JP5094022B2 - Aeration device and membrane filtration unit applied when collecting filtrate of solid-liquid mixed processing liquid - Google Patents

Description

The present invention is generally of the waste water treatment and water purification, to an air diffuser and the membrane filtration unit of the membrane filtration unit is immersed disposed in the processing liquid in the aeration tank to be applied to such membrane separation activated sludge process.

  A membrane separation activated sludge treatment method, which is a typical example to which the apparatus of the present invention is applied, biologically treats organic matter contained in industrial wastewater and domestic wastewater, or wastewater containing microorganisms and bacteria, for example. Thus, solid-liquid separation is performed using various types of separation membranes, and the treated water is recovered or discharged into the treated water tank. Normal membrane separation activated sludge treatment equipment is equipped with a raw water adjustment tank, a denitrification tank, and an aeration tank. In the raw water adjustment tank, the liquid level in the tank is measured by a liquid level gauge, and the liquid feed pump is driven intermittently. Thus, the liquid level in the tank is adjusted to be within a predetermined range. After the raw water sent by the liquid feed pump is introduced into the denitrification tank, the raw water overflowing from the denitrification tank is caused to flow into the adjacent aeration tank. A membrane filtration unit is immersed in this aeration tank. This membrane filtration unit separates the membrane into activated sludge contaminants and treated water, and the filtered treated water is sucked by a suction pump and collected or discharged into a treated water tank. Most of the excess sludge in the aeration tank is sent to the sludge storage tank where it is stored, dried and then incinerated. A part of the excess sludge is returned to the denitrification tank by a liquid feed pump and circulates between the denitrification tank and the aeration tank.

  A typical example of the membrane filtration unit is a hollow fiber membrane module obtained by arranging a plurality of sheet-like hollow fiber membrane elements in which a large number of porous hollow fibers are arranged in parallel on the same plane at a predetermined interval. And an air diffuser disposed below the hollow fiber membrane module. As for the said hollow fiber membrane module, the whole shape which consists of a plurality of hollow fiber membrane element has comprised the substantially rectangular parallelepiped. One air diffuser has a plurality of air diffuser pipes provided with holes and slits in a pipe made of metal, resin, etc., in parallel, and one end of each air diffuser pipe is connected to the air supply pipe of the aeration blower. ing. Air sent from the aeration blower is discharged into the sludge through the air diffuser.

  The air discharged from the air diffuser rises as bubbles and is mixed with surrounding sludge to form a gas-liquid mixed flow, which swings the hollow fiber membrane element of the upper hollow fiber membrane module. By this swinging, the attached sludge adhering to the membrane surface of the hollow fiber membrane element is peeled off from the membrane surface, and so-called air scrubbing cleaning is performed to suppress clogging of the membrane surface. When treating domestic wastewater, industrial wastewater, etc., the organic matter is adsorbed to the aerobic microorganisms by bringing the air generated from the diffuser into contact with the organic matter in the sludge of the aeration tank in the presence of aerobic microorganisms. Metabolized and biologically treated with sludge.

  The hollow fiber membrane module and the air diffuser are surrounded by a rectangular cylindrical blocking plate that is open at the top and bottom. This shielding plate becomes a wall part for generating a gas-liquid mixed flow by the rising of the bubbles generated from the air diffuser and guiding the flow from the upward flow to the downward flow. The gas-liquid mixed flow generated by the bubbles discharged from the diffuser does not scatter in an oblique direction, but rises straight and efficiently contacts the hollow fiber membrane module. At this time, due to the uniform dispersion of the gas-liquid mixed flow with respect to the membrane surface of the hollow fiber membrane module, the hollow fiber membrane is swung as described above to uniformly wash each hollow fiber membrane element. After that, the gas-liquid mixed flow flows over the upper end of the shielding plate to the periphery and descends to form a swirling flow in the vertical direction as a whole. The activated sludge is agitated by this swirling flow, and the biological treatment is made uniform.

  In addition to the sheet-like hollow fiber membrane element having a porous hollow fiber as a constituent member, a membrane separation module is used which includes a filtration membrane having a plurality of fine pores. For example, a flat membrane type There are various known separation membranes such as a tubular membrane type and a bag-like membrane type. Examples of the material include cellulose, polyolefin, polysulfone, PVDF (polyvinylidene fluoride), PTFE (polytetrafluoroethylene), and ceramics. Thus, hollow fiber membrane modules using hollow fiber membrane elements are widely used because of a large filtration area.

  The average pore diameter of the micropores formed in the porous hollow fiber is generally an average pore diameter of 0.001 to 0.1 μm for a membrane called an ultrafiltration membrane, and an average pore size of 0.1 to 1 μm for a membrane generally called a microfiltration membrane. It is. For example, when used for solid-liquid separation of activated sludge, the pore diameter is preferably 0.5 μm or less, and when sterilization is required as in the case of filtration of purified water, the pore diameter is preferably 0.1 μm or less.

  Incidentally, a plurality of air diffusion holes whose openings are directed vertically downward are formed in the air diffusion pipe made of a metal pipe or a synthetic resin pipe of the above air diffusion device. Therefore, air is discharged from the air diffuser through the air diffusers vertically downward into the sludge and rises as bubbles, but there is a lot of excess sludge below the air diffuser, and that sludge enters the air diffuser. Therefore, the adhering matter may eventually block the opening of the diffusing tube, making it impossible to diffuse. In order to prevent this, conventionally, the air diffuser is cleaned.

  For the cleaning, for example, the operation of the suction pump and the aeration blower is stopped, the aeration device is pulled up from the inside of the tank and the aeration tube is cleaned, or the attached sludge is sucked out by a spirometer provided in the aeration blower. Or by sending liquid into the diffusing tube and removing clogged sludge by liquid pressure. However, temporarily stopping the wastewater treatment even if temporarily avoids it as much as possible because the daily treatment amount is determined in a state where there is no room, and the treatment efficiency is greatly reduced. Should.

  The present invention has been made to solve these problems, and a specific purpose thereof is filtration of a solid-liquid mixed treatment liquid capable of cleaning an air diffuser at an arbitrary time without stopping the treatment of waste water. An object of the present invention is to provide a method for cleaning an air diffuser during liquid recovery.

Such a problem is a diffuser of a membrane filtration unit that is immersed in a treatment tank, which is a basic configuration of the present invention, and has at least one end connected to a blower via an air main pipe . A gas supply pipe, a liquid supply pipe having one end connected to the pump and the other end joined in the middle of the air main pipe, a branch pipe connected to the other end of the gas supply pipe, and orthogonal to the branch pipe And a plurality of diffuser tubes having a plurality of diffuser holes that are horizontally disposed and open substantially vertically downward, wherein the diffuser tube is a value obtained by multiplying the sectional opening area of the diffuser tube by the number of the diffuser tubes. Is set to a value smaller than the value obtained by multiplying the sectional opening area of the branch pipe by the number of the branch pipes, the gas flow rate in the branch pipe is 5 m / sec or less, and the supply amount of the liquid is 0. .03L / min / mm ² or more on the set effect with a diffuser comprising Resolve to.

According to a preferred aspect of the present invention, in addition to the above-described configuration, the total opening area of the air diffusion holes of one air diffusion pipe is set to be smaller than the cross-sectional opening area of the air diffusion pipe. Yes.
Further, in the present invention, as a second basic configuration, the membrane separation module is a hollow in which a plurality of sheet-like hollow fiber membrane elements in which a large number of porous hollow fibers are arranged in parallel on the same plane are arranged. The membrane filtration unit includes a hollow fiber membrane module and the air diffuser disposed below the hollow fiber membrane module.

Effect

As can be understood from the above configuration, the basic idea of the air diffuser according to the present invention is to mix the liquid into the gas sent from the aeration blower to the air diffuser, and send the gas-liquid mixed flow to the air diffuser. By dissolving and blowing off the fluid pressure of the gas-liquid mixed flow and the attached sludge, the air holes closed by the attached sludge are opened. The supply of the liquid to the gas at this time can be continuously performed while the waste water is being processed, but an electromagnetic open / close valve is attached to the liquid supply pipe , and the liquid is supplied in advance based on a signal from the control unit. You may make it supply a liquid for every period.

  For example, in the membrane separation activated sludge treatment, the filtration operation is intermittently performed to wash the membrane module of the membrane filtration unit. Specifically, for example, after 6 minutes of filtration operation, the filtration operation is stopped for 1 minute, and this is repeated. If the method for cleaning an air diffuser of the present invention is performed when the filtration operation is stopped, the cleaning operation can be performed while continuously performing the waste water treatment.

Here, when air is fed from the aeration blower to the air diffuser via the gas supply pipe and the liquid (water or treated water) is joined to the air via the gas supply pipe, the liquid is mixed with the air. The gas becomes large bubbles and flows through the diffuser. Here, a part of the air in the gas-liquid mixed flow rises in the liquid in the diffuser pipe, collects in the upper inner wall part in the diffuser pipe, and presses the liquid against the lower inner wall part by the internal pressure, so that a lot of liquid Comes in contact with the attached sludge. At this time, bubbles in the liquid are simultaneously dispersed to promote the dissolution of the attached sludge. When the flow velocity of the gas flowing in the gas distribution pipe exceeds 5 m / sec, the liquid on the downstream side of the horizontally arranged gas distribution pipe is pushed by the gas, and the amount of liquid increases from the upstream side. The air diffuser is usually attached to the gas distribution pipe horizontally in a ladder shape. As described above, when the gas flow rate exceeds 5 m / sec, the amount of liquid in the pipe increases on the downstream side of the gas supply pipe , so that the cleaning with the gas-liquid mixture in the diffuser pipe arranged on the downstream side is performed on the upstream side. It exceeds the cleaning with the gas-liquid mixture in the diffuser tube , and cleaning unevenness occurs in the length direction of the gas supply tube , and uniform cleaning cannot be performed. On the other hand, if the amount of liquid supplied is less than 0.03 L / min / mm ² , the attached sludge does not dissolve and the cleaning effect is greatly reduced.

  Furthermore, by setting the sum total of the opening area of the air diffusion holes of one air diffusion pipe to be smaller than the cross-sectional opening area of the air diffusion pipe, the fluid pressure in the air diffusion pipe can easily crush the attached sludge. At this time, if the value obtained by multiplying the cross-sectional opening area of the air diffusion pipe by the number of the air diffusion pipes is set smaller than the value obtained by multiplying the cross-sectional opening area of the gas distribution pipe by the number of the gas distribution pipes, the same For this reason, it is easy to obtain the fluid pressure necessary for crushing the attached sludge in the air diffuser.

Hereinafter, preferred embodiments of the present invention will be specifically described with reference to the drawings.
FIG. 1 shows a schematic configuration of an aeration process in a membrane-separated activated sludge treatment apparatus suitable for carrying out a method of cleaning an aeration apparatus when collecting a filtrate of a solid-liquid mixed treatment liquid according to the present invention.

  According to the membrane separation activated sludge treatment apparatus, the raw water introduced into the raw water adjustment tank (not shown) is intermittently transferred to the denitrification tank (not shown) by a liquid feed pump (not shown) so as to maintain a predetermined liquid level range. Then, the raw water overflowing from the denitrification tank is introduced into the adjacent aeration tank 4. A large number of membrane filtration units 5 are immersed in the sludge of the aeration tank 4. The treated water membrane-separated into activated sludge and treated water by the membrane filtration unit 5 is sent to the treated water tank by suction by the suction pump Pv and collected or discharged as it is. On the other hand, a part of the concentrated sludge composed of microorganisms which have been aerated in the aeration tank 4 and proliferated is stored in a sludge storage tank (not shown). A part of the concentrated sludge inside the aeration tank 4 is returned to the denitrification tank by a liquid feed pump (not shown) and circulates between the denitrification tank and the aeration tank.

  FIG. 2 shows a typical example of a normal membrane filtration unit 5. As shown in the figure, the membrane filtration unit 5 includes a hollow fiber membrane module 9 in which a plurality of hollow fiber membrane elements 10 arranged in a direction perpendicular to the yarn length are supported and fixed in parallel, and the hollow fiber membrane module 9 And an air diffuser 15 disposed at a predetermined interval below the air gap. The hollow fiber membrane element 10 communicates and supports the upper end opening end of a membrane sheet 11 in which a large number of porous hollow fibers 10a are arranged in parallel to the filtered water discharge pipe 12 via a potting material 11a, and the lower end thereof. It is closed and fixed and supported by the lower frame 13 via the potting material 11a, and both ends of the filtered water outlet pipe 12 and the lower frame 13 are supported by a pair of vertical rods 14. A large number of hollow fiber membrane elements 10 are accommodated and supported in parallel in substantially the entire volume of a rectangular cylindrical upper wall member 20 whose upper and lower end surfaces are open with the sheet surface vertical. Here, in the hollow fiber membrane element 10, generally, as shown in FIG. 3, a large number of porous hollow fibers 10a are arranged in parallel on the same plane with the same gap.

In this embodiment, the porous hollow fiber 10a is made of PVDF (polyvinylidene fluoride) hollow hollow fiber that is hollow in the longitudinal direction along the center, and the pore diameter of the filtration hole is 0.4 μm. The effective membrane area per sheet is 25 m ² . The sheet-like hollow fiber membrane element 10 is used in 20 pieces per membrane filtration unit 5 and has a depth of 30 mm, a width of 1250 mm, and a length from the upper surface of the filtrate extraction pipe 12 to the lower surface of the lower frame 13. Is 2000 mm. The size of the single membrane filtration unit 5 including the air diffuser 15 is 1552.5 mm in depth, 1447 mm in width, and 3043.5 mm in height. The filtered water extraction pipe 12 has a length of 1280 mm, its material is ABS resin, and the vertical rod 14 is made of SUS304.

  However, the material such as the porous hollow fiber 10a, the filtrate extraction pipe 12, and the vertical rod 14, the size of the hollow fiber membrane element 10, the size of the membrane filtration unit 5, and the number of the hollow fiber membrane elements 10 per unit Etc. can be variously changed according to the application. For example, in terms of the number of the hollow fiber membrane elements 10, it can be arbitrarily set to 20, 40, 60,... According to the processing amount, or the material of the porous hollow fiber 10a can be cellulose, polyolefin, Conventionally known ones such as polysulfone, polyvinyl alcohol, polymethyl methacrylate, and polyfluorinated ethylene can be applied.

  At one end of the filtrate extraction pipe 12 of each hollow fiber membrane element 10, an outlet 12a for high-quality filtered water (treated water) filtered by each porous hollow fiber 10a is formed. In this embodiment, an L-shaped joint 12b is attached to each outlet 12a in a liquid-tight manner via a sealing material, similarly to the membrane filtration unit 5 shown in FIG. Moreover, as shown in FIG. 3, the water collection header pipe | tube 21 is installed horizontally along the edge by the side in which the said outlet 12a is formed in the upper end of the said upper wall material 20. As shown in FIG. The water collecting header pipe 21 is formed with water collecting ports 21a at positions corresponding to the plurality of outlets 12a, and an L-shaped joint 21b similar to the outlet 12a serves as a sealing material in each water collecting port 21a. It is liquid-tightly attached.

  The treated water outlet 12a of the filtered water outlet 12 and the water outlet 21a of the water header 21 are connected to each other by connecting the L-shaped joints 12b and 21b attached to each other. . At one end of the water collection header pipe 21, a water suction port 21 c connected to the suction pump Pv via the filtered water suction pipe line 22 is formed. As shown in FIG. 1, the water suction port 21 c formed for each water collection header pipe 21 and the filtered water suction pipe 22 are interposed in suction pipes 22 a branched from the filtered water suction pipe 22. The flow rate adjustment valve 23 is connected. Here, the suction pipe line 22a rises from the water collection header pipe 21 to an upper position higher than the liquid level of the aeration tank 4, and is connected to the filtered water suction pipes 22 arranged horizontally. In the present embodiment, the filtered water suction pipe 22 that is arranged horizontally and extends outside the tank is connected to a suction port of a suction pump Pv that is bent downward outside the tank and installed on the ground. . A drain line is connected to the discharge port of the suction pump Pv, and the filtrate is sent to a treatment water tank (not shown) or discharged as it is.

As shown in FIG. 4, the air diffuser 15 includes a rectangular cylindrical body that is coupled to the lower end of the upper wall member 20 and that is open at the top and bottom, and has four support columns 24 a that extend downward from the lower ends of the four corners thereof. Is housed and fixed at the bottom of the lower wall member 24 having As shown in FIG. 1, the air diffuser 15 is connected to an aeration blower B disposed outside via an air main pipe 18. Specifically, it is a branch pipe and is provided with a gas supply pipe 16 . The open end of the gas supply pipe 16 is connected to one end of a branch pipe 25 that extends horizontally in the width direction along the inner wall surface on the front side of the lower wall member 24. Are arranged in a ladder shape with a predetermined interval, one end communicating with the branch pipe 25 and fixed, and the other end fixed horizontally along the inner wall surface of the lower wall member 24 on the back side. A plurality of diffuser tubes 17 are provided.

  In the present embodiment, the end of the diffuser pipe 17 connected to the gas supply pipe 16 communicates with the inside of the gas supply pipe 16, and the other end of the diffuser pipe 17 is closed. The air diffuser 15 according to the present embodiment is arranged corresponding to each of the plurality of membrane filtration units 5, and the air sent from the same aeration blower B is diverted to the respective air diffusers 15. An air main pipe 18 directly connected to B is provided, and the air main pipe 18 is connected to each air diffuser 15 through a gas supply pipe 16 that is a branch pipe.

  A liquid supply pipe 26 joins the air main pipe 18 or the gas supply pipe 16. Liquid is actively supplied to the liquid supply pipe 26 from a liquid (water or treated filtered water) supply source (not shown) by a liquid feed pump (not shown). The liquid supply at this time may be maintained when the suction pump Pv is driven, that is, when the filtration operation is performed, or may be performed when the filtration operation is stopped. May be.

  As described above, the plurality of membrane filtration units 5 immersed in the same aeration tank 4 are connected to the same filtered water suction pipe 22 through each suction pipe line 22 a and the flow rate adjusting valve 23. When the sludge treatment is continuously performed for a long period of time, clogging progresses on the surface of the membrane of the membrane filtration unit 5, so that the filtration flow rate decreases or the transmembrane pressure difference increases. In order to suppress such an increase in transmembrane pressure difference, so-called air scrubbing is performed using a gas-liquid mixed fluid of air and sludge discharged from the air diffuser 15 disposed below the hollow fiber membrane element 10. At the same time, each porous hollow fiber 10a is swung to remove and remove the sludge substance adhering to the membrane surface, thereby performing physical cleaning. At the same time, biological treatment is performed by activating the nitrification reaction by microorganisms.

  Here, the activated sludge in the aeration tank 4 is subjected to solid-liquid separation through the hollow portion of the porous hollow fiber 10a of the membrane filtration unit 5, and the filtered water is actively sucked by an external suction pump Pv, which is not shown in the drawing. Send it to the water tank and collect it. In the present embodiment, the operation at this time is repeated by stopping the suction pump Pv for one minute and then stopping for one minute. That is, the suction operation of filtered water by the suction pump Pv is intermittently performed. The driving of the aeration blower B is maintained even during the filtration operation and at the time of stopping, and air is always sent to the air diffuser 15. Therefore, not only during the filtration operation but also when the filtration operation is temporarily stopped, the hollow fiber membrane of the hollow fiber membrane module 9 is generated by the upward flow of the gas-liquid mixed liquid of bubbles and activated sludge discharged from the air diffuser 15. The sludge adhering to the membrane surface is peeled off from the membrane surface, and so-called air scrubbing cleaning is performed.

  In addition, when the filtration operation is stopped, filtered water suction from the hollow fiber membrane module 9 is not performed, and only air scrubbing is performed. Since the air scrubbing at this time is not filtered and sucked by the porous hollow fiber 10a, the adhesion of sludge is reduced, so the cleaning effect is extremely high compared to the filtration operation, and the transmembrane pressure difference is reduced. Increases recovery speed. In the present embodiment, the filtered water is supplied into the air flowing through the air main pipe 18 or the gas supply pipe 16 via the liquid supply pipe 26 in accordance with the temporary stop of the filtration operation. The gas-liquid mixed flow supplied and mixed with the filtered water reaches the plurality of air diffusers 17 through the branch pipes 25 of the air diffuser 15.

  At this time, a part of the air in the gas-liquid mixed fluid sent to the diffuser tube 17 gathers on the upper surface of the filtered water, that is, the upper inner wall portion of the diffuser tube 17, and gradually increases the internal pressure to transfer the fluid to the lower inner wall of the diffuser tube 17 It comes to press against the part. On the other hand, air in the filtered water becomes bubbles and flows in the filtered water, causing turbulent flow in the filtered water. Due to this turbulent flow effect and the increase in internal pressure, the adhering sludge solidified by closing the air diffuser hole of the air diffuser 17 is dissolved and pushed out from the air diffuser into the activated sludge outside the tube to efficiently remove the adhering sludge. To do.

For the present invention, it is important that the flow rate of filtered water supplied from the fluid supply pipe is 0.03 L / min / mm ² or more. If the amount of filtered water supplied is less than 0.03 L / min / mm ² , the amount of liquid with respect to the air is too small, and the effect of the liquid as described above cannot be expected, and the dissolution of adhering sludge does not progress, and the cleaning effect Is significantly reduced. Further, the flow velocity of the air flowing through the branch conduit 25 needs to be 5 m / sec or less. If it exceeds 5 m / sec, the height of the gas-liquid mixture in the branch line 25 at the inlet side and downstream blockage side of the branch line 25 is not uniform due to the influence of the gas flow velocity, and the downstream blockage side In this case, the height in the pipe is higher than that on the inlet side. As described above, when the pipe height on the downstream blockage side is higher than that on the inlet side, the liquid height of the diffuser pipe 17 disposed on the downstream blockage side is higher than the liquid height of the diffuser pipe 17 disposed on the inlet side. Therefore, there is a difference in the cleaning of the inner wall surface of the air diffuser and the air diffuser holes, and it may become impossible to remove the attached sludge.

  Furthermore, in the present embodiment, the sum of the opening areas of the air diffusion holes of one air diffusion pipe 17 is set to be smaller than the cross-sectional opening area of the air diffusion pipe 17. Further, in the above embodiment, one end of each air diffuser 17 is connected and fixed to one branch conduit 25, but both ends of each air diffuser 17 are connected to two branches 25 and connected. It may be fixed. In any case, the value obtained by multiplying the sectional opening area of the diffuser pipe 17 by the number of the diffuser pipes 17 is smaller than the value obtained by multiplying the sectional opening area of the branch duct 25 by the number of the branch ducts 25. Setting is also important. When the opening area is set in such a relationship, the mixing effect of the liquid and the gas is further increased, and the cleaning effect of the air diffuser 15 can be greatly improved.

  Examples of the present invention will be specifically described below together with comparative examples.

An air diffuser having an inner diameter of 25 mm and a length of 1400 mm was connected and fixed at an equal pitch between two parallel branch pipes having an inner diameter of 100 mm and a length of 1400 mm. The air diffuser was formed with nine diffuser holes with a pitch of 120 mm, with openings having a diameter of 5 mm directed vertically downward. The amount of air flowing through the gas distribution pipe was 200 m ³ / hr, the amount of water was 100 L / min, and the gas-liquid cleaning time of the air diffuser was 1 min at a rate of 6 times / day. After 6 months of this operation, the state of obstruction of the air diffuser was investigated silently. As a result, no obstruction was observed.

Comparative Example 1

  The conditions other than the water supply rate being 10 L / min were all the same as in Example 1. As a result of investigating the common state of the air diffuser after operation for 6 months, blockage was found in 5 places. It was.

Comparative Example 2

Except for the air supply rate of 350 m ³ / hr, all the conditions were the same as in the example, and after checking the closed state of the air diffuser after operation for 6 months, blockage was found in 8 places.

It is explanatory drawing which shows schematic structure of the filtered water collection | recovery apparatus with which the washing | cleaning method of the aeration apparatus which is typical embodiment of this invention is applied. FIG. 3 is a three-dimensional view showing the entire configuration of a normal membrane filtration unit with a part broken away. It is a perspective view which shows typically the structural example of the membrane element which is a structural member of a hollow fiber membrane module. It is a three-dimensional view of the diffuser which is one of the structural members of the membrane filtration unit.

Explanation of symbols

4 Aeration tank 5 Membrane filtration unit 9 Hollow fiber membrane module 10 Hollow fiber membrane element 10a Porous hollow fiber 11 Membrane sheet 11a Potting material 12 Filtrated water discharge pipe 12a Filtered water discharge port 12b L-shaped joint 13 Lower frame 14 Vertical rod 15 Air diffuser 16 Gas supply pipe 17 Air diffuser pipe 18 Air main pipe 20 Upper wall material 21 Water collecting header pipe 21a Water collecting port 21b L-shaped joint 21c Water inlet 22 Suction pipe 22a Suction pipe 23 Flow rate adjusting valve 24 Lower wall material 24a Post 25 Branch pipe 26 Liquid supply pipe Pv Suction pump B Aeration blower

Claims (3)

An air diffuser for a membrane filtration unit immersed in a treatment tank,
At least one gas supply pipe (16) having one end connected to the blower (B) through an air main pipe (18) , one end connected to the pump (P), and the other end to the air main pipe (18) A liquid supply pipe (26) that merges in the middle of the gas supply pipe, a branch pipe (25) connected to the other end of the gas supply pipe (16), and a horizontal pipe that is orthogonal to the branch pipe (25). And a plurality of diffuser tubes (17) having a plurality of diffuser holes that open substantially vertically downward,
The diffuser pipe (17) is a value obtained by multiplying the sectional opening area of the diffuser pipe (17) by the number of the diffuser pipes (17) to the sectional opening area of the branch pipe (25). 25) is set to a value smaller than the value multiplied by the number of
An air diffuser in which a gas flow rate in the branch pipe is set to 5 m / sec or less and a supply amount of the liquid is set to 0.03 L / min / mm ² or more. One of the sum of the opening areas of the diffusing pores of the diffuser tube is an air diffuser of the set formed by claim 1, wherein less than the cross-section opening area of the diffuser tube.

The membrane separation module comprises a hollow fiber membrane module in which a plurality of sheet-like hollow fiber membrane elements in which a large number of porous hollow fibers are arranged in parallel on the same plane, and the hollow fiber membrane module and the hollow fiber membrane A membrane filtration unit comprising: the air diffuser according to claim 1 or 2 disposed below a module.

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