The invention relates to a dewatering device, and more particularly relates to a dewatering device and a tensioning apparatus for a belt conveyor which both may form part of a wastewater screening apparatus.
Wastewater screening apparatus are known which separate solid material from wastewater and also compact the solid material for disposal. Such apparatus may be used, for example, to remove solids from a flow of sewage so that the water from the sewage can proceed to further treatment prior to discharge or reuse. The separated solids may be disposed of in landfill.
An example of such a screening apparatus is described in U.S. Pat. No. 8,302,780. U.S. Pat. No. 8,302,780 describes a screening apparatus which uses a continuous filter belt to filter solid material from an aqueous mixture. The filtered solid material is removed from the filter belt and is passed to a dewatering device in the form of a screw press which mechanically extracts liquid from the solid material through compaction.
Although the above-referenced prior art screening apparatus is able to remove a significant amount of water from the solids, water still remains trapped therewithin. Accordingly, it is desirable to improve the dewatering process so as to produce solids with a lower water content.
Additionally, the installation and maintenance of the filter belt can be difficult and time-consuming. It is therefore also desirable to address this issue.
In accordance with an aspect there is provided a tensioning apparatus for a belt conveyor, the tensioning apparatus comprising:
The mounting bracket may be a pillow block bearing which is configured to rotatably support the roller.
The linear actuator may be a screw-driven actuator.
The linear actuator and/or linear guide may comprise a measurement scale for determining the position of the roller.
The linear guide may support the shaft of the roller in a cantilevered manner.
For a better understanding of the invention, and to show more clearly how it may be carried into effect, reference will now be made, by way of example, to the accompanying drawings, in which:
The presently described apparatus processes wastewater to extract most of the water content leaving a semi-dry organic cake which has value in post processes. The process receives the wastewater, referred to as “dirty water” and first filters it to remove most of the liquid content and then compresses the remaining cake to extract most of the remaining water. The filtration step uses a fine mesh continuous conveyor belt filter cloth to capture solids and then an auger drive to press most of the remaining water out of the cake. A wash spray is directed on the back of the filter which not only washes away debris that is attached on the outside of the filter cloth, but also clears debris normally clogged within pores of the filter cloth. In the auguring step, the cake and debris is compressed, which squeezes out the remaining dirty water and the wash water. A free water drain is located at one end of an auger channel while the cake/debris are compressed and moved by the auger screw within the auger channel in the opposite direction.
The debris captured by the filter cloth is driven downwardly into an open collection chamber which delivers the debris into the auger screw which conveys the debris to a compression chamber. Wash water that is not absorbed in the debris is free to flow above and around the auger's flights and by gravity flows toward and into the free water drain. The free water drain is located in an enclosed obstructed location so that only overflow liquid is able to freely flow into the drain. By allowing this drainage, a liquid level in the collection chamber is controlled and the dewatering drain located under the dewatering section is able to drain the remainder of water absorbed in the solid debris so that the solids debris that exits the device can meet a specified moisture content.
Plant 10 separates and dewaters wastewater 15A entering plant 10 at inlet 30. Wastewater 15A may have a total suspended solids (TSS) in the range of from about 100 to 2,000 mg/L. This wastewater 15A may be collected from a typical municipal sewage system which might have about 300 mg/L TSS. Trash, garbage and other materials usually found in wastewater drainage may be separated using a pre-filter. Downstream of pre-filter wastewater 15A enters plant 10 at inlet 30 where it encounters diverter panel 140 dropping onto catch shelf 150 whereupon it spills onto conveyor belt 80 as shown in
A cake 15C left behind on and in conveyor belt 80 comprises between 40-90% of the TSS of the wastewater 15A depending on the type and fineness of the filter material of which belt 80 is made. Conveyor belt 80 moves continuously as an inclined rotating linear conveyor. Both upper 82 and lower 84 portions of belt 80 may be planar and may move in parallel with each other in opposite directions and over spaced apart top roller 210 and bottom roller 205 (
As belt 80 moves over top roller 210 some portion of cake 15C may fall into cake collection basin 110 and therefore into auger screw 120 as best illustrated in
Cake 15C and wash water 15D are carried by auger screw 120 to the left in
Overflow drain 240, located at the right end of auger screw 120 in
With the water extraction step described above, cake 15C is converted to a semi-solid consistency which passes out of plant 10 though door 72 when pressure within the wire cage 200 is sufficient to push open door 260 against tension springs. The semi-solid cake 15C may have a water content of between only 50% and 60%.
The auger screw 120 is mechanically rotated within auger trough 122 by an electric auger drive motor 230, as shown in
As shown in
The take-up device 302 comprises a non-actuated linear guide 304 and a linear actuator 306.
The linear guide 304 comprises a rod 308 (1¼″ diameter solid stainless steel) and a bearing 310. The rod 308 is slidably supported by the bearing 310 such that it can move linearly relative to the bearing 310. The bearing 310 may comprise a pair of linear non-metallic bushings which are spaced from one another along the longitudinal axis of the guide 304 so as to provide the optimum stiffness and smoothness of motion. The rod 308 is provided with a mounting bracket 311 at its distal end for connecting the rod 308 to a shaft 312 of the roller 210. In this example, the mounting bracket 311 is a pillow block bearing which rotatably couples the rod 308 to the shaft 312, but in other arrangements the shaft 312 may not rotate such that the mounting bracket 311 can fixedly connect to the shaft 312.
The linear actuator 306 comprises a stationary part 314 (stator) and a moving part 316 (pusher). The stationary part 314 forms a body of the actuator 304 and is bolted onto the bearing 310 of the linear guide 304. The moving part 316 is a rod which is bolted at its distal end to a mounting plate 318. The mounting plate 318 connects to the mounting bracket 311 of the linear guide 304 via an arm 320. The moving part 316 is translatable relative to the stationary part 314 via suitable drive means. In the example shown, the linear actuator 306 is a screw-driven actuator which comprises a lead screw that translates the moving part 316 relative to the stationary part 314. The linear actuator 306 comprises an adjuster nut 322 which rotates the lead screw in order to move the moving part 316. The adjuster nut 322 provides a stationary point of actuation of the linear actuator 306 which allows repeated motion with a tool.
The linear guide 304 supports the weight of the roller 210 in a cantilevered manner. The linear guide 304 has sufficient rigidity that it is able to withstand the resulting forces and ensure the roller 210 moves along a linear path. The linear actuator 306 is arranged so that its longitudinal axis is parallel with the longitudinal axis of the linear guide 304. The linear actuator 306 is therefore able to drive the linear guide 304 so as to move the roller 210 between extended and retracted positions.
In the retracted position, the belt 80 is slack such that it can be easily fitted, serviced and removed. In the retracted position, the rod 308 fully penetrates the non-metallic linear bushings of the bearing 310 for 6⅝ inches. With the linear actuator 306 in the extended position, the belt 80 is properly tensioned for operation. A maximum tension of up to 3200 lbs. may be applied by the linear actuator 306 so as to preload the belt 80.
The linear actuator 306 is provided with an incremental measurement scale 324 which defines the position of the moving stationary part 316 relative to the stationary part 314. As described previously, the belt 80 is provided with two take-up devices, one on each side of the belt 80. The scale 324 on each side provides a visual indication of how far the take-up device has been extended or retracted. By matching each scale to the same value, the tracking of the belt 80 can be accurately and repeatably set with no external tooling. Tracking refers to how straight a belt travels over two rollers. If one piston is extended further than the other, the belt will want to travel towards the tighter piston. This can lead to potential failure and/or damage of the filtration belt assembly. This tensioning system provides a more accurate and repeatable method of applying equal force across the entire width of the belt 80. The individual take-up devices provide visually measureable positioning to easily adjust belt tracking within 1.5 mm (0.06″). These measurements can be documented and plotted over time, aiding in the prediction of service interval and/or life of the filtration belt assembly.
The bottom of the compression chamber 402 has a structural wedge wire screen 404, allowing the compressed water to filter through for discharge.
The auger screw 120 in the compression chamber 402 covers 80% of the wedge wire surface. In this example, the auger screw comprises a shaft 408 on which a helical blade 406 is formed. The blade 406 has a 9″ diameter (right hand) and a 9″ pitch over its length within the trough 122. Once inside the compression chamber 402, the helical blade 406 reduces to ¾ pitch so as to compress the solids. As shown in
The solids continue to be compressed as they transfer through the compression chamber 402 until they reach the mixing blades 410. The mixing blades rotate with the shaft 408, cutting through the concentrated dewatered solids mass.
The outlet 411 of the compression chamber 402 comprises a discharge cone 412. In the example shown, the discharge cone 412 has a 60° solid angle surface. The discharge cone 412 is translatable relative to the compression chamber 402 to provide an outlet out of the compression chamber 402 (of up to 8″ in area), but is biased towards the compression chamber 402 (i.e. towards a closed position) by two spring-biased compression pistons 414 that provide balanced force and precise motion.
The mixing blades 410 break up the solids mass as it begins to be forced out of the discharge cone 412. Breaking up the solids mass provides two benefits. The solid mass is separated, freeing any trapped water inside the solid mass and maintaining equal distribution of the solids around the discharge cone 412. Maintaining the equal distribution of solids around the discharge cone is critical in having uniform compression in the compression chamber 402. The solids are forced against the surface of the discharge cone 412, discharging the solids 360° around the cone. The cone force can be adjusted to provide a linear force from 0 lbs. to 67.2 lbs., giving up to 1.11 psi.
Although the tensioning apparatus has been described with reference to a wastewater screening apparatus, it will be appreciated that it may be applied to any belt conveyor.
Filing Document | Filing Date | Country | Kind |
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PCT/GB2016/053920 | 12/12/2016 | WO | 00 |
Number | Date | Country | |
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62265855 | Dec 2015 | US |