CN208583188U - A kind of parallel channels film and its membrane module - Google Patents
A kind of parallel channels film and its membrane module Download PDFInfo
- Publication number
- CN208583188U CN208583188U CN201721749865.3U CN201721749865U CN208583188U CN 208583188 U CN208583188 U CN 208583188U CN 201721749865 U CN201721749865 U CN 201721749865U CN 208583188 U CN208583188 U CN 208583188U
- Authority
- CN
- China
- Prior art keywords
- parallel channels
- film
- parallel
- utility
- model
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of parallel channels film and its membrane modules.The utility model parallel channels film is that a plurality of cylindrical channel is arranged in parallel along same plane, and separating layer outer wall is wrapped up outside above-mentioned a plurality of cylindrical channel.The utility model parallel channels membrane module is that a plurality of parallel channels film is arranged in parallel along its runner direction, and also keeping parallelism arranges between each plane of parallel channels film arrangement, shell is arranged outside a plurality of parallel channels film, shell both ends are poured.The film product of the utility model can effectively avoid the deposition problem between film wire, to improve the antifouling property of film product.
Description
Technical field
The utility model relates to water-treatment technology fields, more specifically, be related to it is a kind of for liquid separation it is parallel
Press mold and its membrane module outside channel.
Background technique
Sewage treatment is carried out using membrane technology, especially hollow-fibre membrane or plate membrane technology, is current sewage treatment neck
The core technology in domain, and the technology being most widely used.For flow channel for liquids, runner generally cylindrical in shape do not have dead angle and
Flow resistance is smaller, and for the runner of other opposite cross sections, liquid flowing is more smooth.Press mold is main outside common cylindrical shaped runner
Form is the outer press mold of doughnut, has been widely used in the fields such as environmental protection and water process at present.
In recent years with the integrated development of membrane technology and other technologies, hollow-fibre membrane product is proposed many new
It is required that.Many fields as associated in membrane technology and biotechnology, for the efficiency for improving sewage treatment, it usually needs improve activity
The concentration of sludge, meanwhile, to meet investment, land occupation and safeguarding simple etc. requirement, and need to shorten entire sewage treatment
The process of technique then simplifies the pre-treatment intake to hollow-fibre membrane.Then, sewage with suspended active sludge is into film
It is easy to form deposition between film wire during filtering, film wire is caused to pollute severe.Although plate membrane is in anti-high sludge
It is more advantageous than hollow-fibre membrane in terms of concentration, but its filling area is smaller, integrated equipment size of the same area is big, maintenance at
This height.
Utility model content
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, is provided a kind of parallel
Channel membrane and its membrane module.
The utility model parallel channels film, is achieved by following technical proposals, and a plurality of cylindrical channel is along same flat
Face is arranged in parallel, and separating layer outer wall is wrapped up outside above-mentioned a plurality of cylindrical channel.
The a plurality of cylindrical channel number is 4-10 item.
The cross-sectional circumference side of the parallel channels film is made of straight line or the mellow and full company by having periodical concaveconvex structure
Continuousization curve is constituted.
The utility model parallel channels membrane module, is achieved by following technical proposals, and a plurality of parallel channels film is along it
Runner direction is arranged in parallel, and also keeping parallelism arranges between each plane of parallel channels film arrangement, a plurality of parallel channels film peripheral hardware
Shell is set, shell both ends are poured.
A plurality of parallel channels film number is 6-12 item.
Compared with prior art, the utility model has the beneficial effects that
Compared with existing doughnut membrane technology, film product described in the utility model can effectively avoid the deposition between film wire
Problem, to improve the antifouling property of film product;Compared with existing plate membrane technology, film product tool described in the utility model
There is higher packed density, to assign equipment higher processing capacity.
Detailed description of the invention
Fig. 1 is the utility model parallel channels film cross section straight-line profile schematic diagram;
Fig. 2 is the utility model parallel channels film cross-section curve appearance schematic diagram;
Fig. 3 is the utility model parallel channels membrane module cross-sectional view.
Specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that this place
The specific embodiment of description is only used to explain the utility model, is not used to limit the utility model.
Parallel channels film is as shown in Figs. 1-2, and a plurality of cylindrical channel is arranged in parallel along same plane, above-mentioned a plurality of cylinder
Separating layer outer wall is wrapped up outside channel.The a plurality of cylindrical channel number is 4-10 item.The cross-sectional circumference of the parallel channels film
While being made of straight line (see Fig. 1) or by having the mellow and full serialization curve of periodical concaveconvex structure to constitute (see Fig. 2).
The parallel channels film is crowded with common solution (or melt) runner exit by managing with parallel core liquid (gas)
Out prepared by die orifice.The solution or melt can be the solution-polymerized SBR or melt spinning film forming feed liquid of different formulations.Fluid squeezes
Using cooling or coagulating bath etc. are solidified, pore-forming obtains after out.
Parallel channels membrane module is as shown in figure 3, a plurality of parallel channels film is arranged in parallel along its runner direction, parallel channels film
Also keeping parallelism arranges between each plane of arrangement, shell is arranged outside a plurality of parallel channels film, shell both ends are poured.It is a plurality of
Parallel channels film number is 6-12 item.
The membrane module its water inlet, produce water and concentrated water direction should all be parallel with press mold outside parallel channels.
The above is only the preferred embodiment of the utility model, it is noted that for the general of the art
For logical technical staff, without departing from the principle of this utility model, several improvements and modifications can also be made, these change
It also should be regarded as the protection scope of the utility model into retouching.
Claims (4)
1. a kind of parallel channels film, characterized in that a plurality of cylindrical channel is arranged in parallel along same plane, above-mentioned a plurality of cylinder
Separating layer outer wall is wrapped up outside channel, the cross-sectional circumference side of the parallel channels film is made of straight line or by having periodically bumps
The mellow and full serialization curve of structure is constituted.
2. parallel channels film according to claim 1, characterized in that a plurality of cylindrical channel number is 4-10 item.
3. a kind of parallel channels membrane module, characterized in that a plurality of parallel channels film described in claim 1 is flat along its runner direction
Row arranges, and also keeping parallelism arranges between each plane of parallel channels film arrangement, and shell, shell are arranged outside a plurality of parallel channels film
Both ends are poured.
4. parallel channels membrane module according to claim 3, characterized in that a plurality of parallel channels film number is 6-12 item.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721749865.3U CN208583188U (en) | 2017-12-15 | 2017-12-15 | A kind of parallel channels film and its membrane module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721749865.3U CN208583188U (en) | 2017-12-15 | 2017-12-15 | A kind of parallel channels film and its membrane module |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208583188U true CN208583188U (en) | 2019-03-08 |
Family
ID=65531813
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721749865.3U Active CN208583188U (en) | 2017-12-15 | 2017-12-15 | A kind of parallel channels film and its membrane module |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208583188U (en) |
-
2017
- 2017-12-15 CN CN201721749865.3U patent/CN208583188U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103657123B (en) | A kind of distributor of horizontal falling film evaporator | |
CN203346151U (en) | Double-layer aeration curtain membrane module | |
CN106006892B (en) | Micro swirl flocculation plant | |
CN104014142B (en) | Efficient liquid distributor for falling-film evaporator | |
CN208583188U (en) | A kind of parallel channels film and its membrane module | |
CN102389712A (en) | External-pressure type hollow fiber ultrafiltration membrane assembly with turbulence promoter structure | |
CN108014645A (en) | A kind of parallel channels film and its membrane module | |
CN206965532U (en) | A kind of Floating aeration coupling curtain type film assembly | |
CN203890487U (en) | Electroplating turbulence device | |
CN206853250U (en) | A kind of multi-stage water purifier of fast-connection filter element | |
CN209552004U (en) | A kind of mold of ceramic membrane idiosome extrusion molding | |
CN202700198U (en) | Self-cleaning composite ceramic filter core | |
CN102383203B (en) | Energy-saving type spinning die head for spinning box | |
CN205360689U (en) | Stationary flow formula settling basin | |
CN205033539U (en) | Injection mold's counter -flow cooling device | |
CN203469581U (en) | Simple filter water tank | |
CN202842128U (en) | Shrimp cultivation pool | |
CN203157093U (en) | Totally-coated double-layer co-extrusion plastic mold | |
CN202599158U (en) | Pure-titanium heat exchanger with vortex water outlet | |
CN203985594U (en) | Variable height sewage discharger | |
CN202410525U (en) | External pressure type hollow fiber membrane ultrafiltration component with anti-pollution structure | |
CN208164263U (en) | A kind of rubber and plastic extruder extruder head | |
CN213610152U (en) | Filter core of installation is invertd in lower business turn over | |
CN104689719A (en) | Air-blast-available external pressure type hollow fiber membrane module with one fixed end | |
CN208857006U (en) | A kind of petroleum wastewater Microbiological Lab processing unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |