CN115475531A - Separation membrane module unit - Google Patents

Separation membrane module unit Download PDF

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Publication number
CN115475531A
CN115475531A CN202110603093.7A CN202110603093A CN115475531A CN 115475531 A CN115475531 A CN 115475531A CN 202110603093 A CN202110603093 A CN 202110603093A CN 115475531 A CN115475531 A CN 115475531A
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CN
China
Prior art keywords
separation membrane
membrane module
frame
fixing frame
shape
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Pending
Application number
CN202110603093.7A
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Chinese (zh)
Inventor
金成镇
宋成焕
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Sany Enc
Original Assignee
Sany Enc
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Publication date
Application filed by Sany Enc filed Critical Sany Enc
Priority to CN202110603093.7A priority Critical patent/CN115475531A/en
Publication of CN115475531A publication Critical patent/CN115475531A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/04Hollow fibre modules comprising multiple hollow fibre assemblies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/04Backflushing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/18Use of gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/007Modular design
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

The present invention relates to a separation membrane module unit, which can uniformly wash the whole of the outer side and the inner side of a hollow fiber membrane bundle of a separation membrane module by including a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame and a diffuser, thereby increasing the effective washing area, improving the performance of the separation membrane module and remarkably increasing the service life of the separation membrane module, and enabling a user to selectively and conveniently additionally install a plurality of separation membrane unit modules formed in a unit form for use according to the filtration capacity.

Description

Separation membrane module unit
Technical Field
The present invention relates to a separation membrane module unit, and more particularly, to a separation membrane module unit which includes a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame, and a diffuser, and which can uniformly wash the entire outer and inner sides of a hollow fiber membrane bundle of the separation membrane module, thereby increasing an effective washing area, and thus increasing the performance of the separation membrane module while remarkably increasing the lifespan of the separation membrane module, and which can allow a user to selectively and conveniently additionally install a plurality of separation membrane unit modules in a unit form according to filtration capacity.
Background
In general, a separation membrane module, which is an immersion type filtration apparatus, is installed inside a reaction tank, and sewage and wastewater can be filtered by using water permeability of the separation membrane module, and in order to increase water permeability of the separation membrane module, it is necessary to remove impurities attached to the separation membrane module at a certain period by means of, for example, a cross-flow filtration method, a reverse washing method, an air washing method, or the like.
As an immersion type filtration apparatus using the above-described separation membrane module (hollow fiber membrane module), there is disclosed an immersion type filtration apparatus including a plurality of hollow fiber membrane modules, a filtrate capturing and transferring block for supporting the upper ends of the hollow fiber membrane modules, an air injecting and transferring block provided with an air injection port for supporting the lower ends of the hollow fiber membrane modules, and a mesh filter, see patent document 1 (korean registered patent No. 0646001, 2006.11.07 registration).
However, in the immersion type filtration apparatus using the conventional separation membrane module (hollow fiber membrane module), since the washing air is brought into contact with only the surface of the separation membrane module exposed to the outside and cannot wash the separation membrane located inside, the entire separation membrane module cannot be uniformly washed, which leads to a problem that the effective area for washing the separation membrane is reduced and the life of the separation membrane module is further shortened.
In addition, in the immersion type filtration apparatus using the conventional separation membrane module (hollow fiber membrane module), since the same amount of air cannot be injected into each separation membrane module, the air cleaning effect differs at different portions from one another in the entire filtration apparatus, and sludge accumulates in portions where air cleaning is insufficient, thereby causing a problem of further rapid decrease in performance of the separation membrane.
Further, in the immersion type filtration apparatus using the conventional separation membrane module (hollow fiber membrane module), since the separation membrane module is manufactured in advance to have a specific filtration capacity, a user cannot selectively adjust the filtration capacity according to the filtration required from a small-scale capacity to a large-scale capacity.
Therefore, there is a need for research and development of a separation membrane unit module for a filtration apparatus, which includes a structure in which the entire outside and inside of a hollow fiber membrane portion to which a bundle-shaped form is applied in a separation membrane module can be uniformly washed, thereby increasing an effective washing area, thereby improving the performance of the separation membrane module and remarkably increasing the lifespan of the separation membrane module, and also allowing a user to selectively and conveniently additionally install a plurality of separation membrane modules configured in a unit form according to filtration capacity.
Documents of the prior art
Patent literature
(patent document 0001) korean registered patent No. 0646001, 2006.11.07.
(patent document 0002) korean registered patent No. 0552712, 2006.02.20.
(patent document 0003) korean registration No. 1070383, 2011.09.28.
(patent document 0004) korean registered patent No. 1402197, 2014.05.26.
Disclosure of Invention
Technical problem to be solved
In order to solve the above problems, it is an object of the present invention to provide a separation membrane unit module which includes a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame, and a diffuser, and can uniformly wash the entire outer and inner sides of a hollow fiber membrane bundle of the separation membrane module, thereby increasing an effective washing area.
Another object to which the technology of the present invention is applied is to uniformly wash the entire outer and inner sides of a hollow fiber membrane bundle of a separation membrane module by using a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame, and a diffuser pipe, thereby increasing an effective washing area and thereby remarkably increasing the service life of the separation membrane module while enhancing the performance of the separation membrane module.
Another object of the present invention is to provide a reactor including a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame, and a diffuser, in which a plurality of separation membrane unit modules configured in a unit form can be selectively and conveniently attached to a user according to the filtration capacity of a reaction tank.
Still another object of the technology to which the present invention is applied is to conveniently maintain and manage a separation membrane module by realizing modularization and thereby conveniently separating the separation membrane module installed on a support frame and performing washing treatment by means of reverse washing, etc., by including the separation membrane module, the support frame, a vertical fixing frame, an external fixing frame, and a diffuser pipe.
(II) technical scheme
The present invention for achieving the above object is as follows. That is, the separation membrane module unit to which the present invention is applied, as a separation membrane module unit which is installed and fixed inside a reaction tank to filter sewage and wastewater, includes: a separation membrane module, the upper end of which is connected with the suction pump through a pipeline, a hollow fiber membrane bundle formed by a plurality of hollow fiber membrane bundles is arranged at the center in the vertical direction, and the water washed upwards from the lower side of the outside of the hollow fiber membrane through the inside can flow out of the reaction tank by the driving of the suction pump; a support frame formed in a frame shape having a through hole formed at the center thereof, on which the lower end of the separation membrane module is seated and mounted; a plurality of vertical fixing frames formed in a vertical frame shape having a certain length, fixedly installed through fixing members at certain intervals along the outer circumference of the supporting frame, and allowing the supporting frame to be fixedly installed in a state of being spaced a certain distance upward from the lower end; an external fixing frame fixedly installed at the lower end, the center and the upper end of the vertical fixing frame through fixing components in a manner of respectively surrounding the vertical fixing frame, and installed on the bottom surface of the reaction tank or fixedly installed on the vertical side wall; and an air diffusing pipe which is composed of a main body which is formed with a plurality of through holes on the upper side surface and is configured on the lower side of the supporting frame for diffusing air bubbles, and a connecting pipe which is formed by bending and extending from the lower side of the main body for a plurality of times in a mutually communicated mode and extending in a mode of sequentially penetrating through the external fixing frames which are arranged on the central part and the upper end part of the vertical fixing frame, wherein the extending end part of the connecting pipe is connected with the air blower through a pipeline, and the air bubbles are diffused upwards from the lower side of the supporting frame by the driving of the air blower, thereby the external surface of the hollow fiber membrane of the separation membrane module is washed.
In this case, the separation membrane module includes: a hollow fiber membrane bundle composed of a plurality of hollow fiber membrane bundles; a lower cover which is opened at the upper and lower parts and is formed in a columnar shape with a placing plate formed at the center, the lower end of the hollow fiber membrane bundle is fixedly installed in a mode of upward spacing a certain distance from the placing plate, a plurality of communication holes are formed on the placing plate in a penetrating way, and the peripheral part of the lower end is placed on the supporting frame; and an upper cover formed in a cylindrical shape with a lower portion opened and a connection port formed at the center of the closed upper side surface in a protruding manner, wherein the upper end of the hollow fiber membrane bundle is fixedly installed in a manner of downward spacing a certain distance from the inner upper side surface; it is preferable.
The separation membrane module may be formed in a rectangular column shape, the support frame may be formed in a square frame shape having an "l" shaped cross section, the vertical fixing frame may be formed in an angular shape having an "l" shaped cross section when viewed in plan view so as to be in close contact with each corner portion of the support frame, the external fixing frame may be formed in a square frame shape having an "l" shaped cross section, and may be fixedly attached to the lower end, the center, and the upper end portions of the vertical fixing frame by fixing members so as to surround the vertical fixing frame, and the external fixing frame disposed at the lower end portion of the vertical fixing frame may be fixedly attached to the l "shape in which the" l "shape is inverted up and down.
Further, the outer fixing frame is preferably formed in a square frame shape having a "l" shape or a "l" shape in cross section, and is preferably formed in a square frame shape in which four portions of corner portions are cut out so that oblique lines are closely attached to each other when viewed in plan view of the end portions facing each other.
The separation membrane module may be formed in a cylindrical shape, the support frame may be formed in a circular frame shape having a "l" shaped cross section, the vertical fixing frame may be formed in a rod shape having a curved arc-shaped cross section when viewed in a plane so as to be attached along a periphery of the support frame, the external fixing frame may be formed in a circular frame shape having a "cross-shaped" cross section, and may be fixedly attached to a lower end, a center, and an upper end portion of the vertical fixing frame by fixing members so as to surround the vertical fixing frame, and the external fixing frame disposed at a lower end portion of the vertical fixing frame may be fixedly attached to the l-shaped frame shape in which the "l" shape is inverted up and down.
(III) advantageous effects
Next, the effects of applying the separation membrane module unit of the present invention will be explained.
First, the outside and inside of the hollow fiber membrane bundle of the separation membrane module can be washed uniformly by including the separation membrane module, the support frame, the vertical fixing frame, the external fixing frame, and the diffuser pipe, thereby increasing an effective washing area.
Second, the outside and inside of the hollow fiber membrane bundle of the separation membrane module can be washed uniformly by using the separation membrane module, the support frame, the vertical fixing frame, the external fixing frame, and the diffuser pipe, thereby increasing the effective washing area and thereby remarkably increasing the service life of the separation membrane module while enhancing the performance of the separation membrane module.
Thirdly, the present invention can allow a user to selectively and conveniently additionally install a plurality of separation membrane unit modules in a unit form according to the filtration capacity of the reaction tank to use the separation membrane unit modules by including the separation membrane module, the support frame, the vertical fixing frame, the external fixing frame, and the air diffusion pipe.
Fourthly, through including separation membrane module, braced frame, vertical fixation frame, outside fixed frame and gas dispersion pipe, can realize the modularization and borrow this conveniently to separate the separation membrane module of installation setting on braced frame and carry out washing processing through modes such as reverse washing to conveniently maintain the management to the separation membrane module.
Drawings
FIG. 1 is a perspective view showing a separation membrane module unit to which the present invention is applied.
FIG. 2 is a schematic perspective view of a separation membrane module unit to which the present invention is applied. Fig. 3 is a combined cross-sectional view illustrating a separation membrane module unit to which the present invention is applied.
Fig. 4 is a main part separation perspective view showing a separation membrane module, which is a main part of a separation membrane module unit to which the present invention is applied.
Fig. 5 is a perspective view showing a fixing structure of a support frame, a vertical fixing frame, and an external fixing frame, which are main parts of a separation membrane module unit to which the present invention is applied.
Fig. 6 is a sectional view showing a use state of a separation membrane module unit to which the present invention is applied.
FIG. 7 is a perspective view showing a separation membrane module unit to which another embodiment of the present invention is applied.
Description of the reference numerals
1000: separation membrane module unit 100: separation membrane module
110: hollow fiber membrane bundle 111: hollow fiber membrane
130: lower cover 131: placement plate
131a: communication hole 150: upper cover
151: connection port 200: support frame
210: through hole 300: vertical fixing frame
400: external fixing frame 500: air diffusing pipe
510: main body 520: connecting pipe
B: and (4) a bolt N: nut
10: suction pump 10a: suction connecting pipe
20: blower 20a: connecting pipeline for air supply
Detailed Description
Next, preferred embodiments of a separation membrane module unit to which the present invention is applied will be described in detail with reference to the accompanying drawings.
Fig. 1 is a separation perspective view showing a separation membrane module unit to which the present invention is applied, fig. 2 is a coupling perspective view showing a separation membrane module unit to which the present invention is applied, and fig. 3 is a coupling sectional view showing a separation membrane module unit to which the present invention is applied.
Fig. 4 is a main portion separation perspective view showing a separation membrane module, which is a main portion of a separation membrane module unit to which the present invention is applied.
Fig. 5 is a perspective view showing a fixing structure of a support frame, a vertical fixing frame, and an external fixing frame, which are main parts of a separation membrane module unit to which the present invention is applied.
Fig. 6 is a sectional view showing a use state of a separation membrane module unit to which the present invention is applied.
As shown in fig. 1 to 6, a separation membrane module unit 1000 to which the preferred embodiment of the present invention is applied filters polluted and waste water by being installed and fixed inside a reaction tank, and generally includes a separation membrane module 100, a support frame 200, a vertical fixing frame 300, an outer fixing frame 400, and a diffuser 500.
In this case, the reaction tank is not specifically shown in the drawings, but may be a reaction tank in a general sewage treatment facility.
Next, a detailed configuration of the separation membrane module unit 1000 to which the present invention is applied will be explained. First, the upper end of the separation membrane module 100 is connected to the suction pump 10 through a pipe, and a hollow fiber membrane bundle 110 formed by bundling a plurality of hollow fiber membranes 111 is disposed at the center in the vertical direction, so that water washed upward from the lower side of the outside of the hollow fiber membranes 111 through the inside can be discharged to the outside of the reaction tank by driving the suction pump.
In addition, the support frame 200 is formed in a frame shape having a through hole 210 formed at the center thereof, and the lower end of the separation membrane module 100 is seated and mounted at the upper portion thereof.
In addition, the vertical fixing frame 300 is formed in a vertical frame shape having a certain length, and a plurality of vertical fixing frames are fixedly installed at certain intervals along the outer circumference of the support frame 200 by fixing members, so that the support frame 200 can be fixedly installed in a state of being upwardly spaced a certain distance from the lower end.
In this case, as shown in fig. 1 to 6, the fixing member may be formed of a bolt B and a nut N, and in particular, a flat head bolt may be used in consideration of interference of the bolt B.
In addition, the external fixing frames 400 are fixedly installed at the lower, central, and upper end portions of the vertical fixing frames 300 by fixing members in such a manner as to surround the vertical fixing frames 300, respectively, installed at the bottom surface of the reaction tank or fixedly installed at the vertical sidewalls.
As the fixing member for fixing the external fixing frame 400 and the vertical fixing frame 300 as described above, the bolt B and the nut N are also preferably applied.
The air diffuser 500 includes a main body 510 formed with a plurality of through holes on an upper side surface thereof and disposed on a lower side of the support frame 200 to diffuse air bubbles, and a connection pipe 520 bent and extended from the lower side of the main body 510 a plurality of times so as to communicate with each other and sequentially passing through the outer fixing frames 400 disposed at the center and the upper end of the vertical fixing frame 300.
Particularly, in the air dispersion pipe 500 as described above, the extended end of the connection pipe 520 is connected to the blower 20 through a pipe, and bubbles are dispersed upward from the lower side of the support frame 200 by the driving of the blower 20 and thereby the outer surface of the hollow fiber membranes 111 of the separation membrane module 100 is washed.
In the separation membrane module unit 1000 to which the present invention is applied, which is configured as described above, the separation membrane module 100 generally includes the hollow fiber membrane bundle 110, the lower cover 130, and the upper cover 150.
Specifically, the hollow fiber membrane bundle 110 is formed by bundling a plurality of hollow fiber membranes 111.
The lower cover 130 is formed in a column shape having an upper portion and a lower portion opened and a mounting plate 131 formed at the center, the lower end of the hollow fiber membrane bundle 110 is fixedly mounted to be spaced apart from the mounting plate 131 upward, a plurality of communication holes 131a are formed through the mounting plate 131, and the peripheral portion of the lower end is mounted on the support frame 200.
When the lower end of the hollow fiber membrane bundle 110 in the lower cover 130 is fixedly attached to the installation plate 131 with a predetermined distance upward, it is preferably fixedly attached by adhesion using an adhesive or the like.
The upper cap 150 is formed in a column shape having a lower portion opened and a connection port 151 formed at the center of the sealed upper surface in a protruding manner, and the upper end of the hollow fiber membrane bundle 110 is fixedly attached to the lower surface of the upper surface of the hollow fiber membrane bundle with a predetermined distance therebetween.
In this case, when the upper end of the hollow fiber membrane bundle 110 in the upper cover 150 is fixedly attached to the upper end of the hollow fiber membrane bundle by being spaced a predetermined distance downward from the inner upper surface, the upper end is preferably fixedly attached to the upper end by adhesion using an adhesive or the like.
In the separation membrane module unit 1000 to which the present invention is applied, which is configured as described above, the separation membrane module 100 is formed in a rectangular column shape as shown in fig. 1 to 6.
In addition, the support frame 200 is formed in a square frame shape having a "l" shaped section.
Further, the above-described vertical fixing frame 300 is formed in an angular form having a "l" -shaped cross section when viewed in a plane in order to be adhered to each corner portion of the support frame 200.
The external fixing frame 400 is formed in a rectangular frame shape having a cross section of "l" shape, and is fixed and mounted by fixing members at the lower end, the center, and the upper end of the vertical fixing frame 300 so as to surround the vertical fixing frame 300.
In this case, the outer fixing frame 400 disposed at the lower end portion of the vertical fixing frame 300 is preferably fixedly mounted in an l-shape in which the l shape is inverted vertically.
That is, by fixedly mounting the outer fixing frame 400 disposed at the lower end portion of the vertical fixing frame 300 in a "l" shape in which the l shape is inverted up and down, the lower end portion can be stably seated when mounted to the inner bottom surface of the reaction tank, and at the same time, the mounting and fixing can be easily performed by a separate bracket or the like so as not to move inside the reaction tank.
Further, the external fixing frame 400 is preferably formed in a square frame shape having a "l" shape or a "l" shape in cross section, and is preferably formed in a square frame shape in which four portions with cut corner portions are formed by dividing, and oblique lines are attached to each other when the divided opposite end portions are viewed in a plane.
In other words, the external fixation frame 400 is formed in a square frame shape in which four unit division frames are divided, and the end portions facing each other are formed in a diagonal line shape and closely attached to each other.
In the separation membrane module unit 1000 to which the present invention is applied, configured as described above, as shown in fig. 6, the suction pump 10 is connected to the connection port 151 of the upper cover 150 of the separation membrane module 100 through the suction connection pipe 10a, so that filtered water obtained while passing through the inside of the hollow fiber membranes 111 can be sucked and treated through the connection port 151 when the suction pump 10 is driven.
In this case, in order to achieve tight connection between the suction connection pipe 10a and the connection portion of the connection port 151, it is preferable to connect by using separate male and female connectors.
Meanwhile, referring to fig. 6, when the blower 20 is driven, bubbles are emitted to the lower side of the separation membrane module 100 through the body 510 of the diffuser pipe 500 by communicatively connecting the blower 20 to the end of the connection pipe 520 of the diffuser pipe 500 through the air supply connection pipe 20 a.
In this case, in order to achieve close connection between the air blowing connection duct 20a and the connection portion of the end of the connection pipe 520 of the air-releasing pipe 500, it is preferable to use separate male and female connectors for connection.
In addition, the bubbles emitted through the main body 510 of the above-described air diffuser 500 may come into full contact with the outer surfaces of the respective hollow fiber membranes 111 in the hollow fiber membrane bundle 110 of the separation membrane module 100 via the through-holes 210 of the support frame 200.
Thereby, the entire outer and inner sides of the hollow fiber membrane bundle 110 of the separation membrane module 100 can be uniformly washed.
In other words, the entire outer surfaces of the hollow fiber membranes 111 arranged inside the hollow fiber membrane bundle 110 of the separation membrane module 100 and the hollow fiber membranes 111 arranged outside can be washed.
FIG. 7 is a perspective view showing a separation membrane module unit to which another embodiment of the present invention is applied.
The embodiment illustrated in fig. 7 is different from the embodiment described with reference to fig. 1 to 6 in the overall view that only the cylindrical form is adopted instead of the square cylindrical form, and thus a detailed description about the constitution of the same reference numeral will be omitted.
In the separation membrane module unit 1000 to which another embodiment of the present invention is applied, the separation membrane module 100 is formed in a cylindrical shape.
The separation membrane module 100 as described above generally includes a hollow fiber membrane bundle 110, a lower cover 130, and an upper cover 150.
Specifically, the hollow fiber membrane bundle 110 is formed by bundling a plurality of hollow fiber membranes 111.
The lower cover 130 is formed in a column shape having an upper portion and a lower portion opened and a mounting plate 131 formed at the center, the lower end of the hollow fiber membrane bundle 110 is fixedly mounted to be spaced apart from the mounting plate 131 upward, a plurality of communication holes 131a are formed through the mounting plate 131, and the peripheral portion of the lower end is mounted on the support frame 200.
When the lower end of the hollow fiber membrane bundle 110 in the lower cover 130 is fixedly attached to the installation plate 131 with a predetermined distance upward, it is preferably fixedly attached by adhesion using an adhesive or the like.
The upper cap 150 is formed in a column shape having a lower portion opened and a connection port 151 formed at the center of the sealed upper surface in a protruding manner, and the upper end of the hollow fiber membrane bundle 110 is fixedly attached to the lower surface of the upper surface of the hollow fiber membrane bundle with a predetermined distance therebetween.
In this case, when the upper end of the hollow fiber membrane bundle 110 in the upper cover 150 is fixedly attached to the upper end of the hollow fiber membrane bundle by being spaced a predetermined distance downward from the inner upper surface, the upper end is preferably fixedly attached to the upper end by adhesion using an adhesive or the like.
The support frame 200 is formed in a circular frame shape having an "l" shaped cross section, and the vertical fixing frame 300 is formed in a rod shape having a curved arc-shaped cross section when viewed in a plane so as to be closely attached along the periphery of the support frame 200.
The outer fixing frame 400 is formed in a circular frame shape having a "l" shaped cross section, and is fixedly installed at the lower end, the center, and the upper end portions of the vertical fixing frame 300 by fixing members so as to surround the vertical fixing frame 300, respectively.
In this case, the outer fixing frame 400 disposed at the lower end portion of the vertical fixing frame 300 is preferably fixed in a l-shape which is inverted vertically in a "l" shape.
In the separation membrane module unit configured as described above to which the present invention is applied, the entire outer and inner sides of the hollow fiber membrane bundle of the separation membrane module can be uniformly washed by including the separation membrane module, the support frame, the vertical fixing frame, the external fixing frame, and the air diffusing pipe, thereby increasing an effective washing area.
Moreover, by using the separation membrane module, the support frame, the vertical fixing frame, the external fixing frame and the diffuser pipe, the entire outside and inside of the hollow fiber membrane bundle of the separation membrane module can be uniformly washed, thereby increasing the effective washing area and thereby significantly increasing the service life of the separation membrane module while enhancing the performance of the separation membrane module.
In addition, the present invention includes a separation membrane module, a support frame, a vertical fixing frame, an external fixing frame, and a diffuser, so that a user can selectively and conveniently mount a plurality of separation membrane unit modules in a unit form according to the filtration capacity of a reaction tank for use.
Furthermore, the separation membrane module comprises the separation membrane module, a supporting frame, a vertical fixing frame, an external fixing frame and an air dispersing pipe, so that modularization can be realized, the separation membrane module arranged on the supporting frame can be conveniently separated, and washing treatment can be conveniently carried out in modes of reverse washing and the like, and the separation membrane module can be conveniently maintained and managed.
While the present invention has been described in detail with reference to the specific embodiments thereof, it will be apparent to those skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope of the invention as defined in the appended claims.

Claims (5)

1. A separation membrane module unit characterized by:
as a separation membrane module unit (1000) for filtering sewage and wastewater by being installed and fixed inside a reaction tank, comprising:
a separation membrane module (100) having an upper end connected to the suction pump (10) through a pipe, and a hollow fiber membrane bundle (110) formed by bundling a plurality of hollow fiber membranes (111) is disposed at the center in the vertical direction, so that water washed upward from the outside lower side of the hollow fiber membranes (111) through the inside is driven by the suction pump to flow out of the reaction tank;
a support frame (200) formed in a frame shape having a through-hole (210) formed at the center thereof, for the lower end of the separation membrane module (100) to be seated at the upper portion thereof;
a plurality of vertical fixing frames (300) formed in a vertical frame shape having a certain length, fixedly installed at certain intervals along the outer circumference of the support frame (200) by fixing members, for the support frame (200) to be fixedly installed in a state of being upwardly spaced a certain distance from the lower end;
an outer fixing frame (400) fixedly installed at the lower, central, and upper end portions of the vertical fixing frame (300) by fixing members in such a manner as to surround the vertical fixing frame (300), respectively, installed on the bottom surface of the reaction tank or fixedly installed on the vertical sidewall; and (c) a second step of,
the air diffusion pipe (500) is composed of a main body (510) which is formed with a plurality of through holes on the upper side surface and is configured on the lower side of the supporting frame (200) for diffusing air bubbles, and a connecting pipe (520) which is formed by bending and extending from the lower side of the main body (510) for a plurality of times in a mutually communicated mode and extending in a mode of sequentially penetrating through the external fixing frames (400) arranged on the center and the upper end part of the vertical fixing frame (300), wherein the extending end part of the connecting pipe (520) is connected with the air blower (20) through a pipeline, and the air bubbles are upwards diffused from the lower side of the supporting frame (200) by the driving of the air blower (20) so as to perform washing treatment on the external surface of the hollow fiber membrane (111) of the separation membrane module (100).
2. The separation membrane module unit according to claim 1, wherein:
the separation membrane module (100) comprises:
a hollow fiber membrane bundle (110) formed by bundling a plurality of hollow fiber membranes (111);
a lower cover (130) which is opened at the upper and lower parts and is formed in a column shape with a placing plate (131) formed at the center, the lower end of the hollow fiber membrane bundle (110) is fixedly installed in a mode of upwards spacing a certain distance from the placing plate (131), a plurality of communication holes (131 a) are formed on the placing plate (131) in a penetrating way, and the peripheral part of the lower end is placed on the supporting frame (200); and (c) a second step of,
and an upper cover (150) which is formed in a column shape with a lower part opened and a connection port (151) formed at the center of the sealed upper side surface in a protruding manner, wherein the upper end of the hollow fiber membrane bundle (110) is fixedly installed in a mode of downwards spacing a certain distance from the inner upper side surface.
3. The separation membrane module unit according to claim 1, wherein:
the separation membrane module (100) is formed in a square column state,
the support frame (200) is formed in a square frame shape having a substantially L-shaped section,
the vertical fixing frames (300) are formed in an angular form having a "" L "" shaped section when viewed in a plane in order to be adhered to respective corner portions of the support frames (200),
the outer fixing frame (400) is formed in a square frame shape with a 'L' shaped cross section, and is fixedly installed at the lower end, the center and the upper end part of the vertical fixing frame (300) through fixing components in a mode of respectively surrounding the vertical fixing frame (300),
an outer fixing frame (400) arranged at the lower end portion of the vertical fixing frame (300) is fixedly mounted in a L shape which is inverted from top to bottom in a L shape.
4. The separation membrane module unit according to claim 3, wherein:
the external fixing frame (400) is formed in a square frame shape with a L-shaped or L-shaped section,
and four portions where corner portions are cut are divided to form a square frame shape in which the divided opposite ends are attached to each other with oblique lines when viewed in a plane.
5. The separation membrane module unit according to claim 1, wherein:
the separation membrane module (100) is formed in a cylindrical form,
the support frame (200) is formed in a circular frame shape having a substantially L-shaped section,
the vertical fixing frame (300) is formed in a bar shape having a curved arc-shaped section when viewed on a plane in order to be attached along the circumference of the support frame (200),
the outer fixing frame (400) is formed in a circular frame shape having a cross section of a 'L' shape, and is fixedly installed at the lower end, the center, and the upper end portion of the vertical fixing frame (300) by fixing members in a manner of surrounding the vertical fixing frame (300) respectively,
an outer fixing frame (400) arranged at the lower end portion of the vertical fixing frame (300) is fixedly mounted in a L shape which is inverted from top to bottom in a L shape.
CN202110603093.7A 2021-05-31 2021-05-31 Separation membrane module unit Pending CN115475531A (en)

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Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336662A (en) * 2001-05-11 2002-11-26 Hitachi Zosen Corp Filtration membrane apparatus for treating water
KR20040055314A (en) * 2002-12-20 2004-06-26 코오롱건설주식회사 Hollow fiber membrane module unit
KR100441752B1 (en) * 2003-11-17 2004-07-23 주식회사 퓨어엔비텍 Foul or waste water disposal device with filtration membrane and filtration membrane guide separated
JP2004344848A (en) * 2003-05-26 2004-12-09 Asahi Kasei Chemicals Corp Membrane separation method and device
CN1923725A (en) * 2005-08-29 2007-03-07 大韩通运株式会社 High efficiency separation membrane assembly for waste water treatment
KR20080105789A (en) * 2007-06-01 2008-12-04 주식회사 퓨어엔비텍 A filtration membrane module guide for multistory filtration membrane module in foul or waste water disposal device
CN201295595Y (en) * 2008-11-25 2009-08-26 孟广祯 Aeration external pressure membrane filter
CN102046273A (en) * 2008-05-27 2011-05-04 株式会社神钢环境舒立净 Hollow-fiber membrane module, method of membrane separation, and apparatus for water treatment
CN102740955A (en) * 2010-06-30 2012-10-17 住友电工超效能高分子股份有限公司 Immersion type membrane module unit and membrane bioreactor device
JP2013255919A (en) * 2013-08-14 2013-12-26 Mitsubishi Rayon Co Ltd Membrane filtration unit
CN205275298U (en) * 2015-12-29 2016-06-01 厦门裕清水环保工程有限公司 Membrane module and installing the system thereof
KR101713927B1 (en) * 2016-09-05 2017-03-09 백운학 Membrane bioreactors filter apparatus for cassette type
JP2020089835A (en) * 2018-12-06 2020-06-11 住友電気工業株式会社 Washing method and immersion-type filtering device
CN111282370A (en) * 2018-12-07 2020-06-16 瑞进能源株式会社 Air purification integrated immersed hollow fiber membrane module device
CN112299555A (en) * 2020-01-16 2021-02-02 广东宇唐环保设备有限公司 High-pollution-resistance MBR (membrane bioreactor) membrane assembly for wastewater treatment

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336662A (en) * 2001-05-11 2002-11-26 Hitachi Zosen Corp Filtration membrane apparatus for treating water
KR20040055314A (en) * 2002-12-20 2004-06-26 코오롱건설주식회사 Hollow fiber membrane module unit
JP2004344848A (en) * 2003-05-26 2004-12-09 Asahi Kasei Chemicals Corp Membrane separation method and device
KR100441752B1 (en) * 2003-11-17 2004-07-23 주식회사 퓨어엔비텍 Foul or waste water disposal device with filtration membrane and filtration membrane guide separated
CN1923725A (en) * 2005-08-29 2007-03-07 大韩通运株式会社 High efficiency separation membrane assembly for waste water treatment
KR20080105789A (en) * 2007-06-01 2008-12-04 주식회사 퓨어엔비텍 A filtration membrane module guide for multistory filtration membrane module in foul or waste water disposal device
CN102046273A (en) * 2008-05-27 2011-05-04 株式会社神钢环境舒立净 Hollow-fiber membrane module, method of membrane separation, and apparatus for water treatment
CN201295595Y (en) * 2008-11-25 2009-08-26 孟广祯 Aeration external pressure membrane filter
CN102740955A (en) * 2010-06-30 2012-10-17 住友电工超效能高分子股份有限公司 Immersion type membrane module unit and membrane bioreactor device
JP2013255919A (en) * 2013-08-14 2013-12-26 Mitsubishi Rayon Co Ltd Membrane filtration unit
CN205275298U (en) * 2015-12-29 2016-06-01 厦门裕清水环保工程有限公司 Membrane module and installing the system thereof
KR101713927B1 (en) * 2016-09-05 2017-03-09 백운학 Membrane bioreactors filter apparatus for cassette type
JP2020089835A (en) * 2018-12-06 2020-06-11 住友電気工業株式会社 Washing method and immersion-type filtering device
CN111282370A (en) * 2018-12-07 2020-06-16 瑞进能源株式会社 Air purification integrated immersed hollow fiber membrane module device
CN112299555A (en) * 2020-01-16 2021-02-02 广东宇唐环保设备有限公司 High-pollution-resistance MBR (membrane bioreactor) membrane assembly for wastewater treatment

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