The present invention relates to a technique for filtering wastewater in which solid components are mixed.
A filtering apparatus is an important tool in making effective use of water resources. This is because wastewater can be converted to purified water by a filtering apparatus. An essential component of a filtering apparatus is an element for removing impurities that include solid matter from wastewater. The amount of solid matter that accumulates in the element is proportional to the time elapsed in filtering. Flow resistance increases when the amount of sediment increases, and the amount of water that can be treated is reduced. In order to restore the amount of water that can be treated, the element must be replaced with a new element or the element must be regenerated.
Considering the effective use of earth resources, regeneration is more preferable to replacing elements. A technique for regenerating elements is described in, e.g., Japanese Patent Application Laid-Open Publication No. 2001-108790 (JP 2001-108790 A). The filtering and regenerating technique described in JP 2001-108790 A is described with reference to
Solid matter in the wastewater flows (arrow B) from an outer surface 101 of an element 100 toward an inner surface 102 when the wastewater flows in the manner indicated by arrow A parallel to the element 100, which is composed of a ceramic filter, as shown in
Water pressure P1 is applied from the inner surface of 102 toward the outer surface 101 when a fixed amount of wastewater is treated, as shown in
Next, the water pressure P2 is rapidly reduced. At this point, the solid matter 103 that is deposited on the outer surface 101 is removed by the effect of the water pressure P1, as described in
Regeneration is smoothly carried out because sludge is soft when the solid matter 103 is principally composed of sludge.
However, in the case that sand and fine metals are mixed in large quantities in the solid matter 103, a substance is formed in which the sand or the like in the sludge is embedded as an aggregate and becomes hard overall, and the removal of the solid matter 103 becomes difficult. The difficulty particularly increases when the thickness of the sediments increases. The regeneration described above is not suitable for wastewater that contains large amounts of sand and the like.
In view of the above, there is a need for a filtration technology that is advantageous for treating wastewater containing large amounts of sand and the like.
In the discussion below, the term “backwashing” is short for “backflow washing.” Backflow washing refers to washing by sending a fluid in an opposite direction of the filtration flow. Also, the term “regeneration” refers to removal of impurities from an element and the regeneration of the element.
According to the present invention, there is provided a wastewater filtering apparatus for filtering wastewater in which solid matter is mixed, the apparatus comprising a container for storing the wastewater; a wastewater inlet tube that is connected to the container and that directs wastewater into the container; a tubular element that is disposed inside the container and that removes impurities containing the solid matter from wastewater that flows from an outside to an inside; a purified water transport tube for drawing out filtered purified water to the exterior of the container; a cleaning water spray tube that is disposed inside the container and that sprays cleaning water to an outside surface of the tubular element; a rotation mechanism for rotating the tubular element when the cleaning water is sprayed, and causing the outside surface of the tubular element to be uniformly aligned facing the cleaning water spray tube; a backflow supply tube for supplying fluid to the inside of the tubular element after the rotation by the rotation mechanism has been stopped, and washing the tubular element using the backflow; and a deposit transport tube which extends from a bottom of the container and whereby the impurities containing the solid matter that has been removed by the cleaning water and the fluid are discharged from the container.
There is an advantage in that the external peripheral surface of the tubular element is cleaned and most of the solid matter is removed in the first step, even fine solid matter that has been embedded on the filter in the second step can be removed by backwashing, and highly precise regeneration can be achieved. As a result, wastewater that contains large amounts of sand and the like can be treated.
Preferably, a plurality of the tubular elements is disposed about a periphery of the cleaning water spray tube. There is an advantage in that a plurality of the tubular elements can be cleaned by using a single purified water spray tube.
Desirably, the purified water transport tube is provided with an activated charcoal filter that further filters the filtered purified water. Very fine sand and the like that cannot be filtered by the tubular element can be reliably filtered. Filtration precision increases.
In a preferred form, the fluid for the backwashing be compressed air. The cleaning of the first step is performed using water, and most of the impurities are removed. The cleaning of the second step is adequately performed using compressed air. In accordance with the present invention, water can be conserved in comparison with the case in which water is used in the first and second steps.
A preferred embodiment of the present invention will be described in detail below, by way of example only, with reference to the accompanying drawings, in which:
As shown in
The rotation mechanism 25 has a rotating shaft 38 that extends in the front/rear direction of the diagram, a rotating shaft sprocket 39 provided to the rotating shaft 38, and a chain 41 that is disposed so as to make contact with rotating shaft sprocket 39 and the sprocket 24 and that drives the sprocket 24, as shown in
A motor 43 for driving the rotation mechanism 25 is provided to the upper portion of the cover 14, as shown in
The effect of the filtering apparatus having the configuration described above will be described next. In other words, an ordinary filtration operation will be described with reference to
The wastewater introduced from the wastewater inlet tube 27 into the container 11 flows from the external peripheral surface toward the internal peripheral surface of the tubular element 17, and the filtration of the first step is performed by the tubular element 17, as described in
Very fine sand and the like that could not be filtered by the tubular element 17 can be reliably filtered. Filtration precision increases.
Purified water that has been purified by the tubular element 17 and the activated charcoal filter 34 in the second step can thereby be obtained in a continuous fashion. However, sand and other solid matter that was contained in wastewater accumulates on the external peripheral surface of the tubular element 17 when the purification operation progresses, and filtration capacity is reduced. In view of the above, the regenerating operation is suitably carried out in the following manner.
First, the wastewater inlet valve 47 is closed in the first step of regeneration, and the introduction of wastewater to the container 11 is stopped, as shown in
When the discharge of wastewater is completed, the wastewater discharge valve 49 is closed, the motor 43 is actuated as indicated by the arrows, and the tubular element 17 is rotated. The cleaning water inlet valve 51 is opened at the same time. At this point, the cleaning water can be sent from the purified water tank 32 to the cleaning water spray tube 21 as indicated by the black arrows. The cleaning water is sprayed from the cleaning water spray tube 21 toward the external peripheral surface of the tubular element 17, and the deposits of tubular element 17 are cleaned in the manner indicated by the imaginary lines.
The large portion of solid matter accumulated on the external peripheral surface of the tubular element 17 can be removed by the cleaning water. The sediments in which sand and fine metals have become mixed in the sludge and hardened can be particularly effectively removed by the water pressure of the cleaning water.
Furthermore, since the tubular element 17 is rotated at a fixed speed by the motor 43, the cleaning water indicated by the imaginary lines uniformly makes contact with the entire periphery of the tubular element 17, and unclean areas do not occur. In other words, a plurality (e.g., six) of the tubular elements 17 can be cleaned in a single process by using a single cleaning water tube 21.
The cleaning water inlet valve 51 closes and cleaning by the purified water is ended when the cleaning is performed by the cleaning water spray tube 21 for a fixed length of time.
Next, in the second step of regeneration, the cleaning water inlet valve 51 is first closed, as shown in
The solid matter that is deposited on the external peripheral surface of the tubular element 17 is blown to the exterior by compressed air as indicated by the white arrows. The cleaning capacity is low because the density of air is less than that of water. However, in the present invention, the quantity of remaining deposits is low and the thickness of the layer is also low because a large portion of the sediments has been cleaned away in the first step of the regeneration operation. For this reason, cleaning is possible even using compressed air in the second step.
The cleaning of the second step can be performed using cleaning water, but the quantity of cleaning water that is used can be reduced when compressed air is used as in the present invention.
The backflow inlet valve 52 is closed and the backflow produced by the compressed air is ended after the backflow produced by the compressed air is carried out for a fixed length of time.
Next, the deposit transport valve 53 is opened. Solid matter collected in the bottom portion of the container 11 and the cleaning water used in the first step are thereby sent from the deposit transport tube 29 to the exterior as indicated by the white arrow in the lower portion of the diagram, and the cleaning of the tubular element 17 is ended.
Next, the overall operation of
A treatment flow rate Q1 is set in step (hereinafter abbreviated as ST) 01 in the manner shown in
The cumulative flow rate Q2 is examined as to whether the treatment flow rate Q1 has been reached (ST04). If the cumulative flow rate is less than Q1, the filtration of wastewater (ST02) continues, and the filtration stops when Q1 is reached (ST05). Specifically, the wastewater inlet valve 47 shown in
Wastewater inside the wastewater tank is discharged from the wastewater discharge outlet (ST06).
The tubular element is rotated (ST07), purified water is sprayed onto the external peripheral surface of the tubular element that is being rotated, and the tubular element is washed (ST08).
The tubular element is backwashed by compressed air (ST09).
The deposits collected in the lower portion of the wastewater tank and the purified water sprayed in ST08 are discharged to the exterior of the wastewater tank (ST10).
The filtration apparatus 10 described above can be provided to a variety of applications. An example in which the filtration apparatus is applied to a workpiece washing apparatus will be described below.
A workpiece washing apparatus 60 includes a reticulated workpiece mount 62 on which a workpiece 61 to be washed is mounted, and a wastewater tank 63 for receiving the wastewater generated when the workpiece 61 is washed, as shown in
One opening of a three-way valve 55 is connected to the flowmeter 35, one of the remaining openings of the three-way valve 55 is connected to the purified water tank 32, and the remaining opening is connected to the workpiece cleaning apparatus 60.
The purified water filtered through the filtration apparatus 10 is allowed to flow to the purified water tank 32 until a prescribed quantity is collected in the manner indicated by arrow (1). The three-way valve 55 is switched when the prescribed quantity of purified water is collected in the purified water tank 32. The purified water is then sent to the workpiece cleaning apparatus 60 when the three-way valve 55 switches in the manner indicated by arrow (2).
The workpiece 61 is cleaned in the manner indicated by the arrow (4) by purified water sent to the workpiece cleaning apparatus 60, and purified water is introduced from a workpiece cleaning water inlet tube 64 in the manner indicated by arrow (3). Sand and the like that have been deposited on the workpiece 61 by cleaning the workpiece 61 is made to fall into the wastewater tank 63 together with water in the manner indicated by arrow (5).
The wastewater collected in the wastewater tank 63 passes through the wastewater inlet tube 27 in the manner indicated by arrow (6), and is introduced into the filtration apparatus 10. The wastewater thus introduced is filtered inside the filtration apparatus 10, and steps (1) through (6) are repeated.
Wastewater is not required to be discarded and a contribution is made to environmental conservation because purified water that has been filtered is used to wash the workpiece 61. The quantity of purified water introduced from the workpiece cleaning inlet tube 64 can be reduced. In addition, purified water obtained by filtration is made to flow into the purified water tank, and the element is regenerated using purified water. The quantity of purified water introduced from the exterior can be reduced, as can running costs of using the filtration apparatus.
Obviously, various minor changes and modifications of the present invention are possible in light of the above teaching. It is therefore to be understood that within the scope of the appended claims the invention may be practiced otherwise than as specifically described.
Number | Date | Country | Kind |
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2007-099477 | Apr 2007 | JP | national |
2008-022946 | Feb 2008 | JP | national |