CN202724803U - Filter element of automatic cleaning membrane filter - Google Patents

Filter element of automatic cleaning membrane filter Download PDF

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Publication number
CN202724803U
CN202724803U CN 201220415503 CN201220415503U CN202724803U CN 202724803 U CN202724803 U CN 202724803U CN 201220415503 CN201220415503 CN 201220415503 CN 201220415503 U CN201220415503 U CN 201220415503U CN 202724803 U CN202724803 U CN 202724803U
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CN
China
Prior art keywords
inner support
filter
pipe
stalk
filter element
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 201220415503
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Chinese (zh)
Inventor
杨琲
翟军
黄义忠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANGHAI LEZE ENVIRONMENTAL ENGINEERING Co Ltd
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SHANGHAI LEZE ENVIRONMENTAL ENGINEERING Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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Application filed by SHANGHAI LEZE ENVIRONMENTAL ENGINEERING Co Ltd filed Critical SHANGHAI LEZE ENVIRONMENTAL ENGINEERING Co Ltd
Priority to CN 201220415503 priority Critical patent/CN202724803U/en
Application granted granted Critical
Publication of CN202724803U publication Critical patent/CN202724803U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a filter element of an automatic cleaning membrane filter. The filter element comprises a plurality of single filter element bodies and a liquid outlet pipe, each single filter element body comprises a membrane, an inner support and a liquid rising pipe, each inner support comprises a plurality of connected cylindrical hollow pipes which are uniformly distributed on the outer cylindrical face of each liquid rising pipe in a petal type structure, the upper bottom of each inner support is hermetically connected with the outer edge of each liquid rising pipe while the lower bottom of each inner support is closed, the hollow pipes of each inner support are communicated with the pipe bottom of each liquid rising pipe through a pipe bottom space, the pedal type outer cylindrical face of each inner support is provided with a plurality of circumferential gaps at intervals along the axis direction, each membrane is made into a filter cartridge shape and covers the pedal type outer cylindrical face of each inner support, the upper end and the lower end of each membrane are hermetically connected with each inner support, and the liquid rising pipe for each inner support is hermetically connected on the liquid outlet pipe. The filter element has the advantages that filter elements can be used in group, liquid with low suspended solids and high suspended solids can be filtered, the suspended solids can be collected and blown to be dry, and the automatic cleaning membrane filter which is large in filling area and good in back wash effect is formed.

Description

A kind of self-cleaning membrane filter filter core
Technical field
The utility model relates to a kind of isolation technics, relates in particular to a kind of self-cleaning membrane filter filter core.
Background technology
Filtration is important in a liquid-solid separation method, for large flow, and large batch of liquid filtering, the filter that many employings can automatic backwash.The filter of automatic backwash mainly contains medium class filter at present, screen cloth class filter, and the fiber-like filter, film class filter etc., every kind of filter has its applicability.Film class filter has a wide range of applications in the Separation of Solid and Liquid field as main class filter a kind of capable of washing, and the membrane filter filtering accuracy is wide, and the film kind is many.The filter of common film class has many disk filters on the market, rotary drum filter etc., such filter generally all adopts high pressure water washing regeneration, but in order to satisfy the requirement of cleaning, monolithic filter is not with the pressure operation, film filling area is little in the system, and system takes up an area large, and the backwash water consumption is very large.The collection of filter cake is difficulty also.U.S. Aquatech company has developed a kind of film filter disc filter, the mode backwash of adopting vacuum to suck, improved greatly film filling area, but the pressure that vacuum is sucked is no more than 1 atmospheric pressure, is difficult to realize effective backwash for some relatively more sticking impurity.In addition, this filter can only be applicable to water body filtration, can not collect filter cake.Domestic also someone attempt with film cover on porous in be lining with the formation candle filter, but the non-constant of backwash effect is found in practice, can not fine collection filter cake.Based on present present situation, the inventor thinks that to develop a kind of filling area large, and efficiently backwash and the self-cleaning membrane filter of effectively collecting filter cake will have very large market prospects.
The utility model content
The purpose of this utility model is to provide a kind of self-cleaning membrane filter filter core for the prior art weak point.This filter element can filter the liquid that contains suspension, reduces the suspension in the filtrate, also can collect the suspension filter cake.
The utility model is by the following technical programs in to realize: a kind of self-cleaning membrane filter filter core, it is characterized in that, and it includes some filter core monomers, drain pipe; Described filter core monomer is comprised of film, inner support, stalk, inner support forms, is on the outer cylinder that the petal type structure is distributed on stalk by some hollow tube disjunctors that are column, the inner support upper base is connected with the stalk outer fringe seal, go to the bottom sealing, each hollow tube of inner support of inner support is communicated with at the bottom of the stalk pipe by the pipe base space, has some phases circumferential slit across a certain distance along its axis direction on the inner support petal type outer cylinder; Described film is made the filter cylinder shape, is covered on the inner support petal type outer cylinder, and film upper/lower terminal and inner support are tightly connected, and the stalk of described each inner support is sealedly connected on the drain pipe.
Be furnished with vertical groove on the described inner support petal type outer cylinder.
Good effect of the present utility model is: a kind of self-cleaning membrane filter filter core that the utility model proposes, have following advantage: film is being close under the effect of filtration pressure difference on the petal type inner support cylinder, utilizes grooves numerous on the cylinder and circumferential slit to collect the liquid that membrane filtration gets off; Film rapid expanding under the effect of backwashing water or gas is circle-shaped during backwash, and the impurity that is attached on the film is cleaned under backwashing pressure and the effect of film expansive force totally.This filter core can use in groups and be installed on the filter, both can filter the liquid of low suspension, also can filter the liquid of high suspended matter, and can collect, dry up this suspension, consist of a kind of filling area large, backwash effect is good, and can effectively reclaim the self-cleaning membrane filter of filter cake, has very large market prospects.
Description of drawings
Fig. 1 is that embodiment of the utility model is installed in the structural profile schematic diagram in the filter.
Fig. 2 is Fig. 1 A section enlarged drawing.
Fig. 3 is the schematic cross-section of filter core under filtration condition.
Fig. 4 is the schematic cross-section of filter core under the backwash state.
The utility model will be further described below in conjunction with embodiment:
Fig. 1~Fig. 2 is that embodiment of the utility model is installed in the structural profile schematic diagram in the filter.Among the figure, a kind of self-cleaning membrane filter filter core, it includes: some filter core monomers 1, drain pipe 3; Described filter core monomer is comprised of film 11, inner support 12, stalk 13, inner support 12 forms, is on the outer cylinder that the petal type structure is distributed on stalk 13 by some hollow tube disjunctors that are column, the petal number is six lobes in the present embodiment, inner support 12 upper bases are connected with stalk 13 outer fringe seals, go to the bottom sealing, inner support 12 each hollow tube of inner support 12 managed the ends by pipe base space and stalk 13 and is communicated with, and has some phases circumferential slit 14 across a certain distance along its axis direction on the inner support 12 petal type outer cylinders; Described film 11 is made the filter cylinder shape, is covered on the inner support 12 petal type outer cylinders, and film 11 upper/lower terminals and inner support 12 are tightly connected, and the stalk of described each inner support 12 is sealedly connected on the drain pipe 3.
The utility model is further taked following measure: be furnished with vertical groove 15 on the described inner support petal type outer cylinder.
The utility model is like this work:
Filter process as shown in Figure 3, liquid sees through film by the outside of crossing filter core, is pooled to the groove on the inner support, and successively by finedraw, petal hollow tube inner tube, stalk is flowed out by the stalk upper end at last.Film is close to the petal inner support and also is petal-shaped under the effect of filtration pressure difference, the particle in the liquid is intercepted at film surface.Can select the film of different model to satisfy to filtering accuracy filtration temperature, the needs of filter medium.
Backwash process is as shown in Figure 4: by the downward flow at high speed in stalk top, by petal hollow tube inner tube, finedraw is the backwash film fast and evenly under the effect of hydraulic pressure or air pressure for backwash liquid when pressure reduction or time reach setting value.Film is under the effect of backwashing water or gas, be circle-shaped by the petal-shaped rapid expanding, impurity is cleaned under backwashing pressure and the effect of film expansive force totally, each organizes successively backwash of filtrate pipe, also can add filter aid during backwash, form cake filtration with filter aid at film, improve filtering accuracy.
The above reaches by reference to the accompanying drawings embodiment and has described embodiment of the present utility model; the structure that embodiment provides does not consist of restriction of the present utility model; those skilled in the art can show and need to adjust according to real in this area, make within the scope of the appended claims various distortion or modification all in protection domain.

Claims (2)

1. a self-cleaning membrane filter filter core is characterized in that, it includes some filter core monomers, drain pipe; Described filter core monomer is comprised of film, inner support, stalk, inner support forms, is on the outer cylinder that the petal type structure is distributed on stalk by some hollow tube disjunctors that are column, the inner support upper base is connected with the stalk outer fringe seal, go to the bottom sealing, each hollow tube of inner support of inner support is communicated with at the bottom of the stalk pipe by the pipe base space, has some phases circumferential slit across a certain distance along its axis direction on the inner support petal type outer cylinder; Described film is made the filter cylinder shape, is covered on the inner support petal type outer cylinder, and film upper/lower terminal and inner support are tightly connected, and the stalk of described each inner support is sealedly connected on the drain pipe.
2. self-cleaning membrane filter filter core according to claim 1 is characterized in that, is furnished with vertical groove on the described inner support petal type outer cylinder.
CN 201220415503 2012-08-21 2012-08-21 Filter element of automatic cleaning membrane filter Expired - Fee Related CN202724803U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220415503 CN202724803U (en) 2012-08-21 2012-08-21 Filter element of automatic cleaning membrane filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220415503 CN202724803U (en) 2012-08-21 2012-08-21 Filter element of automatic cleaning membrane filter

Publications (1)

Publication Number Publication Date
CN202724803U true CN202724803U (en) 2013-02-13

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220415503 Expired - Fee Related CN202724803U (en) 2012-08-21 2012-08-21 Filter element of automatic cleaning membrane filter

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CN (1) CN202724803U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103463988A (en) * 2013-07-24 2013-12-25 乐金电子研发中心(上海)有限公司 Self-cleaning MBR flat sheet membrane module and cleaning method thereof
CN107261626A (en) * 2017-06-07 2017-10-20 常州兆威不锈钢有限公司 A kind of cobalt hydroxide slurry filtration wash unit
CN108310834A (en) * 2017-01-18 2018-07-24 黄学锋 Three-level backwashing system and purging method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103463988A (en) * 2013-07-24 2013-12-25 乐金电子研发中心(上海)有限公司 Self-cleaning MBR flat sheet membrane module and cleaning method thereof
CN103463988B (en) * 2013-07-24 2015-09-23 乐金电子研发中心(上海)有限公司 Self-cleaning MBR flat sheet membrane module and cleaning method thereof
CN108310834A (en) * 2017-01-18 2018-07-24 黄学锋 Three-level backwashing system and purging method
CN107261626A (en) * 2017-06-07 2017-10-20 常州兆威不锈钢有限公司 A kind of cobalt hydroxide slurry filtration wash unit

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130213

Termination date: 20200821