JP4934978B2 - Hollow fiber membrane module - Google Patents

Description

  The present invention relates to a submerged hollow fiber membrane module suitably used for water treatment applications and the like, and more specifically, does not generate internal defects of the submerged medium yarn membrane module, suppresses the bias of the hollow fiber membrane bundle, An object of the present invention is to provide a submerged hollow fiber membrane module suitable for improving production efficiency.

  Conventionally, submerged hollow fiber membrane modules for clean water have been widely used for clean water and industrial water applications, and many embodiments and a wide variety of applications are widely known. In general, the immersion type hollow fiber membrane module is also disclosed in, for example, Patent Document 1, and as shown in FIG. 7, a plurality of hollow fiber membranes 2 are housed in an open cylindrical case 3 that is permeable to water. ing.

  In the immersion type hollow fiber membrane module shown in FIG. 7, one end portion (upper end portion) of the hollow fiber membrane 2 is fixed with a resin 4 to the cylindrical case 3 with the end face opened, The other end portion (lower end portion) of 2 is fixed to the cylindrical case 3 with a resin 4 with the end face closed. When using these submerged hollow fiber membrane modules, the raw water (water to be treated) is usually introduced from the open cylindrical case 3 while being arranged vertically and sucked from the inlet of the upper cap 5, and the hollow fiber. The filtered water that has passed through the membrane and reached the hollow portion is taken out from the upper cap 5 to the outside. At this time, when the filtration proceeds, suspended substances in the raw water adhere to the outer surface of the hollow fiber membrane, the filtration resistance increases, and the membrane permeation flow rate (FLUX) gradually decreases. Therefore, in order to restore the filtration resistance to the original low state, the supply of raw water is stopped, so-called backwashing is performed in which a predetermined amount of filtered water is supplied from the upper cap 5 side, and air is supplied from the inlet 7 provided at the lower part. And air scrubbing is performed to drop the suspended solids and discharge them together with the water in the cylindrical case from the opening of the lower cap 6 and the cylindrical case 3.

  Usually, the immersion type hollow fiber module has a structure in which at least one end portion of the hollow fiber membrane bundle is bonded and fixed with a resin and bonded to the inner surface of the case. Scratching between the hollow fiber membrane and the inner surface of the cylindrical case is large, and yarn damage is likely to occur. Furthermore, the wall surface of the cylindrical case is an open cylindrical case with a net or lattice, and the hollow fiber membrane is substantially exposed to the outside, so that the cylindrical case and the hollow fiber membrane are damaged during transportation and installation. There was a problem to make.

In addition, when the hollow fiber membrane module is manufactured by a centrifugal bonding method in which the hollow fiber membrane module is bonded while being rotated horizontally, the hollow fiber membrane bundle is biased to the lower side of the case due to its own weight, Is isolated and adhered to the vicinity of the inner wall of the case, resulting in thread breakage due to impact during transport of the module and fluid flow during use, and uneven flow of raw water supplied during operation and air scrubbing. , The filtration performance of the membrane varies greatly depending on the site, causing a problem that the filtration performance is lowered.
JP 2002-346344 A

  An object of the present invention is to provide a hollow fiber membrane module that solves the above-described conventional problems and is inexpensive and easy to manufacture.

The present invention achieves the above object. That is, the present invention
(1) A plurality of hollow fiber membranes are arranged in an open cylindrical case, an end cylinder is arranged at an end of the cylindrical case , and the end cylinder is larger than an outer diameter of the cylindrical case A cylindrical first portion having an inner diameter , and a cylindrical second portion that is smaller than the inner diameter of the cylindrical case on the outer side of the cylindrical case in the longitudinal direction of the first portion and that is continuous with the first portion. The hollow fiber membrane module comprising the plurality of hollow fiber membranes and the cylindrical case fixed to the end tube by a resin inside the end tube .

(2) The hollow fiber membrane module according to (1), wherein a through-hole is provided on a circumference of the first portion of the end tube.

(3) The ridge portion of the inner peripheral surface of the second portion of the end tube is configured by a curved surface shape that is convex in the central axis direction of the end tube. (1) or (2) Hollow fiber membrane module.

(4) The ridge portion of the inner peripheral surface of the second portion of the end tube is substantially constituted by a part of a side surface of a cone having a vertex on the central axis of the end tube. The hollow fiber membrane module according to (1) or (2) .

(5) the inner peripheral surface of the first portion of said end tube, characterized in that said tubular case is a surface tapered to expand its clear width in the direction extending (1) - ( The hollow fiber membrane module according to any one of 4) .

According to the first aspect of the present invention, in the end cylinder composed of the first part connected to the cap and the second part continuous to the first part, the inner peripheral surface of the second part is the inner periphery of the cylindrical case. Since it is inside the surface, the hollow fiber membrane can be focused so that it does not come into contact with the cylindrical case, and the hollow fiber membrane that has been shaken by liquid flow during the filtration process or air scrubbing rubs against the cylindrical case This can be alleviated and does not cause yarn damage. Moreover, since the inner peripheral surface of the 1st part of an end cylinder exists on the outer side rather than a cylindrical case outer peripheral surface, it can convey and install, without making a cylindrical case and hollow fiber membranes contact. Further, the end cylinder can be integrated with the cylindrical case by resin at the time of potting, and it is possible to simplify the machining process by eliminating the trouble of attaching the end cylinder in a subsequent process.

In addition, since the second portion of the end tube converges the hollow fiber membrane bundle in the central direction from the cylindrical case, the hollow fiber membrane module is hollow even when manufactured by the centrifugal bonding method in which the hollow fiber membrane module is bonded while rotating horizontally. The hollow fiber membrane bundle is not biased and adhered to the lower part of the case by its own weight, and the hollow fiber membrane is not adhered to the vicinity of the inner wall surface of the case. As a result, thread breakage does not occur due to impact during module transportation or liquid flow during use, the flow of water or air can be made relatively uniform, and filtration performance and cleaning performance can be improved.

According to the second aspect of the present invention, by providing a through hole on the circumference of the first portion of the end tube , it can be used as a resin injection hole as a sealant during potting, and further, inflow of raw water during filtration operation It can also be used as a hole.

According to the third and fourth aspects of the present invention, the ridge portion of the inner peripheral surface of the second portion of the end tube is formed into a curved shape that is convex in the center direction of the end tube, or the apex on the center axis of the end tube When the hollow fiber membrane bundle is inserted, damage to the hollow fiber membrane can be prevented.

According to invention of Claim 5, when attaching an end cylinder to a cylindrical case, it can insert smoothly and it can be set as a module with easy assembly.

  The hollow fiber membrane module according to the present invention will be described below by taking an immersion hollow fiber membrane module used for water filtration as an example. In addition, this invention is not limited to the immersion type hollow fiber membrane module for clean water, It can apply also to hollow fiber membrane modules, such as for industrial water and sewage.

  First, the structure of the hollow fiber membrane module of this invention is demonstrated, referring a figure. FIG. 1 is a schematic longitudinal sectional view of an immersion type hollow fiber membrane module of the present invention, and FIG. 2 is a partially enlarged view of the vicinity of the end tube 10 of FIG.

  As shown in FIG. 1, the submerged hollow fiber membrane module 1 has end cylinders 10a and 10b at both ends of a cylindrical case 3 that is an open system through which raw water can pass, and the cylindrical case having the end cylinders. A plurality of hollow fiber membranes 2 are housed in 3, and both ends of the hollow fiber membranes 2 are liquid-tight with resin 4 together with the end tube 10 a at both ends of the cylindrical case 3 with the end surfaces open. The lower end has a structure capable of introducing air into the hollow fiber bundle, and is liquid-tightly fixed with the resin 4 together with the end tube 10b.

  The upper cap 5 having the filtrate outlet 9 is provided in the upper end cylinder 10a of the cylindrical case 3, and the lower cap 6 having the air inlet 8 is provided in the lower end cylinder 10b of the cylindrical case 3 in a liquid-tight manner. Connected. In addition, although it does not specifically limit as a means to make liquid-tight, what is necessary is just to attach with a sanitary clamp etc. pinching packing. An air introduction valve (not shown) connected to the air source and a first drain valve (not shown) connected to the drainage channel are connected to the inlet 8 of the lower cap 6. A suction pump (not shown) and a filtrate valve (not shown) connected to the filtrate outlet path are connected to the filtrate outlet 9 of the upper cap 5.

  Examples of the material of the cylindrical case 3 and the end cylinders 10a and 10b include polyolefins such as polyethylene, polypropylene, and polybutene, polytetrafluoroethylene (PTFE), tetrafluoroethylene perfluoroalkoxyethylene copolymer (PFA), and four fluorine. Ethylene hexafluoropropylene copolymer (FEP), tetrafluoroethylene ethylene copolymer (ETFE), trifluorinated ethylene resin (PCTFE), ethylene chlorotrifluoroethylene (ECTFE), polyvinylidene fluoride (PVDF), etc. Fluorine-based resins, chlorinated resins such as polyvinyl chloride and polyvinylidene chloride, polysulfone resins, polyether sulfone resins, polyallyl sulfone resins, polyphenyl ether resins, acrylonitrile-butadiene-styrene copolymer resins (ABS) , Acrylonitrile - styrene copolymer resin, polyphenylene sulfide resin, polyamide resin, polycarbonate resin, polyether ketone resin, polyether ether ketone resin is used alone or in a mixture. Other than the resin, aluminum, stainless steel, and the like are preferable, and a composite material such as a resin-metal composite, a glass fiber reinforced resin, and a carbon fiber reinforced resin may be used. Further, the cylindrical case 3 may have a net-like shape, a lattice-like shape, or the like so long as it can pass water and supply raw water to the hollow fiber membrane.

  The material of the hollow fiber membrane 2 is not particularly limited, and polysulfone, polyethersulfone, polyacrylonitrile, polyimide, polyetherimide, polyamide, polyetherketone, polyetheretherketone, polyethylene, polypropylene, ethylene-vinyl alcohol copolymer, Examples thereof include cellulose, cellulose acetate, polyvinylidene fluoride, ethylene-tetrafluoroethylene copolymer, polytetrafluoroethylene, and the like, and these may be combined.

  Examples of the resin 4 that fixes the hollow fiber membrane 2, the cylindrical case 3, and the end tube 10 inside the end tube 10 include an epoxy resin and a polyurethane resin.

  Next, the procedure for using the hollow fiber membrane module shown in FIG. 1 will be described.

  First, in the process of filtering the raw water, the suction pump is driven with the air introduction valve and the first drain valve closed and the filtrate valve opened, and the soaking tank (not shown) surrounding the hollow fiber membrane module 1 is driven. The filled raw water is poured from the cylindrical case 3 and the filtrate is led out from the filtrate outlet 9 to the filtrate outlet.

  At this time, as the filtration proceeds as in the hollow fiber membrane module shown in FIG. 1, suspended substances in the raw water adhere to the outer surface of the hollow fiber membrane, the filtration resistance increases, and the membrane permeation flow rate decreases. Therefore, backwashing and air scrubbing are performed.

  In backwashing, the suction pump is stopped, the first drain valve is closed, the filtrate valve is opened for a predetermined time, and water is allowed to permeate from the inside of the hollow fiber.

  In the air scrubbing, the suction pump is stopped, the first drain valve and the filtrate valve are closed, the air introduction valve is opened for a predetermined time, and air is introduced into the hollow fiber membrane module 1.

  In this way, drainage is performed after backwashing and air scrubbing, but at the time of drainage, the suction pump is stopped and discharged from the first drain valve and the treated water outlet provided in the immersion tank to the outside of the immersion tank. .

The end cylinder in the present invention described above means a sleeve having a function of separating the hollow fiber membrane and the cylindrical case so as not to contact each other. Here, the sleeve means a connector for connecting a cap or piping. Said end sleeve has a larger inner diameter tubular first portion than the outer diameter of the cylindrical case, a smaller inner diameter than the inner diameter of the tubular casing outside the cylindrical case longitudinal first portion It is necessary to provide a cylindrical second portion that is continuous with the first portion . Here, the inner diameter 20 of the first portion of the end tube and the inner diameter 17 of the second portion of the end tube are the inner diameters of the bottom surfaces of the end tube that belong to the first portion of the first portion of the end tube. The inner diameter 20 and the inner diameter on the side belonging to the second part are respectively defined as the inner diameter 17 of the second part of the end tube (see FIG. 2). The hollow fiber membrane can be separated from the cylindrical case, and the hollow fiber membrane that has been shaken by liquid flow during the filtration process or air scrubbing can be reduced from rubbing against the cylindrical case without causing yarn damage. The effect of the present invention is that the cylindrical case and the hollow fiber membrane can be transported and installed without contacting each other, and the end tube can be integrated with the cylindrical case by resin during potting. in order to sufficiently expressed, in the second portion of the end cylinder, all of the inner peripheral surface of the second portion of the end cylinder is located inside the cylindrical inner peripheral surface of the case, and, in the first portion of the end tube it is preferable that all of the inner peripheral surface of the first portion of the end cylinder is outside the cylindrical case outer circumferential surface.

  With respect to the shape of the end cylinder, the opening (inner diameter 17) of the second portion 12 is, for example, more radially than the opening (inner diameter 18) of the cylindrical case when the overall length of the cylindrical case 3 is 1 m and the outer diameter is 150 mm. It is preferably within the range of 4 to 40 mm inside (in the direction of the central axis of the end tube). More preferably, it is within a range of 10 to 20 mm. By making it within this range, it is possible to further reduce the abrasion of the hollow fiber membrane that has been shaken by the liquid flow during the filtration process or air scrubbing to the cylindrical case, and the hollow fiber membrane bundle insertion area can be increased. This is because the film filling rate can be increased. If the opening (inner diameter 20) of the first portion 11 is in the range of 0.5 to 5 mm outside the outer periphery (outer diameter 19) of the cross section of the cylindrical case in the radial direction (the direction opposite to the central axis of the end cylinder). Good. By being within such a range, not only the end tube can be easily inserted into the cylindrical case, but also when the end tube is attached to the cylindrical case, the respective center axes are not easily decentered, and the inner surface of the end tube This is because the resin can surely be impregnated between the outer surface of the cylindrical case and the cylindrical case.

Further, the inner peripheral surface of the first portion shown in 15 of FIG. 5 is a tapered surface whose inner method expands in the direction in which the cylindrical case extends, so that the end tube is changed to the cylindrical case. This is preferable because it can be easily inserted. The length of the end tube in the longitudinal direction is preferably 5 to 50 mm longer than the resin part length 13 for potting, more preferably 10 to 30 mm. In such a case, processing of the through-hole becomes easy, and the exposed area of the cylindrical case can be increased, which is convenient. And it is preferable to provide the through-hole 14 with a diameter of 5-20 mm in the interface vicinity of the resin part for potting. The through hole 14 can be used as a resin injection port during potting and also as a raw water inflow port during filtration operation. The number of through holes provided in this way is preferably 1-12, more preferably 2-4, distributed uniformly on the circumference of the first portion of the end tube. The reason for this is that the resin is impregnated from one hole during potting, eliminating the trouble of closing the other hole with a silicon stopper at that time, and providing a uniform through hole to provide a good balance in the circumferential direction during filtration operation. This is because the raw water can be introduced, and the variation in filtration of the hollow fiber membrane can be reduced.

Further, by smoothly processing or chamfering the ridge portion 16 on the inner peripheral surface of the second portion that is continuous with the first portion, for example, as shown in FIG. 5, the second portion of the end tube The end portion side end portion of the inner peripheral surface is formed in a curved surface shape convex toward the central axis direction of the end tube, or the ridge portion 16 of the inner peripheral surface of the second portion of the end tube is substantially formed as shown in FIG. Or a part of a side surface of a circular cone having a vertex on the central axis of the end tube. By performing such processing and chamfering, it is possible to prevent the hollow fiber membrane from being caught when the hollow fiber membrane bundle is inserted, and preventing the hollow fiber membrane from being damaged.

  And after attaching the end cylinder 10 to the cylindrical case 3, a hollow fiber membrane is inserted, and the cylindrical case and the hollow fiber bundle are separated from this through-hole 14 by impregnating the potting resin by a centrifugal method. Since a module in which the hollow fiber membrane, the cylindrical case, and the end cylinder are integrated with the resin can be manufactured, the trouble of attaching the end cylinder in the subsequent process can be saved, and the processing process can be simplified.

Further, since the hollow fiber membrane bundle is converged in the central direction of the cylindrical case by reducing the inner diameter 17 of the second portion 12, the hollow fiber membrane bundle having a small membrane filling rate when potting the membrane bundle by the centrifugal bonding method. However, the hollow fiber membrane bundle does not adhere to the lower part of the case by the weight of the hollow fiber membrane bundle itself, or the hollow fiber membrane does not adhere to the vicinity of the inner wall surface of the case. As a result, yarn breakage does not occur due to the impact during transportation of the module and the liquid flow during use, the flow of water and air can be made relatively uniform, and the filtration performance and cleaning performance can be improved.

It is a schematic longitudinal cross-sectional view which shows one Embodiment of the immersion type hollow fiber membrane module which concerns on this invention. It is the elements on larger scale of the immersion type hollow fiber membrane module of FIG. 1 which shows the state which the hollow fiber membrane bundle and the cylindrical case are spaced apart by the end cylinder which concerns on this invention. It is an external view which shows one Embodiment of the end cylinder which concerns on this invention. It is the external view which looked at the end cylinder of FIG. 3 from the lower side. FIG. 5 is a cross-sectional view of the end tube showing one preferred embodiment of the present invention (cross-sectional view of the end tube of FIG. 4). It is a cross-sectional view of the end tube showing another preferred embodiment of the present invention. It is a schematic longitudinal cross-sectional view of the conventional immersion type hollow fiber membrane module.

Explanation of symbols

1: Submerged hollow fiber membrane module 2: Hollow fiber membrane 3: Cylindrical case (open system)
4: Resin 5: Upper cap 6: Lower cap 7: Aeration hole 8: Inlet 9: Filtrate outlet 10, 10a, 10b: End tube 11: First portion of end tube 12: Second portion of end tube 13: Resin part length 14: Through hole 15: Inner peripheral surface 16 of the first part of the end cylinder: Ridge part 17 of the inner peripheral surface of the second part of the end cylinder 17: Inner diameter 18 of the second part of the end cylinder: Inner diameter 19: Outer diameter of the cylindrical case 20: Inner diameter A of the first portion of the end cylinder A: Outside in the longitudinal direction of the cylindrical case B: Center axis C of the end cylinder C: Apex of the cone existing on the central axis of the end cylinder D: Side surface of cone having apex on central axis of end tube

Claims (5)

A plurality of hollow fiber membranes are arranged in an open cylindrical case, an end cylinder is arranged at an end of the cylindrical case , and the end cylinder is a cylinder having an inner diameter larger than the outer diameter of the cylindrical case It consists of a first portion of Jo, the first portion cylindrical case longitudinally outwardly to the cylindrical casing inner diameter smaller inner diameter in a by cylindrical second portion continuous with the first portion than in the, The hollow fiber membrane module is characterized in that the plurality of hollow fiber membranes and the cylindrical case are fixed to the end tube by a resin inside the end tube . The hollow fiber membrane module according to claim 1, further comprising a through hole on a circumference of the first portion of the end tube. 3. The hollow fiber membrane module according to claim 1 , wherein a ridge portion of an inner peripheral surface of the second portion of the end tube is formed in a curved surface shape that is convex in a central axis direction of the end tube. . Claim 1 edge portion of the inner peripheral surface of the second portion of said end tube, characterized in that it is composed of a part of the side surface of the conical having a vertex on the center axis of the substantially said end tube Or the hollow fiber membrane module of 2. The inner peripheral surface of the first portion of the end tube is a tapered surface whose inner method expands in a direction in which the cylindrical case extends . the hollow fiber membrane module according to.

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