This invention relates to: hollow fibers, a method of manufacturing a hollow fiber bundle, a cylindrical module of hollow fiber membrane, and an immersion type module of hollow fiber membrane. This invention relates in particular to: a hollow fiber bundle, a method of manufacturing the hollow fiber bundle, a cylindrical module of hollow fiber membrane, and an immersion type module of hollow fiber membrane wherein specified intervals are maintained among the hollow fibers and solid matter accumulated on the outside surface of the hollow fibers is easy to scrub off.
Porous hollow fibers are conventionally in use for filtering liquids, such as in sewage water treatment, drinking water sanitization, fruit juice processing, and blood purification. In many applications, because of large filtering area and facility of cleaning off filtered solid matter, liquid is caused to permeate from the outside surface of the hollow fiber to the inside, in a pressurized type or a suction type. When liquid is filtered by making liquid permeate from the outside surface of the fiber to the inside, solid matter removed by filtering accumulates on the outside surfaces of the hollow fibers. The hollow fibers are bundled and used often as a hollow fiber bundle. Therefore, a method is employed in which the solid matter having accumulated on the outside surfaces of the hollow fibers is removed by the scrubbing of bubbles rising around the hollow fibers (For example, refer to the Patent Document 1).
[Patent Document 1]
Japanese Utility Model 63-38884 (FIG. 2, pp. 1-2)
In the case that the solid matter having accumulated on the outside surface of the hollow fibers is removed by the scrubbing of the rising bubbles, if specified intervals among hollow fibers are not maintained, air for scrubbing is hard to send appropriately around the hollow fibers. In particular in the case that the hollow fibers are put vertically and bundled and nozzles for delivering scrubbing-use air are disposed at the potting that secures the underside of the hollow fibers, density of the hollow fibers becomes high in the vicinity of the nozzles, so that it has been hard to deliver the scrubbing-use air appropriately to the hollow fibers.
Therefore, the object of the invention is to provide: a hollow fiber bundle, a method of manufacturing the hollow fiber bundle, a cylindrical module of hollow fiber membrane, and an immersion type module of hollow fiber membrane wherein specified intervals are maintained among the hollow fibers and scrubbing is easy to carry out even if nozzles or the like are formed in the pottings.
As shown in
the hollow fibers 10 that are open at one side end and closed at the other side end;
a closed side potting 60 plate-shaped at right angle to the hollow fibers 10 for securing the hollow fibers 10 on the closed end 14 side (See
an open side potting 50 plate-shaped at right angle to the hollow fibers 10 for securing the hollow fibers on the open end 12 side, wherein
through holes 30 disposed on a circumference and penetrating in the direction of thickness of the plate shape are formed in the closed side potting,
the hollow fibers are bundled in a cylindrical shape inside the through holes 30 disposed on the circumference, wherein the hollow fibers 10 are disposed with a specified circumferential interval c1 adjacent each other in a circumferential direction and with a specified radial interval r1 adjacent each other in a radial direction, and
the hollow fibers 10 are bundled outside the through holes 30 disposed on the circumference in a shape surrounding the through holes 30 disposed on the circumference wherein the hollow fibers 10 are disposed with a specified peripheral interval c2 adjacent each other in a peripheral direction in the shape surrounding the outside of the through holes and with a specified peripheral right angle interval r2 adjacent each other in a right angle to the periphery.
With the above constitution, as the hollow fibers are disposed with specified intervals maintained around the through holes, scrubbing is easy to carry out.
The specified circumferential interval may be equal to the specified peripheral interval, and the specified radial interval may be equal to the specified peripheral right angle interval.
As shown in
With the above constitution, when scrubbing air is delivered out of the through holes, delivery of scrubbing air becomes more even, so that it becomes easy to supply scrubbing air appropriately around the hollow fibers.
As shown in
With the above constitution, delivery of scrubbing air becomes more even when scrubbing air is delivered out of the through holes, so that it becomes easy to supply scrubbing air appropriately around the hollow fibers.
As shown in
With the above constitution, as the insert member to which the hollow fibers are not secured is inserted in a position on the open side potting opposite of the through hole to which the hollow fibers are not secured in the closed side potting, and the hollow fibers are disposed parallel, scrubbing air flows easily among the hollow fibers.
As shown in
With the above constitution, the hollow fibers are not necessarily parallel any more, scrubbing air passages are less easy to be formed in the intervals among the hollow fibers, so that scrubbing air weaves its way up through the hollow fibers. Therefore, scrubbing the hollow fibers with scrubbing air is carried out more effectively.
As shown in
With the above constitution, as the numbers of hollow fibers inside and outside the through holes disposed on the circumference become appropriate, it becomes easy to supply scrubbing air around all the hollow fibers.
As shown in
With the above constitution, as the through holes are also formed outside the through holes disposed on the circumference, it is possible to supply scrubbing air appropriately around the hollow fibers even if the number of hollow fibers increases and the hollow fiber bundle becomes large-sized.
As shown in
With the above constitution, as scrubbing air may be also supplied from outside the hollow fibers, it reaches the entire hollow fibers more easily.
As for a hollow fiber bundle of the invention, in the hollow fiber bundle as described before the filling rate of the hollow fibers bundled in the cylindrical shape and the hollow fibers bundled in the shape surrounding the through holes may be between 50% and 70%.
Incidentally, the term ‘filling rate’ is all value expressed in percentage of the area taken up with the hollow fibers (cross-sectional area per single hollow fiber multiplied by the number of hollow fibers included in a specified cross-sectional area) to a specified cross-sectional area at right angles to the hollow fibers (cross-sectional area excluding the through holes and the space between the hollow fibers and the casing).
The above constitution makes it possible to take a large filtering area relative to the same cross-sectional area while maintaining intervals among the hollow fibers.
As shown in
forming a screen-like object 20 made of porous follow fibers 10 disposed parallel at approximately even intervals with both ends of the hollow fibers respectively secured with tapes 22;
sealing one side ends 11 of the hollow fibers 10;
winding the screen-like object 20 in a cylindrical shape so as to bundle the hollow fibers 10;
disposing a member forming through hole 32 shorter than the hollow fibers 10 at the periphery of the screen-like object 20 wound in a cylindrical shape in the step of winding on the side opposite 14 on which the sealing is made;
winding up further the screen-like object 20 including the members forming through hole 32;
forming pottings 50, 60 for respectively and integrally securing both ends of the screen-like object 20 wound up while including the members forming through hole in the step of winding up further; and cutting the potting 50 together with the hollow fibers 10 along a plane at right angle to the hollow fibers 10 to open the hollow fibers by cutting off the sealed end 11.
The above constitution makes it possible to dispose the follow fibers parallel at approximately even intervals and as the screen-like object made of hollow fibers with its both ends respectively tied together using tapes is wound up so as to bundle hollow fibers, the hollow fibers are bundled while parallel-disposed intervals are maintained in the direction of winding up the hollow fibers (circumferential direction) and tape thickness intervals are maintained in the overlapping direction (radial direction). The members forming through hole shorter than the hollow fibers are disposed in the process of winding up the screen-like object of hollow fibers, both ends of the wound-up screen-like object of hollow fibers are integrally secured respectively, and the through holes are formed by the members forming through hole or by the removal of the members forming through hole from the secured end. Thus, as the hollow fibers are disposed while specified intervals are maintained around the through holes when scrubbing air is delivered out of the through holes formed in the potting, it is possible to supply scrubbing air for cleaning the outer surfaces the hollow fibers appropriately around the hollow fibers.
As shown in
With the above constitution, as the through holes for delivering scrubbing air are disposed on the circumference, delivery of scrubbing air becomes even and it becomes easy to appropriately supply scrubbing air around the hollow fibers.
As shown in
disposing an insert member 34 shorter than the hollow fibers 10 in the sealed end 11 at a periphery, where the member forming through hole 32 is disposed, of the screen-like object 20 wound in a cylindrical shape in the step of disposing the member forming through hole 32.
The above constitution makes it possible to dispose the insert member in a position just corresponding to the member forming through hole and the hollow fibers are disposed parallel, so that the screen-like object of hollow fibers becomes easy to wind up. While the insert member 34 is typically disposed in a position just corresponding to the member forming through hole 32, for example one may be disposed more outside by one turn or several turns. This also falls within the category of the corresponding position.
As shown in
the hollow fiber bundle 1 as described before;
an oblong casing 70 containing the hollow fiber bundle 1;
a nozzle 76 connected to the casing 70 on the closed end of the hollow fiber bundle 1;
a nozzle 77 connected to the casing 70 on the open end of the hollow fiber bundle 1; and
nozzles 78, 79 connected to the part of the casing 70 between the open side potting 50 and the closed side potting 60.
With the above constitution, as the liquid to be filtered introduced between the open side potting and the closed side potting may be filtered with the hollow fibers and the filtered liquid may be collected with the open end nozzle. As the hollow fibers around the through holes are disposed while specified intervals are maintained in the cylindrical module of hollow fiber membrane, liquid to be filtered flows easily and scrubbing is easy to carry out.
As shown in
the hollow fiber bundle 1 as described before;
an air header 80 in communication with the through holes 30 of the hollow fiber bundle 1; and
a filtered liquid header 90 in communication with the open ends 12 of the hollow fiber bundle 1, and
constituted to be immersible in liquid to be filtered.
With the above constitution, as scrubbing air is delivered through the air header out of the through holes and the hollow fibers are disposed while specified intervals are maintained around the through holes in the immersion type module of hollow fiber membrane, liquid to be filtered flows easily and scrubbing is easy to carry out.
According to the invention, the hollow fiber bundle includes: the hollow fibers that are open at one side ends and closed at the other side ends; a closed side potting plate-shaped at right angles to the hollow fibers for securing the hollow fibers on the closed end side; and an open side potting plate-shaped at right angles to the hollow fibers for securing the hollow fibers on the open end side, in which the closed side potting is formed with through holes disposed on a circumference and penetrating in the plate thickness direction of the plate shape, the hollow fibers are bundled in a cylindrical shape inside the through holes disposed on the circumference and disposed at specified circumferential intervals between one hollow fiber and circumferentially adjacent another hollow fiber and at specified radial intervals between one hollow fiber and radially adjacent another hollow fiber, the hollow fibers are bundled outside the through holes disposed on the circumference in a shape surrounding the through holes disposed on the circumference and disposed at specified peripheral intervals between one hollow fiber and peripherally adjacent another hollow fiber and at specified peripheral right angle intervals between one hollow fiber and another hollow fiber adjacent in the direction at right angles to the periphery. Therefore, the hollow fibers are disposed while specified intervals are maintained around the through holes, so that scrubbing is easy to carry out.
As the screen-like object made of hollow fibers, in which hallow fibers are disposed parallel at approximately even intervals with both ends respectively tied together using tapes, is wound up so as to bundle hollow fibers, the hollow fibers are bundled while parallel-disposed intervals are maintained in the direction of winding up the hollow fibers (circumferential direction) and tape thickness intervals are maintained in the overlapping direction (radial direction). Further in the process of bundling the hollow fibers and, winding up the screen-like object made of hollow fibers, as the members forming through hole shorter than the hollow fibers are disposed and both ends of the wound-up screen-like object made of hollow fibers are respectively secured integrally, the through holes for delivering scrubbing air are formed by the members forming through hole or by the removal of the members forming through hole from the secured ends. Therefore, it is possible to easily manufacture the hollow fiber bundle in which the hollow fibers are disposed while specified intervals are maintained around the through holes.
When the hollow fiber bundle described above is used in the cylindrical module of hollow fiber membrane, as the hollow fibers around the through holes are placed while specified intervals are maintained, it is easy to filter liquid to be filtered and to carry out scrubbing. When the hollow fiber bundle described above is used in the immersion type module of hollow fiber membrane, as the hollow fibers around the through holes are placed while specified intervals are maintained, liquid to be filtered flows easily and scrubbing is easy to carry out.
This application is based on the Patent Applications No. 2005-287096 filed on Sep. 30, 2005 in Japan, the contents of which are hereby incorporated in its entirety by reference into the present application, as part thereof.
The present invention will become more fully understood from the detailed description given herein below. However, the detailed description and the specific embodiment are illustrated of desired embodiments of the present invention and are described only for the purpose of explanation. Various changes and modifications will be apparent to those ordinary skilled in the art on the basis of the detailed description.
The applicant has no intention to give to public any disclosed embodiment. Among the disclosed changes and modifications, those which may not literally fall within the scope of the patent claims constitute, therefore, a part of the present invention in the sense of doctrine of equivalents.
Embodiments of the present invention are described below in reference to appended drawings. In the drawings, the same parts or counterparts are provided with the same reference numerals and symbols, omitting redundant explanations.
First in reference to
Each of the hollow fibers 10 is a hollow fiber made of a porous material. In the hollow fiber 10, a hollow space extends through the center in the longitudinal direction. The outside diameter of the hollow fiber 10 is in the order of for example 1 to 3 millimeters, and the thickness of the membrane making up the hollow fiber is in the order of 10 to 500 micrometers. The hollow fiber 10 is typically made of resin material having resistance against water and chemicals. The term ‘resistance against chemicals’ as used herein means the resistance against chemicals mixed in liquid to be filtered when the hollow fiber bundle 1 is used, and includes resistance against chemicals added when cleaning solid matter accumulated on the surface of the hollow fibers 10. The hollow fiber 10 is preferably made of resin material derived from vinylidene fluoride. Resin material derived from vinylidene fluoride is excellent in heat resistance and mechanical strength in addition to chemical resistance. As resin materials derived from vinylidene fluoride, such ones may be used as: homopolymer of vinylidene fluoride, namely polyvinylidene fluorine, copolymer with other monomer capable of copolymerizing, or mixture of these. As the monomer capable of copolymerizing with resin materials derived from vinylidene fluoride, one kind or more than one kind may be used out of such ones as: Tetrafluoroethylene, propylene hex a fluoride, Trifluoroethylene, Trifluorochloroethylene, and vinyl fluoride. The resin material derived from vinylidene fluoride preferably contain 70 mol % or more of vinylidene fluoride and further preferably be a homopolymer made of 100 mol % of vinylidene fluoride because it is high in both resistance against chemicals and mechanical strength.
The hollow fiber 10 may be manufactured by adding 100 to 300 weight parts in total amount of plasticizer and good solvent of vinylidene fluoride resin to 100 weight parts of resin derived from vinylidene fluoride so that the percentage of good solvent in the total amount of plasticizer and good solvent is 8 to 35 weight %, then extrusion forming, and extracting plasticizer and good solvent with extraction liquid. Further in order to increase the degree of crystallization, it is preferable to apply heat treatment for example at temperatures of 100 to 140 degrees C. for 3 to 900 seconds, followed by uniaxial extension, in a longitudinal direction. The uniaxial extension increases pore rate and pore diameter and improves tensile strength and ultimate elongation, and linearity. Uniaxially extended hollow fiber of vinylidene fluoride-based resin exhibits, as an example, pore rate of 60 to 85%, average pore diameter of 0.05 to 0.15 micrometers, tensile strength of 5 MPa and greater, and ultimate elongation at fracture of 5% and greater.
The hollow fibers 10 are open at their one side ends, and closed at the other side ends.
The closed side potting 60 on the closed end side of the hollow fibers 10 is a disk at right angles to the hollow fibers 10 and made of hard resin material to secure the end of the hollow fibers 10. As the hard resin material, while such ones are used as urethane-based resin and epoxy-based resin, urethane-based resins producing less heat during solidification are favorably used. The closed side potting 60 is formed with through holes 30 and 30′ of the circular cross section passing through the thickness of the disk. One through hole 30′ is located in the center of the closed side potting 60 and the through holes 30 are located at even intervals on the circumference centered on the center of the closed side potting 60. Incidentally, the shape of the cross section of the through holes 30 and 30′ may be of any other shape than circle; such as polygon, ellipse, arcuate slit, etc.
The open side potting 50 on the open end 12 side of the hollow fibers 10 is a disk at right angles to the hollow fibers, made of hard resin material, and the same as the closed side potting 60 in both shape and size, and secures the ends of the hollow fibers 10. The open side potting 50 is usually made of the same material as the closed side potting 60. However, they may be formed respectively different in shape, size, and material. The hollow fibers 10 pass through the open side potting 50 and open on the surface (upper surface in
The hollow fibers 10 are positioned as their both ends are secured with the closed side potting 60 and the open side potting 50. The hollow fibers 10 are disposed parallel, with their intervals maintained at specified intervals. To explain in detail on the surface of the closed side potting 60, the hollow fibers 10 are disposed on a concentric circle around the central through hole 30′ inside the through holes 30 disposed on the circumference. To see it more closely, the hollow fibers 10 are disposed not circularly but spirally. However, as the lead by one turn of the spiral is smaller in comparison with the size of the spiral, when an imaginary circle is assumed by neglecting the lead, a shape concentric with the imaginary shape also falls within the category of the concentric circle. Incidentally, also for the circumference on which the through holes 30 are disposed, a spiral having likewise slight lead is included in the imaginary circle neglecting the lead. On this concentric circle (strictly speaking, approximate concentric circle), the hollow fibers 10 are disposed with their circumferential interval c1 set as a specified circumferential interval. They are also disposed with their radial interval r1 set as a specified radial interval. Incidentally, the circumferential interval and the radial interval may or may not be the same. Here, the radial interval r1 is the interval between adjacent hollow fibers 10 on the concentric circle. When the hollow fibers 10 are disposed in the spiral shape as described above, the radial interval r1 is the interval between hollow fibers 10 produced with the lead of the spiral. The hollow fibers 10 are disposed on a concentric circle inside the through holes 30 disposed on the circumference, or bundled in a cylindrical shape. Incidentally, also in the case that the through hole 30′ is not formed in the center of the closed side potting 60 and the hollow fibers 10 are disposed from the center, because an imaginary circle on the innermost side of the concentric circle is assumed, it should be considered to be included in the category of being bundled in a cylindrical shape assuming a space within the imaginary circle.
The hollow fibers 10 are disposed in a shape surrounding the through holes 30 disposed on a circumference. Here, the term ‘a shape surrounding the through holes 30 disposed on a circumference’ means the shape that includes all the through holes 30 in it and that circumscribes the through holes 30. One through hole 30 may be connected to another with a straight line. A circle may circumscribe all the through holes 30. Or, even a shape being inside the straight line connecting the through hole 30 to another will do, as long as it is a shape of bundled hollow fibers 10 that is discriminated from that of a bundle inside the through holes 30. In
The specified circumferential and radial intervals and specified peripheral interval and peripheral right angle interval may be given by range; and the interval is such that permits filtered liquid to flow among the hollow fibers 10 and that scrubbing air is sent appropriately among the hollow fibers 10 even if solid matter accumulates to a certain extent on the hollow fibers 10. Setting the filling rate of the hollow fibers 10 to 50 to 70% makes it possible to take a large filtering area relative to the same cross-sectional area and makes it easy to appropriately supply scrubbing air around the hollow fibers while the filtered liquid flows through the intervals among the hollow fibers 10. As an example, for the hollow fibers 10 of an outside diameter of 1.3 mm, the specified circumferential interval c1 is set to about 0.2 to 0.7 mm (center to center interval of the hollow fibers 10 of about 1.5 to 2.0 mm), and the specified radial interval r1 is set to about 0.05 to 0.15 mm.
As the hollow fiber 10 in the hollow fiber bundle 1 constituted as described above is high in both linearity and mechanical strength, the closed side potting 60 and the open side potting 50 are securely supported so that the hollow fibers 10 are in a taut state. The liquid to be filtered is collected from the outside surface of the hollow fibers 10 through the inside (hollow part) of the hollow fibers on the open end 12 side by pressurizing the liquid to be filtered or by suctioning it from the open end 12 side. At this time, as the hollow fibers 10 are disposed with high linearity and at specified intervals, liquid to be filtered flows easily among the hollow fibers 10.
The liquid to be filtered is filtered through the porous membrane of the hollow fibers 10 when the liquid enters the inside of the hollow fibers 10. In other words, liquid flowing through the inside of the hollow fibers 10 is already filtered clean. By filtering, solid matter accumulates on the outside surface of the hollow fibers 10.
When the hollow fibers 10 are set up in the taut state, frequency of vibration of the hollow fibers increases when scrubbing is carried out, so that fine sediment is easy to remove.
Incidentally, the hollow fibers 10 may also be set up in a slack state. When the hollow fibers 10 are set up in the slack state, the hollow fibers oscillate largely, so that coarse sediment is easy to remove. Here, the slack state means a state in which the length of the hollow fibers 10 is made longer by 3 to 5%, for example, than the distance between the open side potting 50 and the closed side potting 60. In this case, it is said that the slack rate is 3 to 5%.
When solid matter accumulates on the outside surface, the filtering area of the hollow fibers 10 decreases and so the filtering efficiency decreases. Therefore, it is necessary to remove the solid matter on the hollow fibers 10 by cleaning. To carry out the cleaning, scrubbing air is delivered out of the through holes 30 and 30′ of the closed side potting 60 so as to peel the solid matter off the hollow fibers 10 with upward movement of scrubbing air and by simultaneously occurring vibration (thought to be included in the scrubbing effect) of the hollow fibers 10 themselves. At this time, as the hollow fibers 10 are disposed around the through holes 30 and 30′ while specified intervals are maintained, scrubbing air is supplied appropriately to the hollow fibers 10. In other words, scrubbing air is supplied around or at least near all the hollow fibers 10, so that solid matter accumulated on the outside surface of the hollow fibers 10 is peeled off. In particular when the ratio of the number of hollow fibers 10 inside the through holes 30 disposed on the circumference to the number of hollow fibers 10 disposed outside is set to about 0.2 to 5, it is possible to favorably supply scrubbing air to both inside and outside. Outside that range, scrubbing air may not be distributed evenly to the hollow fibers 10. Incidentally, the ratio is preferably set between 0.5 and 4, more preferably between 0.8 and 3.
As shown in
Next, in reference to
Next, as shown in
When the screen-like object 20 of hollow fibers is wound up in an appropriate number of layers, the members forming through hole 32 are placed around the wound-up screen-like object 20 of hollow fibers. The member forming through hole 32 is formed in the same manner as the member forming through hole 32′. The members forming through hole 32 (four in
As shown in
Now in reference to
Referring back to
The hollow fibers 10 are tied together using the tape 22 while leaving small intervals. The small intervals are maintained even after the winding up is over to leave the circumferential interval c1 or the peripheral interval c2. In other words, when the hollow fiber 10 is wound on the drum 24 (See
As described above, the screen-like object 20 of hollow fibers in which hollow fibers are disposed at approximately even intervals, and both ends of the hollow fibers are tied together respectively using the tapes is, manufactured by winding the hollow fiber 10 around the drum 24 with specified circumferential intervals between turns, tying together with two tapes 22 of a thickness of a specified radial interval or a specified peripheral right angle interval, and cutting the hollow fibers 10 between the two tapes 22. When the screen-like object 20 of hollow fibers is wound, both the member forming through hole 32 and the insert member 34 are placed in positions, and further the screen-like object 20 are wound up as explained with
As shown in
As shown in
When the open side potting 50 and the closed side potting 60 are formed, as the raw materials for the potting materials 52 and 62, or for the protective layers 54 and 64, liquid resins of low viscosity are often used so as to enter among the hollow fibers. Then, due to capillary phenomenon that can occur when the intervals among the hollow fibers 10 are small, the liquid resin sometimes infiltrates up the intervals among the hollow fibers 10. When the upward infiltration occurs in the potting materials 52 and 62, it detracts from the effect of the protective layers 54 and 64. If the upward infiltration occurs in the protective layers 54 and 64, it results in the decrease in the filtering area of the hollow fibers 10. When the specified intervals are maintained among the hollow fibers 10, it is possible to restrict the upward infiltration by this capillary phenomenon.
Next, in reference to
Two more nozzles are connected to the casing 70: a lower side nozzle 78 and an upper side nozzle 79 are connected to the trunk plate 72 of the middle portion 71a. The lower side nozzle 78 and the upper side nozzle 79 are preferably connected respectively to the vicinities of the closed side potting 60 and the open side potting 50.
With the cylindrical module 100 of hollow fiber membrane, liquid to be filtered is introduced through the liquid supply nozzle 76 into the casing 70. Here, the liquid to be filtered is, for example, water to be cleaned, typically with turbidity substances and bacteria floating. The liquid to be filtered is supplied through piping connected to the liquid supply nozzle 76. The liquid to be filtered is first introduced into the entry portion 71b. There, it passes through the through holes 30 and 30′ to enter the middle portion 71a.
The liquid to be filtered finding its way into the middle portion 71a is filtered with the hollow fibers 10 disposed in the middle portion 71a, and enters the hollow spaces in the hollow fibers 10. Here, as the hollow fibers 10 are disposed with their specified intervals maintained, the liquid to be filtered flows easily to all the hollow fibers 10. The filtered liquid entering the hollow spaces in the hollow fibers 10 is introduced from the open end 12 (See
The liquid to be filtered, when part of it is filtered with the hollow fibers 10, increases in concentration. The liquid of increased concentration is discharged from the lower side nozzle 78 or upper side nozzle 79, and succeeding liquid to be filtered is introduced. Arranging the discharge out of the upper side nozzle 79 is particularly preferable, so that succeeding liquid to be filtered prevails in the middle portion 71a.
As the liquid to be filtered is filtered with the hollow fibers 10, solid matter accumulates on the outside surfaces of the hollow fibers 10. Therefore, scrubbing air is supplied through the liquid supply nozzle 76 to the entry portion 71b. To supply scrubbing air, either one of the followings is possible: to connect a scrubbing air transport pipe to a pipe connected to the liquid supply nozzle 76, to employ double piping in which a scrubbing air transport pipe is placed inside a pipe connected to the liquid supply nozzle 76, or to provide a scrubbing air supply nozzle separately from the liquid supply nozzle 76 to deliver scrubbing air. The scrubbing air introduced into the entry portion 71b is delivered through the through holes 30 and 30′ to the middle portion 71a.
The scrubbing air delivered to the middle portion 71a rises through the liquid in the middle portion 71a. As described before, because the hollow fibers 10 are disposed at specified intervals around the through holes 30 and 30′, scrubbing air appropriately flows to all over the hollow fibers 10. The solid matter that has accumulated on the outside surface of the hollow fibers 10 is peeled off by the scrubbing action accompanying the rise of the scrubbing air. Most of the solid matter that has peeled off falls toward the bottom of the middle portion 71a and discharged together with the liquid discharged from the lower side nozzle 78 out of the casing 70.
The cylindrical module 100 of hollow fiber membrane may be alternatively constituted that liquid to be filtered is supplied through one of the lower side nozzle 78 and the upper side nozzle 79, and discharged through the other. In the cylindrical module 100 of hollow fiber membrane, the liquid supply nozzle 76 is exclusively used to supply scrubbing air to the entry portion 71b.
Next, in reference to
The immersion type module 101 of hollow fiber membrane further includes: a connecting pipe 84 connected to the air header 80, an air supply pipe 86 connected to the connecting pipe 84, a connecting pipe 94 connected to the filtered liquid header 90, and a filtered liquid pipe 96 connected to the connecting pipe 94. The air header 80 is securely supported with both the air supply pipe 86 and the connecting pipe 84; the filtered liquid header 90 is securely supported with both the filtered liquid pipe 96 and the connecting pipe 94. As the air header 80 and the filtered liquid header 90 are securely supported, the hollow fiber bundle 1 is maintained in the state in which the hollow fibers 10 maintain linearity or the rate of slackness. With the hollow fiber bundle 1 or the hollow fiber bundle 2, and the air header 80 and the filtered liquid header 90 supported as described above, the module is immersed in the liquid to be filtered. While the immersion type module 101 of hollow fiber membrane is immersed in water to be cleaned held typically in a water tank (not shown), it may be immersed directly in a river if the water to be cleaned is for example river water.
The filtered liquid pipe 96 is connected to the upstream side of a pump (not shown) and the filtered liquid is suctioned with the pump. As the filtered liquid is suctioned, liquid to be filtered is filtered with the hollow fibers 10 and flows from the hollow spaces of the hollow fibers 10, through the open end 12 (See
The scrubbing air delivered into the liquid to be filtered rises through the liquid to be filtered. As described before, because the hollow fibers 10 are disposed while specified intervals are maintained around the through holes 30 and 30′, scrubbing air reaches appropriately to all the hollow fibers 10. The solid matter that has accumulated on the outside surface of the hollow fibers 10 is peeled off by the scrubbing action accompanying the rise of the scrubbing air. The peeled solid matter is removed from the liquid to be filtered as it settles down on the bottom of the water tank, or as it is washed away in the river.
While
While the figures heretofore show that four through holes 30 are formed and the hollow fibers 10 are bundled concentrically, the number of through holes 30 may be changed as shown in
As shown in
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
Number | Date | Country | Kind |
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2005-287096 | Sep 2005 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/JP2006/318424 | 9/15/2006 | WO | 00 | 8/20/2008 |