CN2623323Y - High efficiency ultrafiltration device - Google Patents

High efficiency ultrafiltration device Download PDF

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Publication number
CN2623323Y
CN2623323Y CN 03227844 CN03227844U CN2623323Y CN 2623323 Y CN2623323 Y CN 2623323Y CN 03227844 CN03227844 CN 03227844 CN 03227844 U CN03227844 U CN 03227844U CN 2623323 Y CN2623323 Y CN 2623323Y
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China
Prior art keywords
liquid
utility
model
zone
filtering
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Expired - Fee Related
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CN 03227844
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Chinese (zh)
Inventor
刘仁军
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Individual
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Individual
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Priority to CN 03227844 priority Critical patent/CN2623323Y/en
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Publication of CN2623323Y publication Critical patent/CN2623323Y/en
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Expired - Fee Related legal-status Critical Current

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Abstract

A high efficiency ultrafiltration device consists of a container (1), a filtering medium zone (2), a clear solution zone (3), a waste liquor inlet (4), a clear solution outlet (5), a concentrated solution outlet (6), a flange keep plate (8), clapboards (7) and (9), a bolt (11) and a millipore ceramic membrane pipe (12). The utility model is characterized in that the clapboards (7) and (9) and the millipore ceramic membrane pipe (12) are welded and stuck into a sealed frame in the container (1), the container (1) is divided into the filtering medium zone (2) and the clear solution zone (3). The utility model has the advantages of high efficiency of operating, wide range of application, good effects of separating and purifying, double advantages of filtering and air bearing, long circle and excellent efficiency of bounce-back and regeneration. The utility model is widely applied in the filtering of waste water and waste gas.

Description

The high-performance ultrafiltration device
The utility model relates to a kind of filter:
Before the utility model, there is filter in the system of decontaminating liquid, device such as filter, air supporting, though their suspensions in can filter liquide with separate greasy dirt, but all existing many deficiencies and worn-out sick, mainly is that operational efficiency is low, inferior separating effect, can oil removing and can not remove suspension, it is frequent etc. that frequent complicated, the filtrate of short, maintenance filter cycle can not regenerate and change.
The purpose of this utility model is exactly to overcome above deficiency and a kind of micropore ceramics film pipe ultrafiltration apparatus of proposing.
Advantage of the present utility model is: the operational efficiency height, and wide accommodation, the isolation of purified effect is superior, has to filter and pneumatically supported two-fold advantage, and recoil long-acting rate of regeneration period is splendid.
Invention main points of the present utility model are in the tank body (1), through welding, stick into the sealing frame, tank body (1) are divided into filtration liquid zone (2) and clear liquid area (3) with dividing plate (7), (9) and micropore ceramics film pipe (12).Make most of liquid adsorb its suspension, oils and colloid shape material in through the surface of micropore ceramics film pipe (12) and micropore through pressurization; Under the oxidation of the oxygen that liquid flow and liquid discharge, thereby take away and its harmful substance of oxidation, suspension, oils and colloid shape material obtain better clean-up effect.
Operation principle of the present utility model is:
One, technological process principle is the alternate cycles of two processes of ultrafiltration and flushing
Feed liquor to be filtered enters into waste liquid district (2) through inlet (4) and passes through suspension and oils and the colloid substance that liquid is held back in micropore ceramics film pipe (12) ultrafiltration absorption again; Most of scavenging solution enters into clear liquid area (3) through liquid outlet (5) bleeder.Then fraction concentrated liquid band the suspension that is retained down, and oils and colloid substance are through concentrated solution outlet (6) bleeder.In filtration,, when resistance (pressure reduction) reaches maximum the permission, should carry out backwash because tube-surface film and micro-porous adsorption are constantly cut out and stayed, and membrane pores reduces gradually, and liquid flowing resistance constantly increases.When carrying out backwash, carbonated drink (compressed air) is by the ceramic membrane tube wall, by means of its shearing force, impulse force and particle collision friction cleaning ceramic film pipe, and dirt is discharged in will installing.
Two, oil, outstanding clean thing are removed mechanism
Mechanism General introduction
1, every the filter tool every the filter accidental contact filtration Particle diameter is intercepted and captured owing to contact accidentally less than the particle in pore crack greater than the particle tunicle pipe elimination particle diameter of ceramic-film tube hole
2, precipitation, collision The particle heavier in film device waste liquid district do not precipitate with the streamline motion
3, intercept and capture The particle of many streamline motions contacts and is removed with the film tube-surface
4, adhere to When the flocculation particle passes through ceramic-film tube with oil, they will be attached to the film tube-surface, because some particle of impulsive force of liquid stream and air-flow as yet firm attachment when ceramic-film tube is surperficial, will be punched into ceramic membrane tube wall deep layer by liquid or gas, after ceramic-film tube stops up gradually, surface shear power, resistance just begins to increase, so that make ceramic-film tube can not remove any suspension and oil, some suspensions may penetrate, fluid is exceeded standard, thereby just should begin backwash.
5, the interaction of chemisorptive bond absorption chemistry Oil and particle are in case contact this particle and oil and can work and quilt floats and obtains owing to one or both mechanism wherein with ceramic-film tube surface or with other particle surface
6, the absorption of the moving electricity absorption of physical absorption Electrostatic Absorption Van der Waals force
7, flocculation When contacting with less threshing, bulky grain it can be caught, and forming bigger particle, these bigger particles will be removed owing to above-mentioned one or more mechanism work
8, physics screening The particle that particle that particle diameter is big and particle diameter are little is held back by the ceramic-film tube skin covering of the surface, oxidation under liquid flow and buoyancy and taking out of
Concrete structure of the present utility model and purpose are born by following enforcement and accompanying drawing thereof:
Fig. 1: be vertical section schematic diagram of the present utility model
Fig. 2: be micropore ceramics film pipe schematic diagram of the present utility model
Among the figure:
1:---tank body: the usefulness of filtration, purification work for liquid
2:---filter the liquid zone: be to store liquid to be filtered
3:---clear liquid area: be the clear liquid that stores after filtering
4:---inlet, the usefulness that supplies liquid to be filtered to enter, and work is discharged the usefulness of greasy dirt when recoiling
5:---the clear liquid liquid outlet: for the usefulness of discharging clear liquid, and the usefulness that feeds carbonated drink (compressed air) when doing recoil
6:---concentrated solution outlet: for the usefulness of filtering the concentrated liquid discharge in back
7:---dividing plate: mainly be to isolate the usefulness of filtering liquid zone (2) and clear liquid area (3) and support with micropore ceramics film pipe (12) fixing seal
8:---the flange pressing plate mainly is to fix, seal micropore ceramics film pipe
9:---dividing plate: mainly be to fix, support, seal, isolate the usefulness that (2) are connected with (3) for micropore ceramics film pipe
10:---flange: mainly be the usefulness that connects the tank body centre
11:---bolt mainly is the usefulness of adpting flange and tank body
12:---micropore ceramics film pipe
13, the micropore of micropore ceramics film pipe
Embodiment of the present utility model:
At first on tank body (1), burn-on flange (8), (10), stick into the close encapsulation frame with microtubule ceramic-film tube (12) and dividing plate (7), (9) through weldering, tank body (1) is divided into filtrate district (2) and clear liquid area (3), the centre of using bolt (11) to connect tank body then makes it sealing and fixing.
Then feed liquid to be filtered from inlet (4) pressurization, enter in the liquid zone to be filtered (2), liquid to be filtered by micropore ceramics film pipe (12) micropore and after the film surface filters, clear liquid enters into clear liquid area (3) after outlet (5) is discharged, and concentrated liquid (suspension oils that is trapped out and colloid shape material are under a downforce) is discharged through concentrated solution outlet (6) simultaneously.Out of service after use a period of time, pressurization feeds carbonated drink (compressed air) to clear liquid area (3) from import (5), after carbonated drink (compressed air) is cleaned micropore ceramics film pipe (12), the dirt that cleans out sinks to district to be filtered (2) and is discharged by sewage draining exit (4) or (6), recycles it like this.The utility model is widely used in the purified treatment of various liquid.

Claims (1)

1, high-performance ultrafiltration device, it filters liquid zone (2), clear liquid area (3) by tank body (1), waste liquid import (4), purified liquor outlet (5), concentrated solution outlet (6), flange pressing plate (8), (10), dividing plate (7), (9), bolt (11), micropore ceramics film pipe (12) are formed, and it is characterized in that tank body (1) inner-use clapboard (7), (9) and micropore ceramics film pipe (12) through welding, stick into the sealing frame, tank body (1) is divided into filters liquid zone (2) and clear liquid area (3).
CN 03227844 2003-06-09 2003-06-09 High efficiency ultrafiltration device Expired - Fee Related CN2623323Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 03227844 CN2623323Y (en) 2003-06-09 2003-06-09 High efficiency ultrafiltration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 03227844 CN2623323Y (en) 2003-06-09 2003-06-09 High efficiency ultrafiltration device

Publications (1)

Publication Number Publication Date
CN2623323Y true CN2623323Y (en) 2004-07-07

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 03227844 Expired - Fee Related CN2623323Y (en) 2003-06-09 2003-06-09 High efficiency ultrafiltration device

Country Status (1)

Country Link
CN (1) CN2623323Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101658762B (en) * 2009-09-21 2011-12-21 江苏金山环保工程集团有限公司 Hollow fiber ultrafiltration membrane filter device
CN101543689B (en) * 2009-03-30 2012-03-14 刘仁军 Active composite ceramic membrane purifier
CN107311374A (en) * 2017-05-30 2017-11-03 毛强平 The Zero-discharge treating process and device of a kind of coal chemical industrial waste water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101543689B (en) * 2009-03-30 2012-03-14 刘仁军 Active composite ceramic membrane purifier
CN101658762B (en) * 2009-09-21 2011-12-21 江苏金山环保工程集团有限公司 Hollow fiber ultrafiltration membrane filter device
CN107311374A (en) * 2017-05-30 2017-11-03 毛强平 The Zero-discharge treating process and device of a kind of coal chemical industrial waste water
CN107311374B (en) * 2017-05-30 2020-02-07 苏州新能环境技术股份有限公司 Zero-emission treatment process and device for coal chemical industry wastewater

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20040707

Termination date: 20110609