CN201613112U - Novel flat plate type membrane component - Google Patents
Novel flat plate type membrane component Download PDFInfo
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- CN201613112U CN201613112U CN2010200036212U CN201020003621U CN201613112U CN 201613112 U CN201613112 U CN 201613112U CN 2010200036212 U CN2010200036212 U CN 2010200036212U CN 201020003621 U CN201020003621 U CN 201020003621U CN 201613112 U CN201613112 U CN 201613112U
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- lamina membranacea
- filter
- membrane
- membrane module
- support lamina
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Abstract
The utility model relates to a novel flat plate type membrane component which comprises filter membranes and a support membrane plate used for fixing the filter membranes, wherein the support membrane plate forms a hollow inner cavity by clamping and buckling a side frame, a front mesh plate and a rear mesh plate; filter meshes which are densely distributed are uniformly arranged on the front side surface and the rear side surface of the support membrane plate; the filter membranes are fixedly arranged on the two side surface through the sticking way or the welding way; membrane holes on the filter membranes are communicated with the hollow inner cavity via the meshes on the support membrane plate; a flow guide region is arranged in the hollow inner cavity; and an outflowing nozzle which is communicated with the flow guide region is arranged at one end of the support membrane plate. During the application, liquid is infiltrated from the surface of the filter membranes under the action of negative pressure of a self-priming pump or positive pressure of a filtered mixed solution pressure head, penetrates the meshes of the support membrane plate, enters into the hollow inner cavity, is collected into an outflowing groove via the flow guide region and flows out from the outflowing nozzle, thereby realizing the whole filtration process. The membrane component is characterized by easy processing, high utilization rate of the membranes, uniform distribution of the pressure in the cavity and the like, is easy to assemble into membrane components in various forms and is applicable to the fields of industrial filtration and water treatment.
Description
Technical field
The utility model relates to the filter element of membrane separation device, specifically is flat sheet membrane and the support sheet membrane module that lamina membranacea constituted, and belongs to the membrane separation technique field.
Background technology
Membrane separation technique has separation, concentrates, purifying and multiple function such as refining, have concurrently efficient, energy-saving and environmental protection, molecular level filtration and simple structure, easy and simple to handle, be easy to characteristics such as control.Be widely used in water treatment and food, medicine, biology, chemical industry, metallurgy, biology, the energy, oil, electronics, industrial circle such as bionical at present, become in the industrial production the most effectively one of separation means.Select suitable film separation process, can substitute traditional separation and filter methods such as drum-type vacuum filtration, plate compression, ion-exchange, ion isolation, dust removal by filtration, absorption/regeneration, flocculation/copolymerization, decant/precipitation, evaporation, crystallization.
Filter element minimum in the film filter is called sheet membrane module, it is the basis of filter overall performance performance, also be the key problem in technology of realizing good filter effect, the good fit combination property that directly has influence on filter between membrane material and its mechanical support.
Flat milipore filter and micro-filtration membrane owing to have intensity height, flux stabilized, be easy to advantage such as cleanings, become the membrane technology field and use and development ten minutes membrane material rapidly.At present, the flat-sheet membrane module that is widely used is that membrane material is bonded in the support lamina membranacea both sides that the surface is provided with the groove that confluxes, and layer of non-woven fabric is set as permeable medium between support lamina membranacea and membrane material.Filtered fluid sees through membrane material and flows along the surface of plastics lamina membranacea under swabbing action, until being flowed to flow-out hole.The type sheet membrane module is in actual moving process, because the pressure differential that suction pump produces can make membrane material be close to the surface of supporting lamina membranacea, causes filtration resistance to increase, and causes the decline of filtering the constituent element permeability rate, thereby influences effective flux of film.Even under the situation of nonwoven, can not eliminate the influence that its resistance causes fully as the water conservancy diversion media.In addition, because it is very big to support the filter area of lamina membranacea, the suction eye suction only is set at one end, very easily cause filtering surface pressure differential skewness, each regional real fluxes difference is obvious, even channel occurs and filter the dead angle phenomenon, thereby has reduced the filter efficiency of sheet membrane module.Use the support lamina membranacea of the type, the actual membrane flux is relatively low, film takes place easily pollute, and has shortened the cleaning and the replacement cycle of film.Plate type membrane assembly is rectangular slab frame structure at present, is fixedly mounted on the support, in the running, rely on aeration to wash away the on-line cleaning that membrane material is realized on the film surface, cleaning method is single, and efficient is low, and the energy consumption height need carry out Chemical cleaning in than the short period.
Summary of the invention
The purpose of this utility model is intended to overcome the deficiency that prior art exists, and a kind of novel flat-sheet membrane module is provided, to solve technical disadvantages such as conventional film constituent element filtration resistance is big, pressure distribution is inhomogeneous, the on-line cleaning means are single.
The purpose of this utility model is achieved through the following technical solutions:
A kind of novel flat-sheet membrane module, comprise filter membrane and the support lamina membranacea that is used for fixing filter membrane, the support lamina membranacea is a stereochemical structure, characteristics are: described support lamina membranacea comprises two mesh plates of frame and front and back, the two mesh plate clips in described frame and front and back form hollow cavity, on support lamina membranacea two sides, be fixed with filter membrane by stickup or welding manner, the mesh of fenestra on the filter membrane through supporting on the lamina membranacea communicates with hollow cavity, hollow cavity inside is provided with the water conservancy diversion district, and is provided with the spout that communicates with the water conservancy diversion district at support lamina membranacea one end.
Further, above-mentioned a kind of novel flat-sheet membrane module, wherein, the rectangular structure of described support lamina membranacea, sector structure, trapezium structure, cirque structure or impeller shape structure are evenly distributed with hexagon, circle or square filter mesh on the leading flank of support lamina membranacea and the trailing flank.
Further, above-mentioned a kind of novel flat-sheet membrane module, wherein, the mesh plate and the frame matching surface of two sides are staircase structural model before and after the described support lamina membranacea, and frame is provided with filter membrane stickup band.
Again further, above-mentioned a kind of novel flat-sheet membrane module, wherein, the hollow cavity of described support lamina membranacea is provided with several strengthening rib strips and positioning pillars, and strengthening rib strip is divided into several water conservancy diversion districts with hollow cavity.
The substantive distinguishing features of technical solutions of the utility model and progressive being mainly reflected in:
Characteristics such as that the utility model flat-sheet membrane module has is simple in structure, in light weight, effective filtration area big, cavity pressure is evenly distributed, realize the online anti-cleaning of air water mode by the cavity that supports lamina membranacea, significantly delay the Chemical cleaning cycle of membrane module, effectively reduce the film pollution level, help prolonging the service life of membrane material, be particularly suitable for water treatment and industrial separation field.
Description of drawings
Below in conjunction with accompanying drawing technical solutions of the utility model are described further:
Fig. 1: the structural representation of the utility model sheet membrane module;
Fig. 2 a: the master who supports lamina membranacea looks schematic diagram;
Fig. 2 b: the generalized section that supports lamina membranacea;
Fig. 3 a: support membrane intralamellar part structural representation;
Fig. 3 b: mesh plate structural representation;
Fig. 4: schematic diagram is used in the installation of the utility model sheet membrane module.
The implication of each Reference numeral sees the following form among the figure:
| Reference numeral | Implication | Reference numeral | Implication | Reference numeral | Implication |
| 1 | Sheet membrane module | 2 | |
3 | Support lamina membranacea |
| 4 | |
5 | Frame | 6 | |
| 7 | |
8 | |
9 | |
| 10 | Locating |
11 | Reference column | 12 | The water |
| 13 | Go out to flow |
14 | |
15 | |
| 16 | Cross over pipe | 17 | The hole of confluxing | 18 | Membrane module |
The specific embodiment
As shown in Figure 1, novel flat-sheet membrane module 1 comprises filter membrane 2 and the support lamina membranacea 3 that is used for fixing filter membrane.Supporting lamina membranacea 3 is stereochemical structure, shown in Fig. 2 a, 2b, supporting lamina membranacea 3 is made of with frame 5 leading flank and trailing flank mesh plate 4, two mesh plates in front and back, 4 parallel clips form hollow cavities 6, evenly be provided with densely covered filter mesh 7 on the mesh plate 4 of two sides, front and back, be provided with the filter membrane stickup on the two sides of frame 5 and be with 8, so that paste filter membrane in the two sides, front and back of lamina membranacea, make sheet membrane module have the bilateral filtering function, improve the loading density of filter membrane.As Fig. 3 a, 3b, a side mesh plate is provided with several strengthening rib strips 9 in the hollow cavity, and strengthening rib strip 9 is in order to improve to support the intensity of lamina membranacea, avoids sheet membrane module to produce in the dynamic filtration process being out of shape or is crushed.Have locating hole 10 on the strengthening rib strip 9, the opposite side mesh plate is provided with and the corresponding reference column 11 of locating hole, both tight clips play the location and support the effect of two mesh plates in front and back, and strengthening rib strip 9 is divided into several filtered fluid water conservancy diversion districts 12 (being divided into 4 water conservancy diversion districts among the figure) with hollow cavity simultaneously.Two sides, front and back stickup along lamina membranacea frame 5 is with 8, is fixed with filter membrane 2 by stickup or welding manner, and the filter membrane of both sides is by pasting band and frame 5 realization sealing and fixing.Fenestra on the filter membrane communicates with filter mesh 7 on the mesh plate of both sides, be provided with in the bottom of lamina membranacea frame 5 communicate with each water conservancy diversion district of hollow cavity go out to flow groove 13 and spout 14.
The typical structure form of above-mentioned new membrane constituent element is, support the rectangular structure of lamina membranacea, be distributed with cellular hexagon filter mesh on the leading flank of lamina membranacea and the trailing flank, lamina membranacea is as the mechanical support element of filter membrane, staircase structural model is adopted on the plane that lamina membranacea frame and mesh plate are formed, lamina membranacea outer rim gross thickness is 6mm, and the recessed 0.5mm of inner side step face keeps in one plane with mesh plate.Stickup bandwidth 4.5mm on the lamina membranacea frame is texture structure, adopts welding manners such as glue or ultrasonic wave that the filter membrane sealing is pasted along pasting band, guarantees around the stickup band of lamina membranacea frame water-tight under operating pressure.The two mesh plate clips in front and back form hollow cavities, and the chamber inner height is 1.5mm, and the mesh plate surface is filtered film and covers, and are that band is pasted in the sealing on the frame all around, the spout that the setting of lamina membranacea bottom communicates with cavity.
This novel flat-sheet membrane module is made up of plastic support lamina membranacea and filter membrane material such as micro-filtration, ultrafiltration usually, support the closed space that the lamina membranacea two sides forms a hollow by filter membrane material being pasted or being welded on, the mesh plate of two sides plays the effect of supporting filter membrane.In the negative pressure of self priming pump or filter under the positive pressure of mixed liquor pressure head, filtered fluid infiltrates from the film surface, and the mesh that passes lamina membranacea enters into hollow cavity, imports out the stream groove through each water conservancy diversion district again, flows out from spout then, finishes whole filter operation process.The geometry of sheet membrane module can change according to practical application is different, comprises rectangular configuration, sector structure, trapezium structure, cirque structure or impeller shape structure etc.
Its support lamina membranacea of traditional flat-sheet membrane module adopts the Surface Groove mode usually, by behind the film surface, liquid imports passage all around through supporting the little groove of lamina membranacea surface detail, is discharged by spout then at filtered fluid, pressure is difficult to realize evenly distributing, and filters the dead band membrane flux is exerted an influence.The utility model is different with traditional flat-sheet membrane module, the new membrane constituent element adopts the filter operation of hollow cavate, strengthening rib strip and reference column in the cavity are played a supporting role to two lamina membranaceas in front and back, under the operating pressure of setting, lamina membranacea can not deform even interior flat because of pressurized, well the holding chamber inner flow passage is unobstructed, effectively reduces the sensitiveness of filter membrane to stopping up.Cover the filter membrane on mesh plate surface, because of mesh plate has high percent opening, make filter membrane and hollow cavity realize directly communicating, can not form flow blind angle and inner lead behind the filter membrane pressurized with supporting the lamina membranacea bonding, phenomenons such as the surperficial channel that therefore can effectively avoid very easily taking place in the classic flat-plate formula sheet membrane module, short circuit, bonding, dead band, keep membrane flux stable, improve the filter efficiency of sheet membrane module.Simultaneously, sheet membrane module adopts the hollow cavity structure that extremely is helped realizing online backwash, slows down the pollution that penetrant produces filter membrane, prolongs the Chemical cleaning cycle, reduces the complicated property of film lock out operation, increases work efficiency.In addition, the hollow cavity structure also can improve the loading density of filter membrane to a certain extent, and conserve space reduces cost.
Generally, sheet membrane module adopts the mode of multi-disc parallel connection to use, as shown in Figure 4, by assembly hole 15 and cross over pipe 16 several sheet membrane module 1 parallel connections are assembled into membrane module 18, in the negative pressure of self priming pump or filter under the positive pressure of mixed liquor pressure head, the filtered fluid of each sheet membrane module enters into cross over pipe 16 by its spout 14 and discharges by the hole 17 of confluxing.Sheet membrane module 1 can be the horizontal layout form with cross over pipe 16, gap between each sheet membrane module 1 is provided with according to the characteristic of filter membrane loading density needs and filtered fluid, support lamina membranacea 3 and adopt thermoplastic to make, by forming the filtered fluid passage between spout 14 and the cross over pipe 16.Spout 14 sealings of supporting on the lamina membranacea 3 assign on the cross over pipe 16, fit together by assembly hole 15 between the lamina membranacea and are connected with cross over pipe 16.
The membrane module that adopts this novel flat-sheet membrane module to make need not setting and is flexible coupling or other seal, has significantly reduced the leakage link, and device structure is simple, and processing and easy for installation is easy to maintenance and lamina membranacea and changes.Several that on cross over pipe, offered hole of confluxing, it is unique link that realization is tightly connected between sheet membrane module and the cross over pipe, usually adopt modes such as plain washer, fluid sealant, welding can reach sealing purpose, for realizing excellent sealing, whole filtration system provides convenience, very help the service life of membrane component and prolong, also can effectively reduce the possibility that too much causes the filtered fluid secondary pollution because of connecting link simultaneously.
It is emphasized that, new membrane constituent element and the membrane module of making therefrom, be applicable to the membrane filtration material such as ultrafiltration, micro-filtration of different apertures and characteristic, can conveniently realize the separation of solidliquid mixture such as particle, colloid, microorganism and molecular level mixture, the medium that filters mixed liquor comprises water or other liquid substances.According to the medium of filtering mixt and the specific requirement of concentrate type, character and industrialization operation, the utility model can be done the adaptability change according to actual needs on size, shape, filter operation mode, also can reduce or increase the length of the distance between the sheet membrane module and the connecting piece that confluxes, sheet membrane module can be selected connected mode flexibly with airtight combination of connecting piece.Main range of application of the present utility model comprises:
1) the utility model hollow cavate sheet membrane module can be applicable to the manufacturing of membrane separation plants such as industrial material separation, product purification, water treatment, replace precipitation, clarification in the industrial separation operation, concentrate, traditional handicraft such as filtration, significantly improve filter effect, reduce the complicated property of filter operation; Its membrane module can combine with coagulation and the biochemical processing method in the water treatment, substitutes present widely used sedimentation processing technology, and the suspended particulate substance in the efficient trap water, colloid, big molecule, bacterium and biological substance reach desirable water outlet effect;
2) adopt the membrane filtration material in nanofiltration or other similar apertures, the utility model can be applicable to the membrane separation plant manufacturing that is used to remove molecular level impurity and bacterium, virus etc. in the water treatment; The membrane module that adopts ultrafiltration or similar aperture filter membrane to make has the bigger potentiality of applying in fields such as drinking water treatment, reusing sewage processing, high-purity industrial water supplies;
3) adopt micro-filtration or other more wide-aperture filtering materials, the utility model can apply to the manufacturing of industrial separation equipment such as food, medicine, biology, chemical industry easily, substitute methods such as traditional precipitate and separate, vacuum filtration, plate compression, centrifugation, have simple to operate, clean outstanding advantages such as convenience, efficient energy-saving, environmental protection.
In sum, unique, the novel structure of the utility model design has overcome technological deficiencies such as classic flat-plate formula sheet membrane module filtration resistance is big, pressure distribution is inhomogeneous, the on-line cleaning means are single.That the sheet membrane module of hollow cavate has is simple in structure, handling ease, in light weight, consumptive material is few, the lamina membranacea surface pressure distribution evenly, do not have characteristics such as the dead band of filtration, filtration flux be stable, its membrane module simple installation, the leakage link of device is few, can conveniently realize the diversification on-line cleaning, the Chemical cleaning cycle of significant prolongation system and the service life of membrane material, for the popularization of membrane technology provides a kind of effective new method, be expected at industrial separation and water treatment field has application prospects.
Below only be concrete exemplary applications of the present utility model, protection domain of the present utility model is not constituted any limitation.Innovation part of the present utility model is the filter type of flat panel filter film is carried out with the hollow cavate, thereby optimize the filter operation process and improve membrane filtration efficient, the formation method comprises the supporting construction that employing is different, also comprises the method for using porous aggregate to form approximate cavity.All employing equivalents or equivalence are replaced and the technical scheme of formation, all drop within the utility model rights protection scope.
Claims (4)
1. novel flat-sheet membrane module, comprise filter membrane and the support lamina membranacea that is used for fixing filter membrane, the support lamina membranacea is a stereochemical structure, it is characterized in that: described support lamina membranacea comprises two mesh plates of frame and front and back, the two mesh plate clips in described frame and front and back form hollow cavity, on support lamina membranacea two sides, be fixed with filter membrane by stickup or welding manner, the mesh of fenestra on the filter membrane through supporting on the lamina membranacea communicates with hollow cavity, hollow cavity inside is provided with the water conservancy diversion district, and is provided with the spout that communicates with the water conservancy diversion district at support lamina membranacea one end.
2. a kind of novel flat-sheet membrane module according to claim 1, it is characterized in that: the rectangular structure of described support lamina membranacea, sector structure, trapezium structure, cirque structure or impeller shape structure are evenly distributed with filter mesh on the leading flank of support lamina membranacea and the trailing flank.
3. a kind of novel flat-sheet membrane module according to claim 1 is characterized in that: the mesh plate and the frame matching surface of two sides are staircase structural model before and after the described support lamina membranacea, and frame is provided with filter membrane stickup band.
4. a kind of novel flat-sheet membrane module according to claim 1 is characterized in that: the hollow cavity of described support lamina membranacea is provided with several strengthening rib strips and positioning pillars, and strengthening rib strip is divided into several water conservancy diversion districts with hollow cavity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200036212U CN201613112U (en) | 2010-01-12 | 2010-01-12 | Novel flat plate type membrane component |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200036212U CN201613112U (en) | 2010-01-12 | 2010-01-12 | Novel flat plate type membrane component |
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| CN201613112U true CN201613112U (en) | 2010-10-27 |
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|---|---|---|---|
| CN2010200036212U Expired - Fee Related CN201613112U (en) | 2010-01-12 | 2010-01-12 | Novel flat plate type membrane component |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103395878A (en) * | 2013-06-29 | 2013-11-20 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of split-type combined membrane bioreactor |
| CN103395877A (en) * | 2013-06-29 | 2013-11-20 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of one-piece combined membrane bioreactor |
| CN105107383A (en) * | 2015-08-31 | 2015-12-02 | 成都易态科技有限公司 | Liquid filter membrane component |
| CN107413198A (en) * | 2017-06-01 | 2017-12-01 | 成都易态科技有限公司 | The filter of filtering film component and its composition |
-
2010
- 2010-01-12 CN CN2010200036212U patent/CN201613112U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103395878A (en) * | 2013-06-29 | 2013-11-20 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of split-type combined membrane bioreactor |
| CN103395877A (en) * | 2013-06-29 | 2013-11-20 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of one-piece combined membrane bioreactor |
| CN103395878B (en) * | 2013-06-29 | 2015-04-29 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of split-type combined membrane bioreactor |
| CN103395877B (en) * | 2013-06-29 | 2015-06-03 | 北京工业大学 | Method and apparatus for nitration and nitrate nitrogen enrichment of one-piece combined membrane bioreactor |
| CN105107383A (en) * | 2015-08-31 | 2015-12-02 | 成都易态科技有限公司 | Liquid filter membrane component |
| CN107413198A (en) * | 2017-06-01 | 2017-12-01 | 成都易态科技有限公司 | The filter of filtering film component and its composition |
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Owner name: SHANGHAI MARITIME UNIV. Free format text: FORMER OWNER: SUZHOU 3R TECHNOLOGY CO., LTD. Effective date: 20130711 Free format text: FORMER OWNER: SHANGHAI MARITIME UNIV. Effective date: 20130711 |
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Owner name: SUZHOU 3R TECHNOLOGY CO., LTD. Free format text: FORMER NAME: SUZHOU INDUSTRY PARK YINUOKE ENVIRONMENTAL TECHNOLOGY CO., LTD. |
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Free format text: CORRECT: ADDRESS; FROM: 215021 SUZHOU, JIANGSU PROVINCE TO: 201306 NANHUI, SHANGHAI |
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Address after: Suzhou City, Jiangsu province 215021 Industrial Park Shen Hu Lu sea lakeside Patentee after: Suzhou three Creole Technology Co.,Ltd. Patentee after: Shanghai Maritime University Address before: Suzhou City, Jiangsu province 215021 Industrial Park Shen Hu Lu sea lakeside Patentee before: Suzhou Industrial Park Yinuoke Environmental Technology Co.,Ltd. Patentee before: Shanghai Maritime University |
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Owner name: SUZHOU MOHAI MEMBRANE TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: SHANGHAI MARITIME UNIV. Effective date: 20130805 |
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Effective date of registration: 20130805 Address after: 215011 No. 209 Chuk Yuen Road, Suzhou hi tech Development Zone, Jiangsu Patentee after: SUZHOU MOHAI SEPARATION TECHNOLOGY CO.,LTD. Address before: 201306 No. 1550 seaport Avenue, Lingang New Town, Shanghai Patentee before: Shanghai Maritime University |
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