JP2009279485A - Separation device and separation method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a separation device and a separation method which can treat the whole amount of supplied liquid, hardly causes clogging and can separate even fine solid matter. <P>SOLUTION: The separation device 1 for separating solid matter K contained in liquid is provided with a separation container 2 of a closed type in which a swirling flow region S is disposed, wherein a supply part 3 of liquid and a wedge-wire screen 5 for separating the solid matter K are formed on a wall 2c constituting the separation container 2, the supply part 3 is configured so as to jet pressurized liquid in the tangential direction of the swirling region S and produce a swirling flow of liquid in the swirling region S and the wedge-wire screen 5 is formed on the wall 2c contacting with the swirling region S. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a separation apparatus and a separation method used for efficiently separating solid impurities contained in a liquid in wastewater treatment facilities such as drainage treatment facilities of various factories and plants and sewer pipes.

  Factories and various plant facilities are provided with treatment facilities for separating solids from wastewater and liquid. For example, waste water that has washed an object often contains fine solids, and the solids are separated by a separation device equipped with a filter or the like, and only the cleaned washing waste water is discharged out of the system or re-used. We use for use. In addition, various liquid products may contain fine solids as impurities during the manufacturing process, and similar separation devices are provided to separate the solids from the liquid.

  In addition, drainage of rainwater and the like flowing into sewer stormwater drainage treatment facilities laid in urban areas is partly stored or discharged in the ground by rainwater storage and penetration facilities and the rest is discharged into rivers and the like. The rainwater flowing through the sewer is contaminated with solid impurities such as earth and sand, various garbage, paper, and fallen leaves (hereinafter simply referred to as solids), and these solids flow into the river. This causes water pollution and environmental pollution, and if it flows into the rainwater storage and penetration facility without treatment, it is necessary to frequently maintain the facility, which is disadvantageous in terms of cost. In particular, infiltration facilities may cause a decrease in osmotic function, making it difficult to use for a long period of time. Therefore, a wastewater separation device for separating solids is provided in a part of the sewer.

  As a device for separating solids from wastewater, there is a swirling flow type separation device that generates a swirling flow (swirl) in the horizontal direction in the wastewater and separates the solids by the swirling flow, for example, trade name of UFT in Germany Fluid Sepp is known. However, a separation apparatus that does not have a filter or a screen is easy to maintain, but it is difficult to reliably separate and capture floating solids and fine solids.

  Patent Document 1 discloses a separation device that combines a swirl flow generation method and a screen separation method. In the separation tank of Patent Document 1, a cylindrical screen is disposed below a separation tank having a circular plane cross section, and a swirling flow is generated in the tank by supplying waste water in a tangential direction from above the separation tank. Solids are separated by a screen arranged in the screen, and only waste water is allowed to pass outside the screen.

  On the other hand, Patent Document 2 discloses a purification device that uses a swirling flow to purify bathtub water. The purification device described in Patent Document 2 uses a filter in which a stainless woven filter laminated with a reinforcing plate made of a porous sintered plate is housed in a container.

  In this purification device, the bathtub water to be purified from the bathtub is pumped in the tangential direction of the container to generate a swirling flow in the container, and the solid matter is captured and separated by the filter to obtain clean bathtub water in the bathtub. It is returning. And the solid substance adhering to the filter is removed by the backwash operation performed periodically. When the solid matter is separated while generating the swirling flow in this way, the solid matter adhering to the filter surface is concentrated and attached in the central direction of the swirling flow, so that clogging of the entire filter can be suppressed. Has been.

JP-A-8-141326 JP-A-2005-74058

  All of the conventional swirling flow type separation devices or the separation devices combining swirling flow and a screen are open-type that is operated at normal pressure with the upper part of the device being open to the atmosphere. In such an open type separation apparatus, for example, when the supply amount of the liquid to be processed increases beyond the processing capacity, a part of the supplied liquid overflows the apparatus without being processed and is discharged downstream. .

  Since the liquid processing capacity in an open type separation apparatus is limited by the liquid passing area of the filter or screen, the liquid passing area has to be increased in order to increase the processing capacity. There is a problem that the installation area and cost of the increase. Furthermore, solids may have to be separated from the liquid even in a system in which the liquid pressurized by a pressurizing means such as a pump circulates. However, an open type separation apparatus is applicable to such a pressurized system. I can't do it.

  On the other hand, in Patent Document 2, bath water pressurized by a pump is supplied to a filter, and solids are separated while generating a swirl flow there, but the back surface of a stainless woven filter, which is a flexible fabric, is reinforced with a reinforcing plate. In addition, a swirl flow is generated along the surface of the stainless woven filter. Such a fabric filter has a problem that the solid matter adhering to the structure is easily entangled with the weave.

  Therefore, in Patent Document 2, clogging is suppressed by using a swirling flow, but since the surface of a flexible stainless woven filter is easily deformed, the pressure applied by the pump is limited. Therefore, the flow velocity of the generated swirling flow is also suppressed to a low level, and the solid matter entangled with the swirling flow having such a low flow velocity cannot be efficiently separated. As a result, the adhering solid matter is not peeled to such an extent that it gradually moves to the center side of the swirling flow between the filter textures by the moving force of the swirling flow, and the clogging preventing effect is limited. Therefore, in Patent Document 2, a switching valve is provided in the bathtub water system, and backwashing is periodically performed to remove the solid matter from the filter.

  However, frequent backwashing operations are not preferable because the consumption of backwashing water increases and the separation efficiency of solids per hour decreases. SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to solve the problems in such a conventional liquid separation device, and to provide a new separation device and a separation method using the same.

  A first separation device of the present invention that solves the above-described problem is a device for separating solids contained in a liquid, and includes a closed-type separation container provided with a swirl flow region therein, and constitutes the separation container. A liquid supply unit and a wedge wire screen for separating solids are formed on the wall, and the supply unit ejects the pressurized liquid in a tangential direction of the swirl flow region so that the swirl flow of the liquid flows into the swirl flow region. The wedge wire screen is formed on the wall in contact with the swirl flow region.

  Further, the second separation device is the above-described first separation device, wherein the separation container is formed in a rectangular parallelepiped shape, a supply portion is formed on one side of the rectangular parallelepiped wall, and the wall side facing the wall on which the supply portion is formed. Is provided with a derivative having an inclined part or an arc part, and the supply part ejects liquid pressurized in the direction of the derivative, so that the liquid changes its direction at the inclined part or arc part of the derivative and swirls. And the screen is formed on one or both of the walls sandwiching the derivative.

  Further, the third separation device according to the second separation device, wherein the separation container is provided with a division body for dividing the inside into a first chamber and a second chamber, an opening is formed in the division body, The swirl flow region is provided in one chamber and a supply portion is formed, and the wedge wire screen is formed in the first chamber or in at least a part of the first chamber and the second chamber, and in the second chamber. Is provided with a depositing portion of solid matter flowing in from the opening.

  Further, the fourth separation device according to any one of the first to third separation devices, wherein a discharge chamber is provided outside the separation container, and the liquid in the separation container passes through the screen and is ejected to the discharge chamber. It is composed of.

  Further, a fifth separation device according to any one of the first to third separation devices is provided with a plurality of the separation containers, and provided with distribution pipes that distribute and supply liquid to the supply portions of the separation containers, A common discharge chamber is provided outside each separation container, and the liquid in each separation container passes through the wedge wire screen and is ejected to the discharge chamber.

  The first separation method of the present invention is a method for separating a solid contained in a liquid, wherein any one of the first to fifth separation devices is used, and a liquid pressurized from the supply unit is removed. A liquid swirl flow is generated in the swirl flow region by being ejected in a tangential direction of the swirl flow region, and the liquid from which the solid matter is separated by the wedge wire screen is ejected to the outside of the separation container. It is.

  Further, the second separation method is the first separation method, wherein the pressurized liquid ejected from the supply unit is arranged to cause the swirl flow region to generate a vertical or horizontal swirl flow in the swirl flow region. It is characterized by arranging.

  In addition, the third separation method is the first separation method, wherein the separation container is disposed so that the pressurized liquid ejected from the supply unit generates a horizontal swirl flow in the swirl flow region, The separation vessel is characterized in that the wedge wire screen is formed only on the upper side of the generated swirling flow.

  Further, the fourth separation method is the above-described first separation method, wherein the pressurized liquid ejected from the supply unit generates a swirling flow in an inclined direction between the vertical direction and the horizontal direction in the swirling flow region. The separation container is arranged as described above, and the wedge wire screen is formed only on the upper side of the generated swirl flow as the separation container, and the solid discharge unit is formed on the wall constituting the lower end portion in the inclined direction. The solid material deposited inside the separation container is discharged from the discharge portion.

  The first separation device of the present invention includes a closed-type separation container provided with a swirl flow region therein, and a wedge wire screen for separating a liquid supply unit and solid matter is formed on a wall constituting the separation container, The supply unit is configured to eject a pressurized liquid in a tangential direction of the swirl flow region to generate a swirl flow of the liquid in the swirl flow region, and the wedge wire screen is disposed in the swirl flow region. It is formed in the said wall which touches, It is characterized by the above-mentioned.

  The wedge wire screen used in the first separating apparatus of the present invention is formed by arranging a plurality of wedge wires having a wedge-shaped cross section in parallel with each other, but is not suitable for metals such as stainless steel or hard plastics. Because it is made of a hard material, it has high rigidity and does not easily deform. Therefore, the pressure of the liquid supplied to the separation container can be increased, and a high-speed swirling flow can be generated. Unlike the fibrous filter, the wedge wire screen does not have a texture, and the liquid passes through a large number of parallel slits.

  Therefore, as described above, when the wedge wire screen is used to generate a high-speed swirling flow, the solid matter attached to the wedge wire screen is efficiently peeled off and the clogging suppressing effect is remarkably enhanced. Therefore, even if a case where a backwash operation is required occurs, the interval can be significantly increased.

  In addition, when the pressure of the liquid to be supplied is increased, the amount of liquid passing through the screen is increased in proportion thereto, and the rotational speed of the swirl flow is also increased, but the liquid overflow phenomenon does not occur as in the open type separation device. . Therefore, there is an advantage that the liquid throughput can be increased by increasing the pressure of the supplied liquid without increasing the liquid passing area of the screen.

  The wedge wire screen can efficiently separate even fine solid impurities by reducing the arrangement interval (slit interval) of the wedge wires. Further, since it is made of a hard material as described above, there is no fear of breakage and the like, and cleaning with high-pressure water or the like inside and outside the separation container is possible.

  Further, in the second separation device, in the first separation device, the shape of the separation container is formed in a rectangular parallelepiped, a supply portion is formed on one side of the rectangular parallelepiped wall, and the wall facing the wall on which the supply portion is formed A derivative having an inclined part or an arc part is provided on the side, and the supply part is configured to eject a liquid pressurized in the direction of the derivative and change the direction at the inclined part or the arc part to generate a swirling flow. A wedge wire screen can be formed on one or both of the walls.

  By forming the separation container in a rectangular parallelepiped in this way and providing the derivative, the generation of the swirl flow in the swirl flow region can be more easily and reliably maintained, so that even if the liquid processing capacity varies greatly, Separation is possible. Further, when screens are formed on both walls sandwiching the derivative, liquid is ejected equally from the wedge wire screens on both, and a swirling flow is generated at the center of the swirling flow region. For this reason, the solid matter does not adhere to one wedge wire screen.

  Further, in the third separation device, when the separation container in the second separation device is formed in a rectangular parallelepiped, a partition body for dividing the inside of the separation container into a first chamber and a second chamber is provided, and the partition body is opened. The first chamber is provided with a swirl flow region and a supply portion, and a wedge wire screen is formed in the first chamber or in at least a part of the first chamber and the second chamber, The two chambers can be provided with a solid depositing portion flowing from the opening.

  When the separation container is divided into the first chamber and the second chamber in this manner, the solid matter can be separated in the first chamber and the solid matter separated in the second chamber can be deposited. That is, in the first chamber, the solid matter is separated by the wedge wire screen, and the solid matter is separated from the wedge wire screen by the formation of the swirl flow, and the solid matter separated in the first chamber is formed into a divided body. It is guided to the second chamber from the opened opening and falls (or discharged). Therefore, the ratio of the solid matter separated by the wedge wire screen staying in the swirl flow for a long time inside the first chamber, which is the main separation region, is reduced, and as a result, the separated solid matter is removed from the screen in the first chamber. Since the possibility of reattaching to the surface is greatly reduced, high separation efficiency can be maintained for a long time.

  In the fourth separation device, in any of the first to third separation devices, a discharge chamber is provided outside the separation container so that the liquid in the separation container is ejected to the discharge chamber through the wedge wire screen. Can be configured. When such a discharge chamber is provided, when the separation device is inserted into the pipeline of the liquid processing system, the separation container is connected to the upstream line of the processing system, and the discharge chamber is connected to the downstream line of the processing system. Can be connected.

  Furthermore, in the fifth separation device, in any of the first to third separation devices, a plurality of separation containers are provided, and a distribution pipe that distributes and supplies the liquid to the supply unit of each separation container is provided. A common discharge chamber can be provided outside the separation container, and the liquid in each separation container can pass through the wedge wire screen and be ejected to the discharge chamber. By providing a plurality of separation containers in this way, the liquid processing capacity can be increased or decreased as required. In addition, by providing a common distribution pipe and discharge chamber, when the separation device is inserted into the liquid processing system, the upstream side of the processing system can be connected to the distribution pipe, and the downstream side of the processing system can be connected to the discharge chamber. As a result, the connection form can be simplified.

  Further, in the first separation method of the present invention, a swirling flow is produced by using any one of the first to fifth separation devices and ejecting the pressurized liquid from the supply section in the tangential direction of the swirling flow region. A swirling flow of liquid is generated in the region, and a liquid obtained by separating solids with a wedge wire screen is ejected to the outside of the separation container. According to this separation method, the solid matter attached to the wedge wire screen can be peeled off by the swirling flow, and therefore the solid matter can be efficiently separated from the liquid without causing the wedge wire screen to be blocked for a long period of time. Further, by increasing the pressure of the liquid to be supplied, the liquid throughput can be greatly increased as compared with the open type separation device without increasing the liquid passing area of the wedge wire screen.

  In the second separation method, in the first separation method, the separation container is disposed so that the pressurized liquid ejected from the supply unit generates a swirl flow in the vertical direction or the horizontal direction in the swirl flow region. can do. Depending on the type and nature of the liquid or solid matter, or due to restrictions on the installation location of the separation container, it may be preferable to generate a vertical swirl flow or a horizontal swirl flow. The separation apparatus of the invention can meet these demands only by changing the arrangement of the separation container.

  Further, in the third separation method, in the first separation method, the separation container is arranged so that the pressurized liquid ejected from the supply unit generates a horizontal swirl flow in the swirl flow region. A structure in which a wedge wire screen is formed only on the upper side of the generated swirling flow can be used. If it does in this way, it will become easy to deposit the solid substance with comparatively large specific gravity which circulates on a swirl flow near the bottom of a separation container. In addition, when the wedge wire screen is formed only on the upper part, it is difficult for solid matter to adhere to the wedge wire screen, and when the solid matter adheres, the solid matter is easily peeled off.

  Further, in the fourth separation method, in the first separation method, the pressurized liquid ejected from the supply unit generates a swirl flow in an inclined direction between the vertical direction and the horizontal direction in the swirl flow region. A separation container is arranged on the wall, a wedge wire screen is formed only on the upper side of the generated swirl flow, and a solid material discharge part is formed on the wall constituting the lower end part in the inclined direction. The solid matter accumulated inside the separation container can be discharged from the discharge portion.

  In this way, solids with relatively large specific gravity that circulate on the swirl flow easily accumulate near the bottom of the separation container, and the accumulated solids move downward along the slope and concentrate. From there, the solid matter can be easily discharged to the outside. In addition, when the wedge wire screen is formed only on the upper part, it is difficult for solid matter to adhere to the wedge wire screen, and when the solid matter adheres, the solid matter is easily peeled off.

  Next, the best mode for carrying out the present invention will be described with reference to the drawings. 1A and 1B are views showing a first embodiment of the separation apparatus of the present invention, in which FIG. 1A is a cross-sectional view taken along line AA in FIG. 1B, and FIG. 1B is a cross-sectional view taken along line BB in FIG.

  The separation device 1 includes a closed type separation container 2 having a swirl flow region S therein. The separation container 2 is a rectangular parallelepiped surrounded by an upper wall 2a, a lower wall 2b, and a peripheral wall 2c made of, for example, a metal plate such as a stainless steel plate or a plastic plate, and one side of the peripheral wall 2c constituting the rectangular parallelepiped (FIG. 1 ( A supply part 3 for supplying pressurized liquid is formed on the left peripheral wall 2c) of b). For example, an upstream pipe (not shown) of a drain pipe of a factory is connected to the supply unit 3. The “closed type separation container 2” referred to in the present invention is a separation container 2 having a structure in which a pressurized liquid supplied from the supply unit 3 is closed so as not to be ejected outside except a screen 5 described later. Means.

  On the side of the peripheral wall 2c facing the peripheral wall 2c on which the supply unit 3 is formed (on the side of the peripheral wall 2c on the right side of FIG. 1B), an inclination that extends linearly from the upper wall 2a to the peripheral wall 2c is extended. There are provided a first derivative 4 having a portion and a second derivative 4a having an inclined portion inclined linearly from the peripheral wall 2c to the lower wall 2b. These derivatives 4 and 4a are made of the same material as that of the separation container 2, but may have an arc portion that extends in an arc shape instead of the inclined portion. Further, the inclined portion and the arc portion may be formed in a V shape or an arc shape whose cross-sectional shape orthogonal to the extending direction is limited to a linear shape. It is preferable to form such a V shape or an arc shape since the flow velocity of the swirl flow is more uniform in the width direction perpendicular to the swirl direction than in the case of the straight shape.

  Note that at least one of the derivatives 4 and 4a may be omitted depending on circumstances.

  The supply unit 3 ejects the pressurized liquid in the tangential direction of the swirl flow region S (specifically, it ejects along the peripheral region Sa in the swirl flow region), so that the swirl flow region S has an arrow-like shape. A swirl flow is generated. Here, the swirl flow region S is formed by the inner surface of the wall of the separation container 2, but the peripheral region Sa has a certain width inward from the inner surface of the wall of the separation container 2 surrounding the swirl flow region S. This is a band-like region. In this embodiment, the region along the inner surface of the upper wall 2a shown in FIG. 1B is the peripheral region Sa, and the supply unit 3 ejects liquid in the horizontal direction along the peripheral region Sa. .

  A discharge chamber 6 is provided outside the separation container 2. The discharge chamber 6 is formed in a rectangular parallelepiped shape having a peripheral wall 6c and a lower wall 6b made of, for example, a metal plate such as a stainless steel plate or a plastic plate, and an upper portion thereof is covered with a detachable lid 6a. A discharge portion 7 is formed on one side of the peripheral wall 6c of the discharge chamber 6, and the discharge portion 7 is connected to, for example, a downstream pipe (not shown) of a drain line of a factory.

  As shown in FIG. 1 (a), the peripheral wall 2c of the separation container 2 is formed in a rectangular shape with a flat cross section, but a wedge wire screen 5 is formed on both of the walls sandwiching the derivative 4 on the long axis side. ing. In other words, the wedge wire screens 5 are respectively formed on the walls in contact with both ends of the swirling flow in the width direction. The wedge wire screen 5 is also suitable for separating fine solids K, for example, solids K having an average particle diameter of about 10 microns to 1 mm. Next, the wedge wire screen 5 will be specifically described.

  2A is a perspective view of the wedge wire screen 5 of FIG. 1 as viewed from the front, and FIG. 2B is a perspective view of the wedge wire screen 5 as viewed from obliquely above. The wedge wire screen 5 is made of a metal such as stainless steel or a hard plastic containing glass fiber or carbon fiber and has high rigidity.

  The wedge wire screen 5 is configured by arranging a plurality of wedge wires 5a having a wedge-shaped cross section in parallel. For example, a minute slit 5b of about 10 μm to 1 mm is formed between the wedge wires 5a. Each wedge wire 5a is fixed to a plurality of support bars 5c by spot welding or the like. Each slit 5b formed in the wedge wire screen 5 prevents, for example, a solid material K of about 10 μm to 1 mm from passing, and allows only a liquid containing the solid material K smaller than the slit width to pass. In the example of FIG. 1, the wedge wire screen 5 is provided so that the axial direction of each wedge wire 5 a coincides with the vertical direction of the separation container 2, as shown in FIG.

  FIG. 3 is a partially enlarged sectional view of the wedge wire 5a and the slit 5b constituting the wedge wire screen 5 shown in FIG. The wedge wires 5a having a wedge-shaped cross section are arranged in parallel with each other at a predetermined interval, and the surface of the head 5d forms the peripheral surface of the swirl flow region. The axis M of the wedge extending in the vertical direction from the surface of the head 5d is inclined with respect to the direction along the peripheral area Sa of the swirling flow area S indicated by the arrow L. The angle α between the direction of the arrow L and the surface of the head 5d is set to 3 to 8 degrees, usually about 5 degrees. However, this inclination angle can also be set to 0 degree.

  The separation device 1 of the present invention separates the solid matter K contained in the liquid. For example, the separation container 2 is connected to a pipe line on the upstream side of the factory waste water, and the liquid ejected from the wedge wire screen 5 is discharged. When discharging directly into the drainage channel, the separation container 2 can be arranged in the space above the drainage channel, and in that case, it is not necessary to provide the discharge chamber 6. Further, when the separation container 2 is connected to the upstream line of the factory waste water and the separation container 2 is directly immersed in the downstream drainage reservoir, it is not necessary to provide the discharge chamber 6. That is, the separation container 2 according to the present invention can be disposed in any of the discharge chamber, the air, and the liquid.

  Next, a method for separating the solid substance K contained in the liquid by the separation apparatus 1 of FIG. 1 will be described. For example, when the separation device 1 is installed in a sewer or factory drain line pressurized by a pump, the supply unit 3 of the separation container 2 is connected to a pipe on the upstream side of the pipe and discharged. The discharge part 7 of the chamber 6 is connected to piping on the downstream side of the pipe line.

For example, when a liquid such as drainage pressurized to several kg / cm ^{2 by a} pump or the like is continuously supplied to the supply unit 3 of the separation container 2, the liquid is supplied from the supply unit 3 in the tangential direction of the swirling flow region S. Ejecting (specifically, ejecting horizontally along the peripheral region Sa on the upper side of the separation container 2). The ejected liquid moves horizontally on the upper side of the swirl region S, is turned downward by the upper derivative 4, is further turned horizontally by the lower derivative 4 a, and the supply unit 3 is placed below the swirl region. It moves horizontally toward the formed peripheral wall 2c, and then rises along the peripheral wall 2c. A liquid swirling flow as indicated by an arrow is generated in the swirling region S by the movement of the liquid.

  A part of the swirling liquid passes through the wedge wire screen 5 and is ejected to the discharge chamber 6 and then discharged from the discharge portion 7 to the downstream side of the pipeline. On the other hand, the solid K is blocked by the wedge wire screen 5 and separated. The separated solid matter K temporarily adheres to the wedge wire screen 5, but is efficiently separated from the wedge wire screen 5 by the swirl flow, and circulates in the swirl flow region S together with the liquid. The solid K having a relatively large specific gravity quickly settles below the separation container 2 and accumulates at the bottom. On the other hand, since the fine solid K tends to be hard to settle, it circulates in the swirl flow region for a considerably long time. However, since the absolute amount of the fine solid K is small, the separation action in the separation container 2 does not greatly hinder. When the accumulation amount of the solid substance K in the separation container 2 reaches an allowable level, the separation operation is stopped and the accumulated solid substance K is taken out.

  When the liquid continuously pressurized from the supply unit 3 as described above is continuously supplied to the swirl flow region S, an amount of liquid corresponding to the supply amount is ejected from the wedge wire screen 5 to the discharge chamber 6, and the liquid Is continuously generated in the swirl flow region S during the continuous supply. When the pressure of the liquid to be supplied is increased, the amount of ejection from the wedge wire screen 5 increases in proportion thereto, so that the amount of liquid supplied also increases and the speed of the swirling flow increases. On the other hand, the amount of solid matter K attached to the wedge wire screen 5 per unit time increases in proportion to the amount of liquid ejected from the wedge wire screen 5, but the solid matter K from the wedge wire screen 5 increases due to the increase in the flow velocity of the swirl flow. Since the ability to peel off increases, the balance between the two will not be lost.

  In the above description, the separation container 2 is arranged so that the supply unit 3 is on the upper side. However, the separation container 2 can be arranged upside down, horizontally, or inclined. . When arranged upside down, the liquid is ejected horizontally from the supply unit 3 to the lower side of the separation container 2, and a swirling flow in the up and down direction opposite to that in FIG. 1 is generated. If it is placed horizontally, a swirling flow in the horizontal direction is generated, and if it is arranged in a tilted manner, depending on the degree of inclination, a swirling flow in a slanting direction between the swirling flow in the vertical direction and the swirling flow in the horizontal direction is generated. To do. However, regardless of which swirling flow form is selected, the solid K is separated efficiently.

  FIGS. 4A and 4B are diagrams schematically showing a second embodiment of the separation apparatus of the present invention, in which FIG. 4A is a cross-sectional view taken along the line CC in FIG. 4B, and FIG. 4B is a cross-sectional view taken along the line DD in FIG. It is. The part of the separation device 1 different from that of the first embodiment is only the internal structure of the separation container 2, and the other parts are configured in the same manner. Therefore, the separation apparatus 1 of the second embodiment schematically shows only the separation container 2, and the same parts are denoted by the same reference numerals, and redundant description is omitted.

  The separation container 2 formed in a rectangular parallelepiped is provided with a plate-like division body 11 that divides the inside into a first chamber 9 and a second chamber 10, and a portion near the peripheral wall 2 c where the supply unit 3 is formed. An opening 12 is formed in the partition 11. A swirl flow region S is provided in the first chamber 9 and a supply part 3 is formed. The peripheral wall 2c side (the right peripheral wall 2c side in FIG. 4B) facing the peripheral wall 2c where the supply part 3 is formed. Is provided with a derivative 4 having an inclined portion inclined from the upper wall 2a to the peripheral wall 2c. On the other hand, a solid K depositing portion 13 is provided using the internal space of the second chamber 10.

  Wedge wire screens 5 are respectively formed on both walls sandwiching the derivative 4, and the wedge wire screens 5 extend from the upper end of the first chamber 9 to the bottom surface of the second chamber 10. The division body 11 is made of, for example, a metal plate such as a stainless plate or a plastic plate, and one end portion thereof is curved upward in an arc shape as shown in the figure, and this portion constitutes a derivative 4a having an arc portion. .

Next, a method for separating the solid substance K contained in the liquid by the separation apparatus 1 of the second embodiment will be described. Similarly to the first embodiment, when a liquid such as waste water pressurized to about several kg / cm ^{2 by a} pump or the like is continuously supplied to the supply unit 3 of the separation container 2, the liquid is supplied from the supply unit 3. Spouting horizontally (spouting in the tangential direction) along the peripheral region Sa above the swirling flow region S. The ejected liquid moves horizontally on the upper side of the swivel region S, is turned downward by the upper derivative 4, is further turned horizontally by the lower derivative 4 a, and the supply unit 3 forms the lower side of the swirl region. It moves horizontally toward the peripheral wall 2c, and then ascends along the peripheral wall 2c as indicated by an arrow. A liquid swirling flow as indicated by an arrow is generated in the swirling region S by the movement of the liquid.

  Part of the swirling liquid passes through the wedge wire screen 5 and the solid K is blocked by the wedge wire screen 5 and separated. The separated solid K is temporarily attached to the wedge wire clean 5, but is separated from the wedge wire screen 5 by the swirling flow, and circulates in the swirling flow region S together with the liquid. The circulating solid substance K falls or moves to the second chamber 10 together with a part of the liquid from the opening 12 provided in the section 11 as indicated by an arrow. Therefore, the circulation amount (retention amount) of the solid substance K in the first chamber 9 having the main separation function is smaller than that in the first embodiment, and the continuous operation period of the separation device 1 can be lengthened accordingly.

  Since the wedge wire screen 5 is also formed in the second chamber 10, as described above, a part of the liquid in the first chamber 9 flows from the opening 12, and from the wedge wire screen 5 in the second chamber 10 to the outside. Erupts. At that time, a swirling flow is formed in the second chamber 10 by the flow of liquid from the opening 12 to the wedge wire screen 5, and the solid matter K moved to the second chamber 10 by the action of the swirling flow is accumulated in the depositing portion 13. Concentrate on the central area of the deposit.

  5A and 5B are diagrams schematically showing a third embodiment of the separation apparatus of the present invention, in which FIG. 5A is a cross-sectional view taken along line EE in FIG. 5B, and FIG. 5B is a cross-sectional view taken along line FF in FIG. It is. The separation device 1 is different from the second embodiment shown in FIG. 4 only in the portion of the wedge wire screen 5 formed in the separation container 2, and the other portions are configured in the same manner. Accordingly, the same parts as those in the second embodiment are denoted by the same reference numerals, and redundant description is omitted.

  The separation container 2 formed in a rectangular parallelepiped is provided with a plate-shaped division body 11 that divides the inside into a first chamber 9 and a second chamber 10, and an opening 12 is formed in the division body 11. A swirl flow region S is provided in the first chamber 9 and a supply part 3 is formed. The peripheral wall 2c side (the right peripheral wall 2c side in FIG. 4B) facing the peripheral wall 2c where the supply part 3 is formed. Is provided with a derivative 4 having an inclined portion inclined from the upper wall 2a to the peripheral wall 2c. On the other hand, a solid K depositing portion 13 is provided using the internal space of the second chamber 10.

  A wedge wire screen 5 is formed only on one of the peripheral walls 2 c sandwiching the derivative 4, and the wedge wire screen 5 extends from the upper end of the first chamber 9 to the bottom surface of the second chamber 10. Even in such a formation form of the wedge wire screen 5, when the pressurized liquid is continuously supplied to the supply unit 3, the liquid is horizontally supplied from the supply unit 3 along the end surface Sa above the swirl flow region S. To erupt. The ejected liquid moves horizontally in the upper part of the swirl region S, is turned downward by the upper derivative 4, is further turned horizontally by the lower derivative 4 a, and the supply unit 3 is formed at the lower part of the swirl region. It moves horizontally toward the peripheral wall 2c and then ascends along the peripheral wall 2c as indicated by an arrow. A liquid swirling flow as indicated by an arrow is generated in the swirling region S by the movement of the liquid. A part of the liquid is ejected from the wedge wire screen 5 to separate the solid matter K.

  In both the second embodiment and the third embodiment, the lower end of the wedge wire screen 5 is extended to the bottom of the second chamber 10. When the lower edge portion of the wedge wire screen 5 is extended to the second chamber 10 below the section 11, the liquid is ejected from the wedge wire screen 5 portion of the second chamber 10 as described above. Is generated from the opening 12 toward the second chamber 10, and this suction force increases in proportion to the outflow amount of the wedge wire screen 5 in the second chamber 10. For this reason, when the lower edge of the wedge wire screen 5 is extended to the bottom of the second chamber 10, the falling rate of the solid matter K circulating in the first chamber 9 on the swirl flow into the second chamber 10 side becomes the largest. .

  However, the selection of the position of the lower end of the wedge wire screen 5 is not limited to this, and it can be extended to the intermediate height of the second chamber 10 or the bottom of the first chamber 9 (the position of the section 11). When the lower edge portion of the wedge wire screen 5 is extended to the intermediate height of the second chamber 10, the amount of liquid ejected from the wedge wire screen 5 portion of the second chamber 10 is smaller than that when the wedge wire screen 5 is extended to the bottom portion. The force of the solid material K that has fallen from the first chamber 9 to the lower second chamber 10 naturally swirls in the second chamber 10 is also weakened, and the solid material K is efficiently deposited on the accumulation portion 13. Therefore, it becomes easy to collect the solid matter K from the accumulation part 13 outside.

  On the other hand, when the lower edge portion of the wedge wire screen 5 is not extended to the first chamber 10 and is kept to the bottom of the first chamber 9, liquid flow from the first chamber 9 to the second chamber 10 does not occur. For this reason, the falling rate of the solid matter K from the first chamber 9 through the opening 12 to the second chamber 10 is also reduced, but the solid matter K accumulates more stably in the accumulation portion 13 of the second chamber 10. It becomes even easier to collect the solid K from the part 13 to the outside.

  6A and 6B are diagrams schematically showing a fourth embodiment of the separation apparatus of the present invention, in which FIG. 6A is a sectional view taken along line GG in FIG. 6B, FIG. 6B is a sectional view taken along line H-H in FIG. (C) is a left side view of (b), and (d) is a right side view of (b). In the separation device of the fourth embodiment, the separation container 2 used in the first embodiment is of a cartridge type, and the other configuration is the same. Therefore, the same parts as those in the first embodiment are denoted by the same reference numerals, and redundant description is omitted.

  The separation container 2 is a cartridge type formed in an elongated rectangular shape, and the supply unit 3 is configured to be attachable / detachable or connectable to a pipe or a wall. Although FIG. 6 schematically shows the supply unit 3, for example, when connecting to a pipe, the tip of the tubular supply unit 3 is connected to a screw part or a flange part so that screw connection to the pipe or flange connection is possible. Formed on the mounting portion 3a. In addition, in order to attach to the through hole provided in the wall, a mounting portion 3a is formed by providing a flange portion or the like in a portion penetrating the wall of the tubular supply portion 3.

  The basic structure of the separation container 2 is configured in substantially the same manner as the separation container 2 shown in FIG. 1, except that the attachment part 3 a is formed on the supply part 3 described above, and the supply part 3 is formed. The first derivative 4 provided on the side of the peripheral wall 2c facing the peripheral wall 2c and the second derivative 4a are formed of a single arc-shaped plate, and below the peripheral wall 2c on which the supply unit 3 is formed. A third derivative 4b having an arcuate portion is formed on the upper wall 2a, and an outlet 2d for taking out the solid material K is provided at the end of the upper wall 2a. It is 4 points of being attached to. Thus, by adding the 3rd derivative | guide_body 4b to the separation container 2, generation | occurrence | production of a swirl flow is performed more reliably and easily. Note that the third derivative 4b can also be added to the separation container 2 of FIG.

  FIG. 7 is a modification of FIG. The difference between the separation container 2 and the example of FIG. 6 is that the interval between the peripheral wall 2c on which the supply unit 3 is formed and the peripheral wall 2c facing it is small, and the whole is substantially circular. Composed. Therefore, the example of FIG. 7 shows only the HH cross-sectional view of FIG. 6, and other drawings are omitted, and redundant description is also omitted.

  FIGS. 8A and 8B are diagrams schematically showing a fifth embodiment of the separation apparatus of the present invention, in which FIG. 8A is a plan view showing a state in which the top cover of the discharge chamber 6 is taken, and FIG. 8B is a FF of FIG. It is sectional drawing. A separation apparatus 1 according to the fifth embodiment has a plurality of cartridge-type separation containers 2 shown in FIG. 6 arranged in a common discharge chamber 6.

  A distribution pipe 14 is attached to the discharge chamber 6. The distribution pipe 14 includes a T-shaped main pipe 14a connected to the peripheral wall 6c of the discharge chamber 6, a plurality of branch pipes 14 (four in the example shown in FIG. 8) branched in parallel from the main pipe 14a, and each branch pipe. A plurality of (four in the example shown in FIG. 8) attached portions 14c formed at predetermined intervals along 14b. An inner screw is formed on the attached portion 14c.

  External screws are formed on the mounting portions 3a of the plurality (16 in the example shown in FIG. 8) of the separation containers 2, and these mounting portions 3a are screw-connected to the mounted portions 14c. In addition, in the example of FIG. 8, although the attachment part 3a of the separation container 3 is arrange | positioned so that it may be located below, it can also arrange | position so that it may become an upper side or a side.

  For example, a pipe on the upstream side of a drainage pipe pressurized by a pump is connected to the main pipe 14 a, and a pipe on the downstream side of the drainage pipe is connected to the discharge part 7 of the discharge chamber 6. When the pressurized liquid is supplied to the main pipe 14a, the liquid is distributed from the main pipe 14a to each branch pipe 14b and supplied to the supply unit 3 of each separation container 2. The liquid is ejected from the wedge wire screen 5 of each separation container 2 to the discharge chamber 6, and the liquid in the discharge chamber 6 is discharged from the discharge portion 7 to the downstream pipe line.

  When the solid matter K accumulated in the separation container 2 reaches an allowable amount, the separation operation is interrupted, the separation container 2 is removed from the branch pipe 14b, the solid substance K is taken out to the outside, and then again returned to the branch pipe 14b. Install. The number of separation containers 2 attached can be arbitrarily selected according to the desired processing volume of the liquid, and the branch pipe 14b portion to which the separation container 2 is not attached can be closed by, for example, connecting a closure plug with a screw.

  FIG. 9 is a view schematically showing a sixth embodiment of the separation apparatus of the present invention according to FIG. 8, wherein (a) is a plan view of the state in which the upper cover of the discharge chamber 6 is taken, and (b) is ( It is GG sectional drawing of a). The separation apparatus 1 of the sixth embodiment is also configured by arranging a plurality of cartridge-type separation containers 2 shown in FIG. 6 inside the common discharge chamber 6, but the separation container 2 is larger than the fifth embodiment shown in FIG. Things are used.

  A distribution pipe 14 is attached to the discharge chamber 6, and a distribution pipe 14 includes a T-shaped main pipe 14 a connected to the peripheral wall 6 c of the discharge chamber 6 and a plurality of pipes branched in parallel from the main pipe 14 a (in the example shown in FIG. 9). 4) short branch pipes 14 and one attached portion 14c formed on each branch pipe 14b. An inner screw is formed on the attached portion 14c.

  External screws are formed on the attachment portions 3a of a plurality (four in the example shown in FIG. 9) of the separation containers 2, and these attachment portions 3a are screw-connected to the attached portions 14c. Although the example of FIG. 9 is also arranged so that the attachment part 3a of the separation container 3 is located on the lower side, it can also be arranged on the upper side or the side. In addition, since the effect | action of the separation apparatus 1 of 6th Example is the same as that of the separation apparatus 1 of 5th Example, the description is abbreviate | omitted.

  FIG. 10 is a diagram schematically showing a seventh embodiment of the separation apparatus of the present invention. Although only the separation container 2 constituting the separation device 1 is shown in FIG. 10, the discharge chamber 6 can be provided outside the separation container in accordance with the example of FIG.

  In the seventh embodiment, the wedge wire screen 5 is formed only on the upper wall 2a of the separation container 2, and the solid container K is separated by arranging the separation container 2 so that the wedge wire screen 5 is on the upper side. ing. The separation container 2 is not provided with the derivatives 4, 4a, etc., but can be provided if necessary.

  When the pressurized liquid is supplied from the supply unit 3, the liquid is ejected horizontally in the tangential direction of the swirl region S as in the example of FIG. 1, and a swirl flow in the horizontal direction is formed in the swirl region S. Part of the liquid passes through the wedge wire screen 5 and is ejected to the outside of the separation container 2, and the solid matter K is blocked by the wedge wire screen 5 and separated. The solid matter K adhering to the wedge wire screen 5 is peeled off by the swirl flow and circulates in the swirl flow region S on the swirl flow, but gradually settles downward due to the difference in specific gravity and accumulates at the bottom. At that time, the solid matter K is accumulated in a state of being collected in the center by the horizontal swirling flow. When the wedge wire screen 5 is formed only on the upper part of the separation container 2 in this way, the solid matter K is difficult to adhere to the wedge wire screen 5, and even when the solid matter K adheres, the solid matter K is easily peeled off. Become.

  FIG. 11 is a view schematically showing an eighth embodiment of the separation apparatus of the present invention according to FIG. Although only the separation container 2 constituting the separation device 1 is shown in FIG. 11, the discharge chamber 6 can be provided outside the separation container in accordance with the example of FIG.

  In the eighth embodiment, similarly to the seventh embodiment, the wedge wire screen 5 is formed only on the upper wall 2a of the separation container 2, and the separation container 2 is arranged so that the wedge wire screen 5 is on the upper side. K is separated. Furthermore, the separation container 2 is divided into a first chamber 9 on the left side and a second chamber 10 on the right side by a plate-shaped partitioning body 11, and an opening 12 is formed in the lower part of the partitioning body 11. Is provided with a depositing portion 13 of solid matter K. The wedge wire screen 5 is formed from the upper side of the first chamber 9 to the right end of the second chamber 10, but the wedge wire screen 5 is formed only in the first chamber 9 or in the second chamber as in the example of FIG. It may be up to 10 in the middle.

  The generation of the swirling flow and the separation action of the solid K in the first chamber 9 are the same as in the seventh embodiment. The solid substance K circulating on the swirling flow in the first chamber 9 moves from the opening 13 to the second chamber 10 together with a part of the liquid, and accumulates in the accumulation portion 13.

  FIG. 12 is a view schematically showing a ninth embodiment of the separation apparatus of the present invention. In FIG. 12, only the separation container 2 constituting the separation apparatus 1 is shown, but the discharge chamber 6 may be provided outside the separation container in accordance with the example of FIG.

  In the ninth embodiment, the wedge wire screen 5 is formed only on the upper wall 2a of the separation container 2, and the solid container K is separated by arranging the separation container 2 so that the wedge wire screen 5 is on the upper side. ing. However, the separation container 8 is not arranged horizontally, but is inclined as shown in the figure. Further, the peripheral wall 2c positioned at the lower end of the inclined separation container 2 is provided with a discharge portion 2d that can be opened and closed. The generation of the swirling flow in the swirling flow region S and the separation action of the solid K are substantially the same as in the seventh embodiment, but the swirling direction of the swirling flow is inclined according to the inclination of the separation container 2.

  Next, a procedure for separating the solid K using the separation container 2 of the ninth embodiment will be described with reference to FIGS. First, as shown to (a), supply of the pressurized liquid from the supply part 3 is started. Next, as shown in (b), when the inside of the separation container 2 is filled with liquid, a swirl flow in an inclined direction is generated in the swirl flow region S, and a part of the liquid is ejected to the outside through the wedge wire screen 5. The solid K is blocked by the screen 5 and separated. The solid matter K adhering to the wedge wire screen 5 is peeled off by the swirling flow and circulates on the swirling flow.

  The circulating solid K settles in order from a relatively large specific gravity and accumulates in the vicinity of the opening 2d obliquely downward as shown in FIG. When the deposition amount of the solid substance K reaches an allowable level, the liquid supply is stopped and the separation operation is interrupted as shown in (d). Next, as shown in (e), the opening 2d is opened, and as shown in (f), for example, while washing water is sprayed from the outside of the wedge wire screen 5, the deposited solid matter K is discharged to the outside. . Next, as shown in (g), the opening 2d is closed and the solid K separation operation is restarted.

  The liquid to which the present invention can be applied may include, for example, rainwater flowing into the sewer from houses, roads, and fields, general wastewater, factory wastewater, kitchen wastewater from restaurants, wastewater from meat processing plants, and industrial water. It is also applicable when reusing these wastewaters. Therefore, the present invention can be preferably used for solid K separation in many industries.

It is a figure which shows 1st Example of a separation apparatus, (a) is AA sectional drawing of (b), (b) is BB sectional drawing of (a). (A) is the perspective view which looked at the wedge wire screen of FIG. 1 from the front, (b) is the perspective view which looked at it from diagonally upward. It is the elements on larger scale of the wedge wire and slit which comprise the wedge wire screen shown in FIG. It is a figure which shows typically 2nd Example of a separator, (a) is CC sectional drawing of (b), (b) is DD sectional drawing of (a). It is a figure which shows typically 3rd Example of a separator, (a) is EE sectional drawing of (b), (b) is FF sectional drawing of (a). It is a figure which shows typically 4th Example of a separator, (a) is GG sectional drawing of (b), (b) is HH sectional drawing of (a), (c) is (b) ) Is a left side view, and (d) is a right side view of (b). It is a modification of 4th Example of a separator. It is a figure which shows typically 5th Example of a separator, (a) is a top view of the state which took the upper cover of the discharge chamber 6, (b) is FF sectional drawing of (a). It is the figure which showed typically 6th Example of the separator according to FIG. 8, (a) is a top view in the state which took the upper cover of the discharge chamber 6, (b) is GG of (a). It is sectional drawing. It is a figure which shows typically 7th Example of a separator. It is a figure which shows typically 8th Example of a separation device according to FIG. It is a figure which shows typically 9th Example of a separator.

Explanation of symbols

S Swirl area Sa Peripheral area K Solid 1 Separation device 2 Separation container 2a Upper wall 2b Lower wall 2c Peripheral wall 3 Supply part 3a Mounting part 4, 4a, 4b Derivative 5 Screen, wedge wire screen 5a Wedge wire 5b Slit 5c Support Rod 5d Head 6 Discharge chamber 6a Lid 6b Peripheral wall 6c Peripheral wall 7 Discharge portion 9 First chamber 10 Second chamber 11 Partition 12 Opening portion 13 Accumulating portion 14 Distribution pipe 14a Main tube 14b Branch tube 14c Mounted portion

Claims (9)

  An apparatus for separating solids contained in a liquid, comprising: a closed-type separation container provided with a swirl flow region therein; and a wedge wire for separating a liquid supply unit and solids on a wall constituting the separation container A screen is formed, and the supply unit is configured to eject a pressurized liquid in a tangential direction of the swirl flow region to generate a swirl flow of the liquid in the swirl flow region, and the wedge wire screen The separation device is formed on the wall in contact with the flow region.   2. The separator according to claim 1, wherein the separation container is formed in a rectangular parallelepiped, a supply part is formed on one side of the wall of the rectangular parallelepiped, and a derivative having an inclined part or an arc part is provided on a wall side facing the wall on which the supply part is formed. The supply unit is configured to generate a swirl flow by changing the direction of the liquid at an inclined part or an arc part of the derivative by ejecting liquid pressurized in the direction of the derivative. The separation apparatus is formed on one or both of the walls sandwiching the derivative.   3. The separation container according to claim 2, wherein the separation container is provided with a partition that divides the inside thereof into a first chamber and a second chamber, an opening is formed in the partition, and the swirl flow region is provided in the first chamber. A supply portion is formed, and the wedge wire screen is formed in the first chamber or in at least a part of the first chamber and the second chamber, and the second chamber accumulates solids flowing from the opening. Separation device characterized in that a part is provided.   4. The discharge chamber according to claim 1, wherein a discharge chamber is provided outside the separation container, and the liquid in the separation container passes through the screen and is ejected to the discharge chamber. Separation device.   4. The discharge chamber according to claim 1, wherein a plurality of the separation containers are provided, a distribution pipe is provided to distribute and supply the liquid to the supply unit of each separation container, and a common discharge chamber is provided outside each separation container. Is provided, and the liquid in each separation container passes through the wedge wire screen and is ejected to the discharge chamber.   In the method of separating the solid contained in the liquid, the liquid pressurized from the supply unit is tangentially moved in the swirl flow region using the separation device according to any one of claims 1 to 5. A separation method, wherein a swirl flow of liquid is generated in a swirl flow region by jetting, and the liquid from which solids are separated by the wedge wire screen is spouted to the outside of the separation container.   7. The separation method according to claim 6, wherein the separation container is arranged so that the pressurized liquid ejected from the supply unit generates a swirling flow in the vertical direction or the horizontal direction in the swirling flow region.   In Claim 6, arrange | positioning the said separation container so that the pressurized liquid ejected from the said supply part may generate | occur | produce a horizontal swirl flow in the said swirl flow area | region, and the said swirl | vortex flow of the said production | generation is produced | generated as the said separation container. A separation method characterized in that a wedge wire screen is formed only on the upper side.   In Claim 6, arrange | positioning the said separation container so that the pressurized liquid ejected from the said supply part may produce | generate the swirl flow of the inclination direction which exists between an up-down direction and a horizontal direction in the said swirl flow area, Separation container is used in which the wedge wire screen is formed only on the upper side of the generated swirl flow and the solid material discharge part is formed on the wall constituting the lower end portion in the inclined direction. A separation method comprising discharging solid matter accumulated in a container from a discharge part.

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