JP6068519B2 - Air diffuser and cleaning method of air diffuser - Google Patents

Description

  The present invention relates to a diffuser tube and a method for cleaning the diffuser tube.

  A membrane body formed of a tube-shaped viscoelastic body and formed with a plurality of air hole slits penetrating between the outer circumferential surface and the inner circumferential surface, and a tubular membrane support body that supports the membrane body from the inside Air diffusers are widely used in sewage treatment equipment.

  Patent Document 1 discloses an air tube body in which a rubber tube having a plurality of cut holes is formed and several holes are formed for the purpose of preventing backflow of sewage and the like into the diffuser tube and clogging of the diffuser hole slit. An air diffusing tube fitted in is disclosed. Several holes are formed in the peripheral surface including the side portion of the air tube main body constituting the air diffuser, and air diffuser slits formed by cut holes are formed in the entire region of the film body.

  In Patent Document 2, one or a plurality of evenly distributed air flow ejection holes are formed only on one end side of a resin-made cylindrical core member, and the cylindrical diffuser member covers the core member. A diffuser is disclosed. The air diffuser is composed of a porous membrane rubber or the like, and the air ejected from the air flow ejection hole formed on one end side of the core member flows through the gap between the core member and the air diffuser, It is comprised so that it may discharge | release from a micropore.

  In Patent Document 3, a plurality of vent holes are formed in a vent pipe attached to the base end side of a tube base material, and air is passed through a slit formed in the peripheral portion of the elastic film covering the tube base material and the vent pipe. Discharged air diffusers are disclosed. Similar to the air diffuser disclosed in Patent Document 2, the air ejected from the vent formed on one end side is released from the slit of the elastic film through the gap between the tube base material and the elastic film.

Japanese Utility Model Publication No. 01-25679 JP 2005-334847 A Japanese Patent No. 4781302

  An air diffuser constructed by fitting a membrane body composed of a tube-shaped viscoelastic body to a tubular membrane support body has no sludge or the like flowing from an air diffuser slit formed in the film body. Although it is considered, in reality, the expansion and contraction are repeated by the air flowing through the gap between the membrane support and the membrane body, and in the process, sludge and the like may flow from some of the diffuser slits. If the elastic force of the air hole slit is reduced due to the change, the inflow amount of sludge and the like may increase and the air hole slit may be blocked.

  Moreover, since the conventional air diffuser described above has air diffused holes formed in portions of the film body that face the through holes formed in the membrane support, most of the air supplied from the through holes is in the vicinity. The problem is that it may be difficult to evenly diffuse along the axial center direction of the diffuser tube by blowing out from the diffuser hole at once, and the elastic force decreases due to the large open diffuser hole near the through hole. There was a problem that sludge may be drawn in when opening.

  When a certain amount of air hole slits are blocked and the air diffusion performance is lowered, a cleaning process is performed in which the cleaning liquid is supplied into the membrane support to clean the air hole slits in order to recover the air diffusion performance. However, if air is supplied with the cleaning liquid remaining in the membrane support after cleaning, the release of air from the through-hole is hindered by the influence of the cleaning liquid remaining on the membrane support, and even if the diffuser slit is cleaned, There was also a problem that early recovery of energy performance was hindered.

  In view of the above-described problems, an object of the present invention is to provide a diffuser that quickly recovers the aeration performance even after supplying the cleaning liquid to the membrane support and cleaning the diffuser, and that can always uniformly diffuse. And a method of cleaning the air diffuser.

In order to achieve the above-mentioned object, the first characteristic configuration of the air diffuser according to the present invention is composed of a viscoelastic body in the form of a tube as described in claim 1 of the claims, and has an outer peripheral surface and an inner peripheral surface. A diffuser tube comprising: a membrane body in which a plurality of aeration hole slits penetrating between surfaces is formed; and a tubular membrane support body that supports the membrane body from the inside,
A through hole penetrating the tube wall of the membrane support is formed on each of the upper surface side and the lower surface side of the membrane support, and at least a region of the film body corresponding to the through hole is formed with the air diffuser slit. In addition , the number of through holes formed on the lower surface side of the membrane support is smaller than the number of through holes disposed on the upper surface side, and the total opening area is also disposed on the upper surface side. The point is smaller than the sum of the opening areas of the holes .

  Since no air hole slit is formed in the region of the film body corresponding to the through hole of the membrane support, the gas ejected from the through hole, for example, air is not immediately released from the air hole slit, and the membrane support As a result, the air diffuser slit in a specific region does not open greatly, and as a result, the air diffuser slit may be blocked. Extremely low.

Further , even when the cleaning liquid is supplied into the membrane support for cleaning and then the supply of air is resumed, the cleaning liquid flows out from the through-hole on the lower surface side of the membrane support by air pressure, and the membrane and the membrane support It flows through the gap and is drained from the diffuser slit. In the meantime, air is supplied in the axial direction along the space formed above the membrane support, and is ejected upward from the through hole on the upper surface side of the membrane support, and the gap between the membrane support and the membrane support is discharged. Since it flows and is discharged from the diffuser slit, the diffuser performance is quickly recovered.

Furthermore, in addition to the fact that the water pressure acting on the membrane body located on the upper surface side of the membrane support is lower than the water pressure acting on the membrane body located on the lower surface side of the membrane support, the supply of the gas supplied to the inside of the membrane support The force that is ejected from the through hole on the upper surface side of the membrane support by pressure and pushes up the membrane body is greater than the force that is ejected from the through hole on the lower surface side of the membrane support and pushes down the membrane body, A gap is stably formed between the film body. As a result, the gas ejected from the through hole on the upper surface side of the membrane support can discharge the bubbles stably from each of the diffuser slits through the gap between the membrane and the membrane support.

In the second characteristic configuration, as described in the second aspect, in addition to the first characteristic configuration described above, the air diffuser slit is formed from 20 degrees to 70 degrees from the vertical line to the left and right sides in a side view of the air diffusion tube. It is in the point formed in the range of the inclination angle of degree .

In the third feature configuration, as described in claim 3, in addition to the second feature configuration described above, a plurality of the through holes are formed on the upper surface side of the membrane support, and each through hole is formed in the membrane. It exists in the point formed so that it may be equally arrange | positioned in the length direction of a support body .

According to the above-described configuration, the air ejected from the plurality of through holes on the upper surface side of the membrane support that is uniformly arranged in the length direction of the membrane support spreads uniformly in the gap between the membrane support and the membrane support. Since air bubbles are discharged from each of the air diffuser slits of the body and uniform and uniformly dispersed bubbles are formed, air can be uniformly diffused in the length direction of the membrane support. In addition, when the cleaning liquid is filled in the membrane support for cleaning the air diffuser, the cleaning liquid that has flowed out from the plurality of through holes on the upper surface side of the membrane support that is evenly arranged in the length direction of the membrane support. evenly spread in the gap between the support, since the cleaning liquid in the aeration pores slits of the membrane body is supplied, Ru can be performed uniformly cleaning the length of the membrane support.

The characteristic configuration of the method for cleaning an air diffuser according to the present invention is the method for cleaning an air diffuser having any one of the first to third characteristics as described in claim 4, wherein the membrane support With the supply of gas to the inside of the body stopped, supply the cleaning liquid to the inside of the membrane support to fill the inside of the diffuser tube with the cleaning liquid, and resume the supply of gas to the inside of the membrane support after the cleaning is completed In addition, the cleaning liquid inside the diffuser tube is discharged from the diffuser slit.

  According to the above configuration, first, the supply of the cleaning liquid is supplied to the inside of the membrane support in a state where the supply of gas to the inside of the membrane support is stopped, the inside of the diffusion tube is filled with the cleaning liquid, and the diffusion tube is cleaned. When the gas supply to the inside of the membrane support is resumed after the cleaning is completed, the cleaning liquid flows out from the through hole on the lower surface side of the membrane support and passes through the gap between the membrane and the membrane support from the diffuser slit to be treated. Discharged inside. Therefore, a ventilation space is secured on the upper side of the inside of the membrane support, and the gas ejected from the through hole on the upper surface side of the membrane support is discharged as a bubble from the diffusion hole slit through the gap between the membrane and the membrane support, Aeration performance recovers quickly.

  As described above, according to the present invention, a diffuser and a diffuser that can quickly diffuse evenly, even after the cleaning liquid is supplied to the membrane support and the diffuser is cleaned. A method for cleaning the trachea can be provided.

Illustration of sewage treatment equipment Illustration of membrane separator Illustration of membrane cartridge Top view of diffuser (A) is a plan view of the diffuser tube, (b) is a cross-sectional side view of the same (A) is a plan view of the air diffuser, (b) is the longitudinal sectional view, and (c) is the bottom view.

Hereinafter, an air diffuser and a method for cleaning the air diffuser according to the present invention will be described.
As shown in FIG. 1, a sewage treatment facility 1 employing a membrane separation activated sludge method includes a pretreatment facility 2, a flow rate adjustment tank 3, a membrane separation tank 4 in which a membrane separation device 6 is disposed, and a treatment. A water tank 5 is provided.

  The pretreatment facility 2 is provided with a screen 2a or the like for removing foreign matters such as foreign matters mixed in the raw water to be treated, and the raw water from which foreign matters have been removed by the screen 2a or the like is stored in the flow rate adjusting tank 3. The Even when the inflow amount of the raw water fluctuates, a flow rate adjusting mechanism such as a pump P or a valve is provided so that the raw water with a constant flow rate is stably supplied from the flow rate adjusting tank 3 to the membrane separation tank 4.

  In the membrane separation tank 4 filled with activated sludge, organic substances in the raw water are decomposed by biological treatment with activated sludge, and the permeated water filtered through the membrane separator 6 is led to the treated water tank 5 and temporarily stored. And then released. Excess sludge grown in the membrane separation tank 4 is drawn out of the tank, and the inside of the tank is kept at a constant sludge concentration.

  As shown in FIG. 2, the membrane separation device 6 includes 100 plate-like membrane cartridges 8 in a membrane case 7 that is open at the top and bottom so that each membrane surface is in a vertical posture and about 6 mm to 10 mm. (In this embodiment, 8 mm) are arranged at regular intervals, and a diffuser 12 is provided below the membrane case 7.

  The air diffuser 12 includes an air diffuser tube 13 in which a plurality of air diffuser slits are formed, and each air diffuser tube 13 is connected to a blower 15 installed outside the tank via an air diffuser header tube 14 and an air passage 15a. . Each air diffuser 13 is connected to a cleaning liquid supply device 19 installed outside the tank via an air diffuser header 14 and a liquid supply path 19a. The cleaning liquid supply device 19 includes a flow rate adjusting mechanism such as a pump and a valve for supplying a certain amount of cleaning liquid.

  A pump 18 as a differential pressure generating mechanism installed outside the tank is connected to the membrane cartridge 8 via a water collecting pipe 17, and the water to be treated in the tank is suction filtered so as to pass through the membrane surface of the membrane cartridge 8. The

  As shown in FIG. 3, the membrane cartridge 8 has filtration membranes 10 disposed on both front and back surfaces of a filter plate 9 made of a thermoplastic resin such as ABS resin having a length of 1000 mm × width of 490 mm, and a joint portion 11 at the periphery of the filtration membrane 10. The filter plate 9 is formed by fusion bonding with ultrasonic waves or heat, or by adhesive bonding using an adhesive or the like.

  The filtration membrane 10 is an organic filtration membrane in which a porous resin is applied and impregnated on a support 10a which is a nonwoven fabric made of PET, for example, and a microporous membrane 10b having an average pore diameter of about 0.2 μm is formed.

  A plurality of groove portions 9b having a depth of about 2 mm and a width of about 2 mm are formed on the surface of the filter plate 9 along the longitudinal direction, and a horizontal groove portion 9c communicating with each groove portion 9b is formed at the upper end portion thereof. Horizontal groove portions 9 c formed on the front and back surfaces are communicated with each other through a communication hole 9 d and communicated with a nozzle 9 a formed on the upper edge portion of the membrane support 9.

As shown in FIG. 2 , each nozzle 9 a is connected to a water collection pipe 17 through a tube 16, a pump 18 is connected to the water collection pipe 17, and the permeated water sucked by the pump 18 is transferred to the treatment water tank 5. It is comprised so that.

  By operating the air diffuser 12 and the pump 18 of the membrane separation device 6 as described above, bubbles generated in the air diffuser 13 supplied with air from the blower 15 are supplied to the membrane cartridge 8, and the water to be treated is filtered. A filtration operation is performed in which a permeated water having a set flow rate is obtained by filtration at 10. For example, when the suction pressure is increased periodically or during filtration operation, the air diffuser with the pump 18 stopped in order to prevent fouling of the filtration membrane 10 while maintaining the properties of the activated sludge in the tank. The relaxation operation which operates only 12 is performed. Further, when the suction pressure increases periodically or after the relaxation operation, a chemical solution cleaning step is performed in which the chemical solution is injected into each membrane cartridge 8 via the water collection pipe 17 to clean the filtration membrane 10.

Next, the configuration of the air diffuser 12 will be described.
As shown in FIGS. 2 and 4, a plurality of diffuser tubes 13 are juxtaposed at a predetermined interval in parallel with each other, and the diffuser header tubes 14 are respectively disposed at one end and the other end of each diffuser tube 13. Is connected. The two diffuser header tubes 14 are provided with a plurality of cylindrical connection ports 14 a corresponding to the diffuser tubes 13 on the side surface. The outer diameter of the connection port 14a is substantially equal to the inner diameter of the diffuser tube 13. The diffuser pipe 13 is connected and fixed to the diffuser header pipe 14 by fitting both ends of the diffuser pipe 13 to the connection ports 14 a of the diffuser header pipes 14.

  An air inlet and a cleaning liquid inlet are provided at one end 14b of the diffuser header pipe 14, and the other end is closed. The air inlet is connected to the outlet of the blower passage 15 a from the blower 15, and the cleaning liquid inlet is connected to the outlet of the liquid supply passage 19 a from the cleaning liquid supply device 19.

  As shown in FIGS. 5A and 5B, each air diffuser 13 includes a cylindrical membrane support 20, a membrane 21 mounted so as to cover the outer peripheral surface of the membrane support 20, and a membrane And a metal band (SUS304 or the like) 22 that is fastened to the outer peripheral surface of the membrane support 20 by tightening both ends of the film 21. 5A is a plan view, and FIG. 5B is a side cross-sectional view. The left side of FIG. 5B corresponds to the upper surface side of the diffuser tube 13, and the right side of FIG. Corresponds to the lower surface side of

  As shown in FIGS. 6A, 6B, and 6C, six through holes 20a are formed at equal intervals (100 mm) in the tube axis direction (length direction) at the center of the upper surface side of the membrane support 20. The two through-holes 20a are formed in the center of the lower surface side of the membrane support 20 at the center in the tube axis direction at a narrow interval (20 mm) in the tube axis direction. The diameter of each through hole 20a is 5 mmφ. Accordingly, the number (two) of the through holes 20a formed on the lower surface side of the membrane support 20 is smaller than the number (6) of the through holes 20a disposed on the upper surface side, and the total opening area is also large. small.

  The membrane support 20 is composed of an ABS resin tube having a thickness of about 4 mm. The film body 21 is composed of a viscoelastic body such as EPDM, polyurethane resin, or silicone rubber, and has a thickness of about 1 mm. The film body 21 is formed with a plurality of air hole slits 21a having a length of about 3 mm, which are cut by a blade so as to penetrate between the outer peripheral surface and the inner peripheral surface.

  As shown in FIG. 5 (b), the air diffuser slit 21 a is a tube axis of the air diffuser 13 within a range of an inclination angle of about 20 degrees to 70 degrees from the vertical line to the left and right sides in a side view of the air diffuser 13. It is formed in a range inward of the band 22 positions on both sides in the direction. In addition, the auxiliary line of FIG.5 (b) does not show an exact angle.

  And it sets so that the diffused hole slit 21a may not be formed in the area | region corresponding to the through-hole 20a formed in the film | membrane support body 20. As shown in FIG. The through-hole 20a only needs to be formed on the upper surface side or the lower surface side of the membrane support 20, and if it is a region that does not overlap with the formation region of the diffuser hole slit 21a, the center or lower surface side of the membrane support 20 It is not limited to be formed in the center.

  An annular convex portion 20 b is formed on the outer peripheral surface of both end portions of the membrane support 20. The membrane body 21 is mounted so as to cover the annular convex portion 20b of the membrane support 20, and the position of the band 22 is inside the annular convex portion 20b. The annular convex portion 20b prevents the film body 21 and the band 22 from being displaced with respect to the film support body 20.

  Cutouts 20c are formed at both end edges at the center of the upper surface side of the membrane support 20 (see FIG. 6A). Cutouts 21b are also formed at both edge portions of the film body 21 (see FIG. 5A). When the membrane body 21 is mounted on the outer peripheral surface of the membrane support 20, the notches 21b of the membrane body 21 are aligned with the notches 20c of the membrane support 20, so that the position of the diffuser slit 21a is as shown in FIG. ).

  With the configuration of the air diffuser 12 described above, air is supplied to each air diffuser 13 from both ends so that the air pressure in the membrane support 20 is made uniform in the tube axis direction, and at the position directly above the membrane support 20. Since the six through-holes 20a are arranged at equal intervals in the tube axis direction, the air ejected from the six through-holes 20a directly above the membrane support 20 is made uniform. Therefore, the membrane body 21 on the upper surface side of the membrane support 20 is pushed up with a uniform pressure, and a uniform gap is formed between the membrane support 20 and the membrane support 20 in the tube axis direction of the membrane support 20.

  The air ejected from the six through holes 20a directly above the membrane support 20 hits the membrane 21 and then flows downward from the side through the gap between the membrane 21 and the membrane support 20 to form the membrane. The gas is discharged as bubbles from the air diffuser slit 21a of 21 into the liquid to be processed. Here, since the air diffuser slit 21a is formed at a position close to the upper surface side and the upper surface side of the air diffuser 13 having a low water pressure, while avoiding the disadvantage that the air ejected from the through hole 20a directly hits the air diffuser slit 21a, Efficiently reaches the air diffuser slit 21a, and can achieve high air diffusion performance that is uniform in the tube axis direction.

When the air diffuser performance of the air diffuser 12 is deteriorated or periodically, a cleaning process is performed in which the cleaning liquid is supplied from the cleaning liquid supply device 19 to the air diffuser 12 for cleaning. In the cleaning step, first, the cleaning liquid is supplied to the inside of the membrane support 20 in a state where the supply of air to the inside of the membrane support 20 is stopped and filled with the cleaning liquid. Then, it is allowed to stand for a predetermined time, and the cleaning liquid filled in the membrane support 20 is caused to flow out from each through-hole 20a by press-fitting the cleaning liquid into the membrane support 20 or a combination thereof, and the membrane body 21 and the membrane support The gap with the body 20 is passed through and brought into contact with the diffuser slit 21a. Thereby, the air diffuser 13 (especially the air diffuser slit 21a) is cleaned.

  After the cleaning is completed, the supply of air to the inside of the membrane support 20 is resumed. Due to the pressure of the air supplied to the inside of the membrane support 20, the cleaning liquid in the membrane support 20 flows out from the through hole 20 a at the lower surface position, passes through the gap between the membrane 21 and the membrane support 20, and the diffuser slit 21 a. Discharged into the liquid to be treated. Here, the cleaning liquid is accumulated in the lower part of the membrane support 20 by its own weight, but the cleaning liquid can be discharged well from the through hole 20a formed on the lower surface side of the membrane support 20.

  As a result of the cleaning liquid in the membrane support 20 being discharged, a ventilation space is secured in the upper part of the membrane support 20, and the air ejected from the through hole 20 a on the upper surface side passes through the gap between the membrane body 21 and the membrane support 20. After that, it is discharged as air bubbles from the diffuser slit 21a. Since the through-hole 20a is formed on the upper surface side of the membrane support 20, when a small ventilation space is formed in the upper part of the membrane support 20, air bubbles are quickly discharged from the air diffuser slit 21a, and early The air diffusion performance of the air diffusion tube 13 is restored.

  The above-described embodiment is one aspect of the present invention, and the present invention is not limited by the description, and it is needless to say that the design can be appropriately changed within a range where the effects of the present invention are exhibited.

13: Air diffuser 20: Membrane support 20a: Through hole 21: Membrane 21a: Air diffuser slit

Claims (4)

A membrane body formed of a tube-shaped viscoelastic body and formed with a plurality of air hole slits penetrating between the outer peripheral surface and the inner peripheral surface; and a tubular membrane support body that supports the membrane body from the inside. An air diffuser provided,
A through hole penetrating the tube wall of the membrane support is formed on each of the upper surface side and the lower surface side of the membrane support, and at least a region of the film body corresponding to the through hole is formed with the air diffuser slit. Not
The number of through-holes formed on the lower surface side of the membrane support is smaller than the number of through-holes disposed on the upper surface side, and the total opening area is also the opening area of the through-holes disposed on the upper surface side. A diffuser characterized by being smaller than the sum of 2. The air diffuser according to claim 1, wherein the air diffuser slit is formed within a range of an inclination angle of 20 degrees to 70 degrees on both right and left sides from the vertical line in a side view of the air diffuser. 3. The dispersion according to claim 2, wherein a plurality of the through holes are formed on the upper surface side of the membrane support, and the through holes are formed so as to be evenly arranged in the length direction of the membrane support. trachea. A method of cleaning an air diffuser according to any one of claims 1 to 3,
With the supply of gas to the inside of the membrane support stopped, a cleaning liquid is supplied to the inside of the membrane support to fill the inside of the diffuser tube with the cleaning liquid, and after the cleaning is completed, the gas is supplied to the inside of the membrane support. A method for cleaning an air diffuser, characterized in that the supply is resumed and the cleaning liquid inside the air diffuser is discharged from the air diffuser slit.

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