JP2010234327A - Coagulation separation apparatus for treatment water - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a coagulation separation apparatus for treatment water which achieves the miniaturization of the coagulation separation apparatus by incorporating a slow stirring tank and a magnetic separator in a contaminated water purifying system into the same casing for integration. <P>SOLUTION: The coagulation separation apparatus comprises slow stirring tanks A1, A2 and A3 which form magnetic flocks by adding magnetic powder and a coagulant to the treatment water and stirring them for coagulating the contaminants in the treatment water; and a magnetic separator B for adsorbing and recovering the magnetic flocks. Among the tanks constituting the slow stirring tanks A1, A2, A3 and the magnetic separator B, at least a plurality of tanks are arranged adjacent to each other and incorporated into the same casing for integral constitution. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to an apparatus for aggregating and separating treated water, and in particular, in a polluted water purification system in which contaminants in treated water such as sewage and factory wastewater are aggregated to generate and remove magnetic floc, a slow agitator In addition, the present invention relates to a coagulation / separation apparatus for treated water in which a pipe for connecting each tank is eliminated by incorporating and integrating a magnetic separation apparatus in the same casing.

Conventionally, in order to remove pollutants present in treated water such as ballast water and factory effluent, magnetic powder and flocculant (polymer flocculant if necessary) are added to the treated water and agitated. A polluted water purification system is adopted in which a magnetic floc is made magnetic, and the generated magnetic floc is adsorbed to a rotating magnetic disk and separated and removed.
The aggregating apparatus A is used as a means for generating the magnetic floc, and the magnetic separating apparatus B configured by arranging a large number of magnetic disk disks having a large number of magnets arranged at predetermined intervals as means for attracting, separating and removing the magnetic floc. It has been adopted.

  However, as shown in FIG. 6, the flocculating / separating apparatus in the conventional polluted water purification system adds a magnetic powder and a flocculant to the treated water, supplies them into the rapid stirring tank C, and rapidly agitate them. Slowly stirring in the slow-speed stirring tanks A1, A2 and A3 divided into stages and slowly stirring in each tank makes the pollutants present in the treated water such as ballast water and factory wastewater magnetized. Magnetic flocs are generated, and stirring blades are arranged in the slow stirring tanks A1, A2, A3 so that the treated water can be stirred at a predetermined speed.

Further, between the rapid stirring tank C of the agglomeration apparatus A and the first slow stirring tank A1, between the slow stirring tanks A1 and A2 of each stage, between the slow stirring tanks A2 and A3, and the slow stirring of the last stage. The tank A3 and the magnetic separator B are connected so as to be connected via pipes D1, D2, D3, and D4, respectively, so that the treated water sequentially flows between the stirring tanks C, A1, A2, and A3. Yes.
For this reason, since the aggregating apparatus A is formed of a separate body in which a plurality of slow stirring tanks and magnetic separation apparatuses are independently formed and connected by piping, the apparatus itself is enlarged, There was a problem that the space for installing this also increased.

  In addition, the flow rate of the treated water is the slowest between the slow-speed agitation tank A3 in the final stage and the magnetic separation device B, so that the magnetic floc settles on the bottom of the pipe, so that the magnetic floc sedimentation prevention to prevent this occurs Although there is no particular limitation on the apparatus E, for example, there is a problem that it is necessary to install a stirrer or the like for winding up the magnetic floc in the pipe D4.

  In view of the problems of the treated water coagulation / separation device, the present invention can reduce the size of the coagulation / separation device by integrating the slow stirring tank and the magnetic separation device in the contaminated water purification system into the same casing. An object of the present invention is to provide an apparatus for aggregating and separating treated water.

  In order to achieve the above object, a slow stirring tank in which magnetic powder and a flocculant are added to the treated water and stirred to agglomerate contaminants in the treated water to generate a magnetic floc, and a magnetic floc is provided. In the coagulation / separation apparatus constituted by the magnetic separation apparatus adapted to perform adsorption / recovery, at least a plurality of tanks of the slow stirring tank and the tank constituting the magnetic separation apparatus are arranged adjacent to each other and integrated in the same casing. It is characterized by comprising.

  In this case, at least one of an inorganic flocculant and a polymer flocculant can be used as the flocculant.

  Moreover, the tank arrange | positioned adjacently can be connected directly by forming the distribution port of the treated water in the partition of the tank arrange | positioned adjacently.

  In addition, the slow stirring tank is a multistage continuous multi-stage slow stirring tank, and the treated water is circulated in the partition between adjacent slow stirring tanks so that the treated water flows in each slow stirring tank in order. While forming a mouth, it can comprise and comprise a stirring blade in each slow stirring tank.

  In addition, the flow port of the treated water formed in the slow stirring tank partition adjacent to the multistage slow stirring tank is set so that the magnetic floc generated in each slow stirring tank is not destroyed by the flow rate of the treated water. The size can be set.

  In addition, in the multistage slow stirring tank and in the vicinity of the treated water inlet, a depressing plate for weakening the force of the treated water flowing in can be provided.

  The apparatus for aggregating and separating treated water according to the present invention includes a slow stirring tank in which magnetic powder and a flocculant are added to treated water and agitation is performed to agglomerate contaminants in the treated water to generate magnetic flocs. In the coagulation / separation apparatus constituted by the magnetic separation apparatus that adsorbs and collects the magnetic flocs, at least a plurality of tanks among the slow stirring tank and the tank constituting the magnetic separation apparatus are arranged adjacent to each other in the same casing. Built-in and integrated configuration eliminates the need for piping connecting between the multi-stage slow stirring tanks, so that the apparatus can be miniaturized and can be easily configured, and convection of treated water between the tanks. And the flow can be smoothed to promote the generation of magnetic flocs.

  In addition, by using at least one of an inorganic flocculant and a polymer flocculant as the flocculant, the flocculant is used according to the properties of the target treated water, thereby further promoting the generation of magnetic flocs. can do.

  Moreover, the tank structure can be simplified by forming the circulation port of the treated water in the partition wall of the adjacently disposed tanks and directly communicating the adjacently disposed tanks.

  In addition, the slow stirring tank is a multistage continuous multi-stage slow stirring tank, and the treated water is circulated in the partition between adjacent slow stirring tanks so that the treated water flows in each slow stirring tank in order. By forming a mouth and providing a stirring blade in each slow stirring tank, the connection between each tank can be reliably and easily connected, and the retention of treated water at the connecting section between the tanks can be prevented. .

  In addition, the flow port of the treated water formed in the slow stirring tank partition adjacent to the multistage slow stirring tank is set so that the magnetic floc generated in each slow stirring tank is not destroyed by the flow rate of the treated water. By setting the size, the generation of the magnetic floc can be ensured.

  Dispersion of treated water into the slow agitation tank by disposing a depressing plate in the multistage slow agitation tank near the treated water inlet to reduce the flow of treated water. Thus, the water can be uniformly stirred in the tank, and the generation of magnetic floc can be promoted.

It is a front view which shows one Example of the coagulation separation apparatus of the treated water of this invention. It is the same side surface longitudinal cross-sectional view. It is block explanatory drawing of the coagulation separation apparatus of the treated water of this invention. It is explanatory drawing of the slow stirring tank provided with the circulation port. It is explanatory drawing which shows the modification of the arrangement structure of a slow stirring tank and a magnetic separation apparatus. It is block explanatory drawing of the conventional coagulation-separation apparatus of a treated water.

  Hereinafter, an embodiment of an apparatus for aggregating and separating treated water of the present invention will be described with reference to the drawings.

  1 to 4 show an embodiment of the apparatus for aggregating and separating treated water of the present invention.

  As shown in FIG. 3, a polluted water purification system for separating and removing magnetic substances from pollutants present in treated water such as ballast water and industrial wastewater as magnetic flocs has a rapid stirring tank C, a coagulating apparatus A and It consists of a magnetic separator B.

  In addition, treatment water such as ballast water and factory effluent needs to be used in advance when an appropriate amount of magnetic powder and flocculant, for example, inorganic flocculant, and magnetic flocs to be generated need to be increased. Accordingly, the polymer flocculant is added and supplied to the rapid stirring tank C, and since the stirring blade S is provided in the tank, the treated water is rapidly stirred and in the slow stirring tank of the next step. To facilitate the generation of magnetic flocs at

  Here, although not particularly limited, the magnetic powder added to the treated water is an iron oxide powder such as triiron tetroxide, and the inorganic flocculant is polyaluminum chloride, iron chloride, sulfuric acid As the water-soluble inorganic flocculant such as ferric iron, and as the polymer flocculant, anionic or nonionic polymer flocculants can be preferably used.

  Then, the rapid stirring tank C and the first slow stirring tank A1 of the aggregating apparatus A are connected by the pipe D1 as in the prior art, and the rapidly stirred treated water quickly enters the first slow stirring tank A1. To be introduced.

  In addition, as shown in FIGS. 3 to 4, the aggregating apparatus A is not limited to a plurality of stages. For example, three stages of slow stirring tanks A1, A2, and A3 are arranged in series. In each of the slow stirring tanks A1, A2, and A3, the treated water to which the magnetic powder and the flocculant have been added in the previous step is stirred at a slow speed to make the pollutants magnetic and generate magnetic flocs. A stirring blade S that rotates slowly is provided. The rotational speed of the stirring blade S provided in each slow stirring tank is determined so as not to destroy the magnetic floc being formed.

  As shown in FIGS. 1, 3 and 4, the slow stirring tanks A1, A2 and A3 formed in a multi-stage system are connected to each other in the lateral direction so as to be continuously connected without piping. It arrange | positions so that it may adjoin to the vertical direction, and between 1st slow stirring tank A1 and 2nd slow stirring tank A2, and 2nd slow stirring tank A2 and 3rd slow stirring so that treated water may distribute | circulate sequentially. A circulation port is formed in the partition between the tanks A3.

  For example, as shown in FIG. 4, between the first slow stirring tank A1 and the second slow stirring tank A2, flow ports 11 and 12 formed at appropriate positions on the same side walls of the tanks A1 and A2, respectively. The space is communicated via a circulation duct 15 disposed outside the tank.

  In this case, the inlet 10 is formed in the first slow stirring tank A1 so as to introduce the treated water from the rapid stirring tank C through a pipe. Desirably, the inlet 10 is as shown in FIG. In addition, the biasing plate 16 is disposed in the first slow stirring tank A1 so as to be disposed at a position in contact with the wall surface and to face the inlet 10 with a slight gap.

  As a result, the treated water introduced from the inflow port is diffused by the force reducing plate 16 and flows into the first slow stirring tank A1, and is uniformly stirred in the tank by the stirring blade S. After that, it is discharged from the circulation port 11 and introduced into the second slow stirring tank A2 from the circulation port 12 through the circulation duct 15, and further, the second slow stirring tank A2 and the third slow stirring tank. The circulation port 13 between the tanks A3 is formed by providing openings directly in the partition walls that are in contact with each other.

  Further, the magnetic separation device B is disposed so as to be stacked above the third slow stirring tank A3, and the flow port 14 is formed in the partition wall connecting the third slow stirring tank A3 and the magnetic separation device B.

  In this case, each of the flow ports 11, 12, 13, and 14 has treated water that sequentially flows between the slow stirring tanks A1, A2, and A3 so that the magnetic flocs that are being formed are not destroyed and the magnetic flocs are increased. The degree of opening is set so that the flow rate gradually decreases so as to grow.

Further, the inlet and outlet formed in one tank, for example, the inlet 10 formed in the first slow stirring tank A1 and the circulation port 11 serving as the outlet are preferably formed at diagonal positions of the tank. .
Thereby, it is possible to prevent the treated water from flowing out by short-circuiting the inside of the tank (shortcut of flow), and it is possible to impart sufficient residence time (processing time) in the tank to the treated water.

Further, the magnetic separation device B constitutes the magnetic disk 2 by arranging a large number of magnetic disk disks 22 having a large number of magnets arranged in a main body casing 20 (magnetic separation tank) on a rotatable main shaft 21 at predetermined intervals. Then, by rotating the magnetic disk 2, the magnetic flocs generated in the slow stirring tanks A 1, A 2 and A 3 in the previous process are attracted to each magnetic disk disk 22 and inserted between the magnetic disk disks. It is configured to be removed via the magnetic floc discharging means provided.
In this case, the entire magnetic disk 2 or a predetermined area (specifically, about 1/2 or more, preferably about 2/3 or more) is immersed in the treated water supplied into the main body casing 20. Thus, the magnetic floc generated in the treated water is efficiently adsorbed.

Here, the arrangement of the multistage slow stirring tanks A1, A2, A3 and the magnetic separation device B is not particularly limited. For example, as shown in FIG. 1 and FIG. The second slow stirring tank A2 is disposed below the tank A1, and the third slow stirring tank A3 is disposed laterally of the second slow stirring tank A2, and the first above the third slow stirring tank A3. The magnetic separation device B is arranged adjacent to the slow stirring tank A1 in the lateral direction, or as shown in FIG. 5A, the first slow stirring tank A1 and the second slow stirring tank A2. And the third slow stirring tank A3 are arranged in series, and the magnetic separation device B is arranged above the third slow stirring tank A3, or as shown in FIG. 5 (b), the first slow stirring tank A3 is arranged. The tank A1, the second slow stirring tank A2, and the third slow stirring tank A3 are sequentially arranged in a bowl shape, and the magnetic separation device B is disposed above the third slow stirring tank A3. Etc. to be arranged, it can be any arrangement.
Thereby, since the partition of each tank is adjoined, it can communicate between each tank and can form a flow path only by forming opening in a partition, without using piping.
In particular, by arranging the magnetic separation device B above the third slow stirring tank A3 which is the last slow stirring tank, the magnetic floc contained in the treated water discharged from the third slow stirring tank A3 is piped. Therefore, the maintenance work can be simplified.

Next, the operation of this treated water aggregating and separating apparatus will be described.
The treated water to which the magnetic powder and the flocculant have been added in advance is introduced into the rapid stirring tank C, rapidly stirred by a stirring blade (not shown), and then into the first slow stirring tank A1 via the pipe D1. When guided, it is slowly stirred by the stirring blade in the tank. From the first slow agitation tank A1 to the second slow agitation tank A2 through the circulation port 11, the circulation duct 15, and the circulation port 12 formed by openings formed in the partition wall, the circulation port from the second slow agitation tank A2 13, the sludge substance in the treated water is agglomerated by slowly agitating with the agitating blades S arranged in the respective tanks to the third slow agitating tank A3. Generate.

  In this case, there is no adjacent piping between the tanks, and the process water is smoothly circulated through the flow port formed by the opening formed directly in the partition wall, so that the treated water can be smoothly distributed and the third slow stirring is performed. Between the tank A3 and the magnetic separation device B, without introducing a pipe, the introduction is made through the circulation port 14 constituted by the opening directly formed in the partition wall. Sedimentation can also be prevented and the entire treated water can be reliably supplied to the magnetic separation device B, and the apparatus can be miniaturized because the respective tanks are stacked in a block shape.

  In this embodiment, the first slow stirring tank A1, the second slow stirring tank A2, the third slow stirring tank A3, and the magnetic separation device B are integrated and arranged. The tank to arrange | position is not limited to this combination, Arbitrary arbitrary tanks are combined (it is not specifically limited, For example, 1st slow stirring tank A1, 2nd slow stirring tank A2, and 3rd slow speed) The stirring tank A3 can be combined, or the second slow stirring tank A2, the third slow stirring tank A3, and the magnetic separator B can be combined.) These tanks are arranged adjacent to each other in the same casing. Can be.

  The magnetic separation device B for separating the magnetic flocs is an arbitrary magnetic separation device using a magnet (including an electromagnet) in addition to the magnetic disk 2 configured by arranging the magnetic disk board 22 on the rotatable main shaft 21. Can be used.

  As mentioned above, although the coagulation separation apparatus of the treated water of this invention was demonstrated based on the Example, this invention is not limited to the structure described in the said Example, In the range which does not deviate from the meaning, the The configuration can be changed.

  The treated water aggregating and separating apparatus of the present invention has a characteristic that the apparatus can be reduced in size by incorporating a slow stirring tank and a magnetic separating apparatus composed of a plurality of stages into the same casing without piping. It can use suitably for the use of the coagulation separation apparatus of treated water.

A Coagulation device A1 1st slow stirring tank A2 2nd slow stirring tank A3 3rd slow stirring tank B Magnetic separation device C Rapid stirring tank D1 Piping S Stirring blade 10 Inlet 11-14 Flowing port 15 Flowing duct 16 Reduction Power plate 2 Magnetic disk 20 Main body casing 21 Spindle 22 Magnetic disk board

Claims (6)

  Magnetic powder and flocculant are added to the treated water, and stirred to agitate the pollutants in the treated water to produce magnetic flocs, and the magnetic flocs to absorb and collect the magnetic flocs In the coagulation / separation apparatus constituted by the separation apparatus, at least a plurality of the tanks constituting the slow stirring tank and the magnetic separation apparatus are arranged adjacent to each other and incorporated in the same casing, and are configured integrally. A coagulation / separation device for treated water.   The apparatus for coagulating and separating treated water according to claim 1, wherein at least one of an inorganic coagulant and a polymer coagulant is used as the coagulant.   The apparatus for aggregating and separating treated water according to claim 1 or 2, wherein the treated water is directly connected to each other by forming a treated water circulation port in a partition wall of the adjacently arranged tank.   The slow-speed agitation tank is a multi-stage continuous slow-speed agitation tank, and the treated water circulation port is provided in the partition wall between adjacent slow-agitation tanks so that the treated water flows through each of the slow-speed agitation tanks sequentially. The apparatus for aggregating and separating treated water according to claim 1, 2 or 3, wherein the apparatus comprises a stirring blade in each slow stirring tank.   The flow rate of the treated water formed in the partition wall of the slow stirring tank adjacent to the multistage slow stirring tank should be sized so that the magnetic flocs generated in each slow stirring tank are not destroyed by the flow rate of the treated water. The apparatus for aggregating and separating treated water according to claim 1, 2, 3, or 4, characterized in that it is set.   6. A derating plate is provided in the multi-stage slow stirring tank and in the vicinity of the treatment water inlet for reducing the force of the treated water flowing in. An apparatus for aggregating and separating treated water as described.

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