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| Tube Settler Systems for Clarification | |||||||||||||||||||||||||||||||||||||
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Tube settlers and parallel plates increase the settling capacity of circular clarifiers and/or rectangular sedimentation basins by reducing the vertical distance a floc particle must settle before agglomerating to form larger particles. |
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Tube settlers capture the settleable fine floc that escapes the clarification zone beneath the tube settlers and allows the larger floc to travel to the tank bottom in a more settleable form. The tube settler’s channel collects solids into a compact mass which promotes the solids to slide down the tube channel. |
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| Why Tube Settlers? | |||||||||||||||||||||||||||||||||||||
Made of lightweight PVC, tube settlers can be easily supported with minimal structures that often incorporate the effluent trough supports. They are available in a variety of module sizes and tube lengths to fit any tank geometry, with custom design and engineering offered by the manufacturer. |
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| Advantages of Tube Settlers | |||||||||||||||||||||||||||||||||||||
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The advantages of tube settlers can be applied to new or existing clarifiers/basins of any size: • Clarifiers/basins equipped with tube settlers can operate at 2 to 4 times the normal rate of clarifiers/basins without tube settlers. • It is possible to cut coagulant dosage by up to half while maintaining a lower influent turbidity to the treatment plant filters. • Less filter backwashing equates to significant operating cost savings for both water and electricity. • New installations using tube settlers can be designed smaller because of increased flow capability. • Flow of existing water treatment plants can be increased through the addition of tube settlers. • Tube settlers increase allowable flow capacity by expanding settling capacity and increasing the solids removal rate in settling tanks. |
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Excerpted from Innovative Plant Operations Yield Bonuses, Opflow, Vol. 6 No. 10 (Oct. 1980) |
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| System Design Criteria | |||||||||||||||||||||||||||||||||||||
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According to Tubular Settlers-A Technical Review, from the Journal AWWA, 331:335 (June 1978), written by Mr. Roderick M. Willis, there are three basic requirements essential for successful performance of tube settlers. 1. There must be laminar (or viscous) flow conditions within the tubes at the maximum flow rate required. Laminar flow is essential so that each slowly-settling floc particle within a tube maintains a steady descent to the collecting surface of the tube and is not intermittently swept upward by turbulent currents within the tube. 2. The residence time within each tube must be ample so that a floc particle entering at the extreme upper edge of the tube will have sufficient time to settle to the collecting surface a vertical distance below. (Once the particle reaches the collecting surface, the coalescing tendency between particles creates a steady sludge formation). 3. The velocity of flow through the tubes must not exceed a critical maximum that would cause the settled sludge to lose stability and be swept out of the tube in the direction of normal flow. As a corollary, the volume of the tube must be ample to allow either accumulation or a continual discharge backward of all sludge, without critically changing the normal flow rate through the tube |
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Size, Shape, and Configuration When selecting a tube settler, careful consideration should also be given to the vertical height of the modules. There are several different size tube settlers, each having a specific application rate. (See Design Application Rate chart) Tube settlers with a vertical height of 24” (610mm) and a tube length of 28” (711mm) are the most commonly used size. 3’ (914mm) and 4’ (1220mm) tube heights, because of longer residence time, are advantageous in many applications as well, such as high flow/high turbidity applications and where existing basins need improved settling capabilities to increase the plants total capacity.
Also, the tube module design should incorporate features that would prevent gaps along the installed modules. These gaps allow short-circuiting of unclarified water to pass around the tube settlers. A module design which allows nesting with adjacent modules is ideal because it maximizes available area and increases the total module strength. |
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Tube Settlers vs. Plate Settlers |
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Material of Construction
Any material used for either water or wastewater should include an ultraviolet radiation inhibitor. Some tube settler modules are constructed of ABS, which is a highly flammable material. A spark from welding, drilling, or a cigarette, etc. could ignite the ABS tube settlers, causing injury to personnel and damage to the tube settlers and surrounding structures. PVC modules (unlike ABS and other materials) have a specific gravity considerably greater than water and will not float. ABS modules have a specific gravity only slightly higher than water and require a tie-down system. This results in greater costs for material and installation. A tube settler module constructed of PVC will not require any hold-down system or clips. The mechanical properties of PVC exceed those of ABS, resulting in a more structurally sound installation. The most important mechanical property of PVC, flexural modulus, is 30% greater then that of ABS. PVC is denser, has greater tensile strength, higher impact strength, and is much less flammable then ABS. |
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| Tube Settler System Design | |||||||||||||||||||||||||||||||||||||
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Tube Settler System design is based on these three criteria: • Flow -- gpm (m/hr) : Required hydraulic flow capacity through the basin • Area -- ft2 (m2) : Plan area of tank for tube settlers. • Design Application Rate: Flow/Area of 1.5 to 3.5 gpm/ft2 (3.66 to 8.56 m/hr) Tube settlers handle maximum application rates from 2.5 to 4.5 gpm/ft2 (6.11 to 11.00 m/hr). The recommended application rate for design purposes is 1.5 to 3.5 gpm/ft2 (3.66 to 8.56 m/hr). This design application rate should be verified in accordance with local design standards for allowable flows, application rates, etc. Consideration of the influent water chemistry, settleability, and basin hydraulics should also play a role in selecting the proper application rate. |
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* Brentwood Tube Settlers ** Tube length is based on an angle of 60° *** Some states are limited by the 10 States Standards application rate of 2.0 gpm/ft2 (4.89 m/hr) |
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| The top of the tube settler modules should be submerged approximately 18” (458mm) to 30” (762mm) below the water surface. To prevent high velocities and short circuiting of tubes, the velocities through the sedimentation basin should be verified. This can be calculated by dividing the flow through the tank (ft3/s) by the cross sectional area (height x width) perpendicular to flow under the tube settler area, where the height is the distance between the bottom of the tube settlers and the basin floor. | |||||||||||||||||||||||||||||||||||||
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| The velocities under the tube settler area generally should not be greater than 0.05 fps. To avoid problems with longitudinal velocity, either the tank width or height should be modified. If this is not feasible, consideration of decreasing the flow is an option. Note that this figure is a general guideline and, if the velocity is a concern, a more detailed hydraulic analysis should be performed. When designing the layout of tube settlers within a basin, care should be given to avoid installation near entrance areas where turbulence could impact the performance of the tubes. In a horizontal basin it is recommended that approximately one-third of the basin length should remain tube-free to act as a quiescent zone. Generally, this is easy to implement because the required area of tube settler coverage will occupy a smaller portion of the basin. | |||||||||||||||||||||||||||||||||||||
Support System Design The support system can be made of stainless steel, painted carbon steel, or aluminum. Supports for the modules must be located a minimum of 1’-0” (305mm) from the end of each module for modules less than 8’-0” (2439mm) in length and 1’-6” (458mm) for modules greater than 8’-0” (2439mm) in length. The support system must be designed with consideration of both live loads (human traffic) and dead loads (Dead loads include the weight of the PVC tube settlers, floc build-up, troughs, baffles, protective surface grating, etc.). The dry weight of PVC tube settlers is approximately 1.75 to 2.00 lbs/ft3. The support system should be designed in accordance with a maximum 8’-0” unsupported span of the tube settler. This design will support both dead and live loads with an adequate safety factor. Some manufacturers will design based on a 10’-0” (3048mm) unsupported span that limits operator access and can be potentially dangerous. In rectangular tanks, the supports should span the full width of the tank. If this is not possible, intermediate support columns may be used. However, the support system should not impact any sludge-collecting device operations or other basin operations. Often concrete center columns are available for use in attachment of the tube settler support system. |
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| Trough Design Troughs and weirs for the tube settler system must be designed to handle peak flows and meet local regulatory requirements. Generally, a flow of 20,000 gpd per linear foot of weir (10 States Standards) is sufficient. Material of construction for troughs and weirs is commonly UV-inhibited, NSF-certified fiberglass or stainless steel. The layout of the troughs should be equally-spaced so flow distribution is realized throughout the tube settler area. A general rule of thumb is that trough spacing should not be more than four times the tube submergence. |
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| Baffle Design Baffles located at the tube settler/quiescent zone interface are required to direct water through the tube settlers area. They should be constructed of UV-inhibited fiberglass, PVC, or stainless steel. The design of the baffle system should be integrated with the support system. |
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| Tube Settler Access During basin design, consideration should be given to operator access for cleaning and (for larger tanks) access to troughs/weirs, as required, within the tube settler area. Like any type of equipment, tube settlers will require periodic cleaning and maintenance. Basin walkway design or a protective covering above the tube settlers should be provided. A plastic or fiberglass grating is ideal because it not only allows access to the tubes, troughs, and weirs but also adds a protective layer to the tube settlers. Any type of grating must be designed to be structurally sufficient, does not hinder tube settler performance, and will not damage the tube settlers. |
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| Why Brentwood Tube Settlers? | |||||||||||||||||||||||||||||||||||||
Brentwood provides complete engineered systems, including tube settlers, supports, baffles, troughs & weirs, and protective surface grating. The advantages of a Brentwood installation are:
• Save money by purchasing an economical packaged system. • Exclusive products and features like AccuGrid Protective Surface Grating and integrated structural ribs provide unique benefits to the tube settler system. • Extensive engineering experience in both plastics design and water treatment technologies are utilized in every system design. |
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Project Customization Every tube settler system is different due to project requirements, tank configuration, etc. Please contact us to provide detailed budget pricing, schematic system layouts, and specifications for your particular system design. |
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| Project Pricing The following case studies are representative of Brentwood’s economic performance within the water industry. The figures shown, adjusted for inflation, are from actual projects. System budget prices will vary considerably based on structural requirements and the scope of the project. |
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*Does not include new inlet piping, flocculation chamber, troughs, weirs, outlet piping. Includes only site grading, excavation, concrete tank |
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Home | Applications |Products | Installations | Product Specifications | Process Design Requests | Installation Guidelines | Contact | Technical Papers Copyright © 2005 Brentwood Industries, Inc.
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