Welders shall be previously qualified by passing
the tests prescribed in the AWS Standard Qualification Procedure,
or by passing such other tests as the Engineer may accept.
1.7.2 Welders shall have been tested within the past twenty
four months and their qualifications shall be considered
as remaining in effect unless the welder is not engaged
in a given process of welding for a period exceeding six
months.
PART 2 - INCLINED PLATE CLARIFIER DESIGN CRITERIA
AND MANUFACTURING SPECIFICATIONS
2.1 INCLINED PLATE CLARIFIER - APPLICATIONS & PERFORMANCE
2.1.1 Applications: The inclined plate clarifier shall
be used to separate entrained suspended solids from a wastewater
stream having a flow rate of *
gallons per minute. Water entering the flash mix section
has previously been conditioned to destabilize micro colloidal
suspended solids. Two additional compartmental tanks with
mixers are provided to flash mix an activated polyelectrolyte
with the conditioned wastewater and then slowly flocculate
the suspended solids into easily settleable masses.
*COMPLETE BLANKS FROM ATTACHED CHART
The flocculated suspended solids precipitate from entrainment
as the hydraulic flows moves through the clarifier’s
inclined plates, collect and slide down the incline, falling
into the clarifier sludge hopper. The settled sludges collect
on the bottom of the sludge hopper, gravity concentrate
and are discharged on an as needed basis to a filter press
or sludge thickener via air diaphragm pumps. The clarified
water gravity flows from the top of the clarifier to a sand
filter or discharge.
2.1.2 Performance: The clarifier shall remove the at least
98% of the destabilized and conditioned micro colloidal
suspended solids from *
gallons per minute flow.
2.2 Inclined Plate Clarifier Manufacturing specification
2.2.1 The manufacturer of the inclined plate clarifier
and related components shall have been manufacturing clarifiers
of the following specified design for at least five years.
The clarifier and components shall be fabricated and assembled
at the steel fabrication facility owned and operated by
the manufacturer. Sandblasting and coating operations shall
also be performed at the manufacturers’ facility.
The manufacturer shall maintain a quality control staff
to perform quality assurance checks during fabrication and
assembly.
2.2.2 Inclined plates shall be set at a minimum of 60 degrees
above the horizontal plane.
2.2.3 The maximum flow rate through the inclined plate
clarifier shall not exceed 0.25 gallons per minute per square
foot of horizontal projected area. (Horizontal projected
area of an inclined plate set at 60° is 50% of the total
surface are).
2.2.4 Forced uniform flow throughout the inclined plate
section shall be created to assure that each plate received
an equal amount of flow and that the flow is distributed
over the entire effective width of each plate without short
circuiting by the incorporation of dual orifices located
at least 6" above and on both sides of the plate sections.
The orifices shall be in two rows located at 2" and
3" respectively below the top overflow weir. The orifice
shall be of a diameter that at maximum design capacity restricts
the flow rate to create a 2" pressure drop through
each orifice. Custom molded Viton or rubber grommets shall
be inserted in each hole. The manufacturer shall supply
data of a installation with at least five years operating
experience that demonstrates this method of flow equalization.
Center mounted effluent collection structures do not provide
uniform flow across the plate section and are not acceptable.
V-notch weirs do not provide uniform flow and thus are not
acceptable.
2.2.5 To ensure full utilization of all plate areas and
to prevent the shearing of floc particles, Velocities through
the unit shall be kept below 1 FPS. Flow velocity calculation
shall be submitted for feed ducts, feed bay and plate separators.
*COMPLETE BLANKS FROM ATTACHED CHART
2.2.6 The clarifier shall be provided with minimum 4 inch
freeboard at design flow rate.
2.2.7 The minimum plate spacing shall be 2 inches. Plates
shall be fabricated of fiber reinforced plastic. The plates
shall be supported by dividers constructed of stainless
steel, Teflon or molded plastic inserts and shall be individually
removable.
2.2.8 The settling plates shall have a length to width
ratio of *
to 1. The plates shall be a minimum of 0.09 inches thick
FRP. The plates shall have a resin rich surface to prevent
fiber show. The plates shall be produced by contact molding
or machine extrusion, "hand or spray lay-up fabrication"
will not be acceptable.
2.2.9 The plates shall be 24" wide supported on the
sides and center, such that unsupported distances shall
not exceed 12". Settling plates wider than 24"
shall be supported on 12" center or provide documentation
and test results that the plates will withstand a load of
100% filled with sludge, specific gravity 1.4 or above,
with all water drained from the clarifier, without plate
collapsing. Manufacturer shall provide a minimum of five
installation references with at least five years service
without failure.
2.2.10 Gasket materials utilized in the plate construction
shall be Viton or Teflon. All assembly clips shall be constructed
of Teflon.
2.2.11 Inlet and outlet shall be flanged connections drilled
to ANSI B16.1.
2.3 MANUFACTURING SPECIFICATIONS - INTEGRAL SLUDGE HOPPER
2.3.1 The inclined plate clarifier shall have an integral
sludge hopper located below the plate zone. The sludge compartment
shall be constructed as an inverted pyramid.
2.3.2 The sludge hopper shall have three (3) sludge samples
3/4" NPT nipples and a 20 inch manway.
2.3.3 The sludge hopper shall have a volume of at least
* gallons.
2.3.4 Two (2) zinc anodes mounted to 3/4" male pipe
plugs shall be mounted in the hopper for galvanic protection.
*COMPLETE BLANKS FROM ATTACHED CHART
2.4 Manufacturing Specifications - Flash Mix and Flocculate
Section
2.4.1 Rapid mix tank shall have a minimum detention time
of 30 seconds at design flow rate.
2.4.2 Rapid mixer to be a single speed (maximum output
speed 70 rpm) mixer comprised of vertical shafted mixer
with at least 75% length of the mix chamber height, gear
reducer and motor. The mixer shall have a rigidly mounted
bottom steady rest support. The gear motor shall provide
at least 300 inch pounds of torque and be driven by a 440V,
3 phase TEFC motor. All seals and bearings shall be above
the water surface.
2.4.3 Flocculating tank shall have a minimum detention
time of 2 minutes at design flow rate with a motorized vertical
shaft mixer, variable speed, that supplies low turbulent
motion to build the floc.
2.4.4 Flocculate mixer shall be a variable speed mixer
5 to 1 ratio with a maximum speed not to exceed 40 rpm’s
comprised of mixer paddles, variable gear reducer and TEFC
motor. The gear motor shall provide at least 300 inch pound
of torque at maximum speed and shall be driven by a 440V,
3 phase motor. The mixer shaft shall have a rigidly mounted
bottom steady rest support. All seals and bearings shall
be above the water surface.
2.4.5 Rapid mix tank and flocculating tank to have a minimum
4 inch freeboard at the design flow rate.
2.4.6 Rapid mix tank shall have a chemical injection pipe
connection for injection of polymer directly below flash
mixer.
2.4.7 The rapid mix and flocculate tank shall be equipped
with at least 3 integral anti-vortexing baffles.
2.5 MANUFACTURING SPECIFICATIONS - PLATFORM
2.5.1 A platform shall be included for the inspection of
the rapid mix, flocculating and clarifier compartment.
2.5.2 Access to the platform shall be provided by ladder.
A cage shall be included if the ladder exceeds 20 feet.
2.5.3 Platform floor grating shall be coated for corrosion
resistance.
2.5.4 The platform shall have a handrail to protect personnel.
The opening between the rails shall be in compliance with
OSHA and UBC standards and shall not exceed 12 inches.
2.6 STRUCTURAL:
2.6.1 All structural and tank steel stresses shall be within
the allowable limits shown in the Steel Construction Manual
of the American Institute of Steel Construction, Eighth
Edition.
2.6.2 The unit to be structurally designed for installation
in Seismic Zone *
in accordance with 1985 Uniform Building Code.
2.6.3 Clarifier shall be fabricated from ASTM A-36 steel.
2.6.4 All exterior welds shall be continuous seal weld
or the weld must be caulked before surface coating.
2.7 ELECTRICAL:
2.7.1 Rapid mixer, flocculate drive and sludge drive unit
shall have 440V, 60 Hz, 3 phase TEFC or TENV motors, maximum
1 HP.
2.7.2 The drives shall be remotely started and stopped.
2.8 TESTING:
2.8.1 All seal welds shall be visually checked for continuity,
pinholes, and voids.
2.8.2 The entire unit shall be shop-hydrostatically tested.
Documentation of hydrostatic test shall be provided.
2.9 SURFACE PREPARATION AND COATING
2.9.1 Surface Preparation: The steel surfaces must be dry
and clean in accordance with the following requirements.
Remove all grease, oils and contaminants as outlined in
SSPC SP1. Remove all weld splatter and grind burrs on cut
edges and rough welds smooth. Blast clean all surfaces after
fabrication in accordance with SSPC SP6 with profile depth
of 1.5-2.5 mils. Apply first primer before any rust bloom
forms.
2.9.2 Caulking: All exterior non-seal welding joints shall
be filled with rubber caulking before painting. Allow sufficient
time for the caulking to dry before applying the finish
coat.
*COMPLETE BLANKS FROM ATTACHED CHART
2.9.3 Exterior Surfaces:
Shop First Coat: Apply one coat average dry film thickness
of two mils minimum, of a high-build catalyzed epoxy. Apply
to all steel surfaces except the areas within 2 inches adjacent
to field welds and surfaces specified to be hot-dip galvanized.
The paint shall be Hempel 4563U.
Shop Finish Coat: Apply one coat average dry film thickness
of 1.0 mils minimum, of a polyurethane paint. Recoat at
time interval recommended by the manufacturer, the final
coat shall be Hempel 5595U.
Third Coat: Field touch-up of damaged and unpainted areas
shall be the same as specified first and second coats at
the same film thickness.
The total dry film thickness shall be an average of 4 mils.
2.9.4 Interior Surfaces:
Shop First Coat: Apply one coat average, dry film thickness
of four mils, of an immersion grade high-build catalyzed
epoxy. Apply to all steel surfaces except the areas within
2 inches adjacent to field welds and surfaces specified
to be hot-dip galvanized. The paint shall be Hempel 15409.
Shop Finish Coat: Apply one coat average, dry film thickness
of 4 mils, of an immersion grade high-build catalyzed epoxy.
Recoat at time interval recommended by the manufacturer,
the final coat shall be Hempel 15409.
Third Coat: Field touch-up of damaged and unpainted areas
shall be the same as specified first and second coats at
the same film thickness. (Liquid Contact).
The dry film thickness shall be an average of 6 mils.
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 sludge thickener tank in such a manner
as to ensure delivery to final location in sound, undamaged
condition. Take special care not to damage interior and
exterior surfaces of sludge thickener tank and associated
supports and pipe coatings or linings. Make satisfactory
repairs to damaged material(s) at no cost. Carry and do
not drag materials. Handle sludge thickener tank according
to manufacturers information.
PART 4 - EXECUTION
4.1 Installation: Inclined plate clarifier tanks 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 inclined plate
clarifier fully operational. Do not weld tank surfaces,
interior or exterior, it will permanently damage the interior
lining. If welding has inadvertently occurred, the interior
surface affected shall be abrasively ground to white metal
and two coats of Hempel 15409 applied, with air dry between
coatings.
4.2 Field Inspection Services: Examine each component of
inclined plate clarifier 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 inclined plate clarifier
operation, shall constitute cause for rejection.
4.3 Start-Up Testing: Manufacturer’s field representative
shall inspect and test unit and certify that the installation
has been performed in accordance with manufacturer’s
recommendations and that the system is ready for operation
by others. Inspection shall consider, but not be limited
to, the following:
- Soundness (without cracked or otherwise damaged parts).
- Completeness in all details, as specified.
- Correctness of settling alignment, set points and relative
arrangement of each component.
- Confirm that the unit is level within ¼"
side to side and end to end.
- Inspect unit for leakage and that all mixers are operating
as specified.
- Inspect coating integrity to insure installation contractor
has applied touch-up paint to all scratches, blemishes
and/or coating discontinuity that occurred during shipping
and installation.
PART 5 - SUGGESTED MANUFACTURER:
The inclined plate clarifier shall be model number # *
manufactured by:
Hoffland Environmental, Inc.
10391 Silver Springs Road
Conroe, Texas 77303
(936) 856-4515 phone / (936) 856-4589 fax
e-mail: hoffland@flex.net
*Model Number *
*Check following page for alternates.
*COMPLETE BLANKS FROM ATTACHED CHART
HOFFLAND ENVIRONMENTAL, INC.
CONE BOTTOM SLUDGE HOPPER
MODEL NUMBER |
SECTION VARIABLE |
2.1.1/2.1.2 |
2.2.8 |
2.3.3 |
2.3.4 |
2.6.2 |
|
25
35
60
75
55
75
125
150
250
110
150
250
300
500
750
1100
|
1 to 1
1 to 1
1 to 1
1 to 1
2 to 1
2 to 1
2 to 1
2 to 1
2 to 1
5 to 1
5 to 1
5 to 1
5 to 1
5 to 1
5 to 1
5 to 1
|
190
450
700
1100
190
450
700
1100
2100
240
550
800
1300
2500
6000
8900
|
476
800
1500
476
800
1500
2300
476
1000
1800
3500
5000
9000 |
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