CN106268196A - A kind of double-flow membrane separator - Google Patents
A kind of double-flow membrane separator Download PDFInfo
- Publication number
- CN106268196A CN106268196A CN201610960565.3A CN201610960565A CN106268196A CN 106268196 A CN106268196 A CN 106268196A CN 201610960565 A CN201610960565 A CN 201610960565A CN 106268196 A CN106268196 A CN 106268196A
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- CN
- China
- Prior art keywords
- plate
- cylinder
- deflection plate
- membrane separator
- hole
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D2053/221—Devices
- B01D2053/222—Devices with plates
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of double-flow membrane separator, including up-hole plate (1), orifice plate (2) and cylinder (3), set dividing plate (4) and deflection plate (5) in described cylinder (3), cylinder (3) offer contour and set up material mixed steam entrance (6) in both sides, cylinder top and material mixed steam outlet (7) separately.Have an advantage in that: orifice plate is divided into four regions, and after hole is carried out coordinate numbering, the hole that orifice plate is corresponding can be quickly found out, substantially reduce installation, the time safeguarded, overhaul, promote work efficiency；After being changed membrane separator into double-flow by single process, the material time of staying in separator doubles, thus membrane separating effect is substantially improved.
Description
Technical field
The present invention relates to membrane separator technical field, a kind of novel double-flow membrane separator.
Background technology
Existing membrane separator simple in construction, function singleness, the defect existed is as follows:
1, existing orifice plate is loose structure, and each hole, by certain spacing proper alignment, owing to hole is too many, is being installed, safeguards, overhauled
Shi Buyi quick and precisely finds the position that orifice plate is corresponding；
2, material flows into from upper end, membrane separator side, flows out from membrane separator opposite side lower end, the time of staying in separator
Shorter.
Summary of the invention
It is an object of the invention to the deficiency overcoming prior art to exist, it is provided that a kind of rational in infrastructure, raising production efficiency
Double-flow membrane separator.
A kind of double-flow membrane separator, including up-hole plate 1, orifice plate 2 and cylinder 3, sets dividing plate 4 and folding in described cylinder 3
Stream plate 5, cylinder 3 offers contour and sets up the material mixed steam entrance 6 in both sides, cylinder top and the outlet of material mixed steam separately
7。
Insulation jacket 8 it is provided with outside cylinder 3.
Described dividing plate 4 is positioned on the axis of cylinder 3, and top is connected with up-hole plate 1.
Described deflection plate 5 is four pieces, and the first deflection plate 5-1 is positioned at below material mixed steam entrance 6, the 4th deflection plate 5-4
Being positioned at below material mixed steam outlet 7, the first deflection plate 5-1 and the 4th deflection plate 5-4 is relative to dividing plate 4 axisymmetricly；Second
Deflection plate 5-2 and the 3rd deflection plate 5-3 is symmetricly set on dividing plate 4 left and right sides.
Described first deflection plate 5-1 and the 4th deflection plate 5-4 is positioned at 2/3rds height of cylinder 3.
Described second deflection plate 5-2 and the 3rd deflection plate 5-3 is positioned at 1/3rd height of cylinder 3.
Compared with prior art, the beneficial effects of the present invention is:
1, orifice plate is divided into four regions, and after hole is carried out coordinate numbering, the hole that orifice plate is corresponding can be quickly found out, greatly
Shorten greatly installation, the time safeguarded, overhaul, promote work efficiency；
2, after being changed membrane separator into double-flow by single process, the material time of staying in separator doubles, thus greatly
Width promotes membrane separating effect.
Accompanying drawing explanation
Fig. 1 is the structural representation of existing membrane separator.
Fig. 2 is the structural representation of existing membrane separator orifice plate.
Fig. 3 is the overall structure schematic diagram of the present invention.
Fig. 4 is the structural representation of orifice plate of the present invention.
Numeral labelling in figure: 1 is up-hole plate, and 2 is orifice plate, and 3 is cylinder, and 4 is dividing plate, and 5 is deflection plate, 5-1 position first
Deflection plate, 5-2 is second deflection plate the second deflection plate, and 5-3 is the 3rd deflection plate, and 5-4 is the 4th deflection plate, and 6 mix for material
Vapour entrance, 7 export for material mixed steam, and 8 is insulation jacket.
Detailed description of the invention
The present invention will be further described with detailed description of the invention in explanation below in conjunction with the accompanying drawings, but not it is protected model
The restriction enclosed.
As shown in Figure 3, Figure 4, a kind of double-flow membrane separator, including up-hole plate 1, orifice plate 2 and cylinder 3, described cylinder 3
Inside set dividing plate 4 and deflection plate 5, cylinder 3 offer contour and set up the material mixed steam entrance 6 in both sides, cylinder top and thing separately
Material mixed steam outlet 7.
Insulation jacket 8 it is provided with outside cylinder 3.
Described dividing plate 4 is positioned on the axis of cylinder 3, and top is connected with up-hole plate 1.
Described deflection plate 5 is four pieces, and the first deflection plate 5-1 is positioned at below material mixed steam entrance 6, the 4th deflection plate 5-4
Being positioned at below material mixed steam outlet 7, the first deflection plate 5-1 and the 4th deflection plate 5-4 is relative to dividing plate 4 axisymmetricly；Second
Deflection plate 5-2 and the 3rd deflection plate 5-3 is symmetricly set on dividing plate 4 left and right sides.
Described first deflection plate 5-1 and the 4th deflection plate 5-4 is positioned at 2/3rds height of cylinder 3.
Described second deflection plate 5-2 and the 3rd deflection plate 5-3 is positioned at 1/3rd height of cylinder 3.
Deflection plate 5 is tetrafluoroethene material, and deflection plate 5 is provided with hole, ceramic-film tube run through after deflection plate 5 respectively with upper hole
Plate 1, orifice plate 2 are connected.The aperture in the hole set on deflection plate 5 is as ceramic-film tube 1.1 times.
The material of deflection plate 5 is changed into soft polytetrafluoroethylene (PTFE) by hard rustless steel, effectively prevent pottery
By deflection plate 5 scratch in membrane tube installation process；The aperture of deflection plate 5 is narrowed down to closer to ceramic-film tube external diameter, formed more preferably
Baffling effect, at utmost reduce material mixed steam in the short circuit phenomenon of deflection plate 5 interlayer；Change the stream of material mixed steam
Through route, improve the work efficiency of membrane separator.
Claims (6)
1. a double-flow membrane separator, it is characterised in that: include up-hole plate (1), orifice plate (2) and cylinder (3), described cylinder
(3) set dividing plate (4) and deflection plate (5) in, cylinder (3) offer contour and set up the material mixed steam in both sides, cylinder top separately
Entrance (6) and material mixed steam outlet (7).
2. membrane separator as claimed in claim 1, it is characterised in that: cylinder (3) outside is provided with insulation jacket (8).
3. membrane separator as claimed in claim 1, it is characterised in that: described dividing plate (4) is positioned on the axis of cylinder (3),
Top is connected with up-hole plate (1).
4. membrane separator as claimed in claim 1, it is characterised in that: described deflection plate (5) is four pieces, the first deflection plate (5-
1) being positioned at material mixed steam entrance (6) lower section, the 4th deflection plate (5-4) is positioned at material mixed steam outlet (7) lower section, the first baffling
Plate (5-1) and the 4th deflection plate (5-4) are relative to dividing plate (4) axisymmetricly；Second deflection plate (5-2) and the 3rd deflection plate (5-
3) dividing plate (4) left and right sides it is symmetricly set on.
5. membrane separator as claimed in claim 4, it is characterised in that: described first deflection plate (5-1) and the 4th deflection plate (5-
4) it is positioned at 2/3rds height of cylinder (3).
6. membrane separator as claimed in claim 4, it is characterised in that: described second deflection plate (5-2) and the 3rd deflection plate (5-
3) it is positioned at 1/3rd height of cylinder (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610960565.3A CN106268196A (en) | 2016-11-04 | 2016-11-04 | A kind of double-flow membrane separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610960565.3A CN106268196A (en) | 2016-11-04 | 2016-11-04 | A kind of double-flow membrane separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106268196A true CN106268196A (en) | 2017-01-04 |
Family
ID=57719734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610960565.3A Pending CN106268196A (en) | 2016-11-04 | 2016-11-04 | A kind of double-flow membrane separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106268196A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050092683A1 (en) * | 2003-10-31 | 2005-05-05 | Goldsmith Robert L. | Membrane devices for pervaporation, gas separations, and perstraction with permeate and sweep fluid conduit and method of use |
| CN202860416U (en) * | 2012-10-31 | 2013-04-10 | 张锋新 | Shell-and-tube steam permeable membrane component |
| CN203678259U (en) * | 2013-12-24 | 2014-07-02 | 江苏九天高科技股份有限公司 | Tubular membrane component |
| CN203737112U (en) * | 2014-01-16 | 2014-07-30 | 武汉智宏思博化工科技有限公司 | Pervaporation molecular sieve membrane assembly |
| CN203916468U (en) * | 2014-01-16 | 2014-11-05 | 武汉智宏思博化工科技有限公司 | The infiltration evaporation inoranic membrane device that a kind of sealing is good |
| CN204891613U (en) * | 2015-07-20 | 2015-12-23 | 江苏久吾高科技股份有限公司 | Tubular membrane module |
| CN206152587U (en) * | 2016-11-04 | 2017-05-10 | 武汉智宏思博化工科技有限公司 | Double fluid journey membrane separator |
-
2016
- 2016-11-04 CN CN201610960565.3A patent/CN106268196A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050092683A1 (en) * | 2003-10-31 | 2005-05-05 | Goldsmith Robert L. | Membrane devices for pervaporation, gas separations, and perstraction with permeate and sweep fluid conduit and method of use |
| CN202860416U (en) * | 2012-10-31 | 2013-04-10 | 张锋新 | Shell-and-tube steam permeable membrane component |
| CN203678259U (en) * | 2013-12-24 | 2014-07-02 | 江苏九天高科技股份有限公司 | Tubular membrane component |
| CN203737112U (en) * | 2014-01-16 | 2014-07-30 | 武汉智宏思博化工科技有限公司 | Pervaporation molecular sieve membrane assembly |
| CN203916468U (en) * | 2014-01-16 | 2014-11-05 | 武汉智宏思博化工科技有限公司 | The infiltration evaporation inoranic membrane device that a kind of sealing is good |
| CN204891613U (en) * | 2015-07-20 | 2015-12-23 | 江苏久吾高科技股份有限公司 | Tubular membrane module |
| CN206152587U (en) * | 2016-11-04 | 2017-05-10 | 武汉智宏思博化工科技有限公司 | Double fluid journey membrane separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170104 |