CN204298113U - Improve the structure of RO counter-infiltration diaphragm utilization rate and flux - Google Patents
Improve the structure of RO counter-infiltration diaphragm utilization rate and flux Download PDFInfo
- Publication number
- CN204298113U CN204298113U CN201420722649.XU CN201420722649U CN204298113U CN 204298113 U CN204298113 U CN 204298113U CN 201420722649 U CN201420722649 U CN 201420722649U CN 204298113 U CN204298113 U CN 204298113U
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- CN
- China
- Prior art keywords
- reverse osmosis
- osmosis membrane
- central tube
- diaphragm
- layers
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- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
A kind of RO reverse osmosis membrane structure improving diaphragm utilization rate and flux, comprise central tube, also comprise some layers of RO reverse osmosis membrane, RO reverse osmosis membrane comprises the filter cloth, primary diaphragm, filter screen and the secondary diaphragm that are superimposed together successively, one end of some layers of RO reverse osmosis membrane is connected with the sidewall of central tube, the other end of some layers of RO reverse osmosis membrane rolls together centered by central tube, is provided with some water inlet structures between two-layer RO reverse osmosis membrane adjacent on central tube.The utility model is owing to have employed some layers of RO reverse osmosis membrane, and RO reverse osmosis membrane structural rate skim structure of the prior art adds water flow; And in the process of filtering, define cross-flow filtration,? improve strainability and the salt rejection rate of RO reverse osmosis membrane structure, have saved resource, reduced living cost, good filtration effect, salt rejection rate and water yield advantages of higher.
Description
Technical field
The utility model belongs to clean water treatment technical field, particularly relates to a kind of structure improving RO counter-infiltration diaphragm utilization rate and flux.
Background technology
Purified water machine is in the market after adopting filter to filter running water, again by RO reverse osmosis membrane hydrotreater pure water, RO reverse osmosis membrane hydrotreater is the core component in purified water machine, and the water effect processed of purified water machine is directly related with the water efficiency processed of RO reverse osmosis membrane hydrotreater.But existing its structure of RO reverse osmosis membrane is simple, salt rejection rate and water flow lower, filter effect is undesirable.And after RO reverse osmosis membrane is damaged, is all directly whole RO reverse osmosis membrane is lost, so just causes the waste of resource.
Utility model content
In order to overcome the problems referred to above, the structure of the raising RO counter-infiltration diaphragm utilization rate that the utility model provides a kind of good filtration effect, salt rejection rate and water yield high to society and flux.
The technical solution of the utility model is: provide a kind of structure improving RO counter-infiltration diaphragm utilization rate and flux, comprise central tube, also comprise some layers of RO reverse osmosis membrane, described RO reverse osmosis membrane comprises the filter cloth, primary diaphragm, filter screen and the secondary diaphragm that are superimposed together successively, one end of some layers described RO reverse osmosis membrane is connected with the sidewall of described central tube, the other end of some layers described RO reverse osmosis membrane rolls together centered by described central tube, is provided with some water inlet structures between two-layer described RO reverse osmosis membrane adjacent on described central tube.
As to improvement of the present utility model, one end of some layers described RO reverse osmosis membrane is distributed on the sidewall of described central tube symmetrically.
As to improvement of the present utility model, described water inlet structure is inlet opening.
As to improvement of the present utility model, described water inlet structure is intake chamber.
As to improvement of the present utility model, one end of described filter cloth is welded on the sidewall of described central tube.
As to improvement of the present utility model, described primary diaphragm and described secondary diaphragm shift to install in the both sides of described filter screen.
The utility model is owing to have employed some layers of RO reverse osmosis membrane, RO reverse osmosis membrane comprises the filter cloth, primary diaphragm, filter screen and the secondary diaphragm that are superimposed together successively, in same film area situation, RO reverse osmosis membrane structural rate skim structure of the prior art adds water flow; And in the process of filtering, define cross-flow filtration, improve strainability and the salt rejection rate of RO reverse osmosis membrane structure, RO reverse osmosis membrane is arranged on the sidewall of central tube by fixing female end and fixing male end, have saved resource, reduced living cost, good filtration effect, salt rejection rate and water yield advantages of higher.
Accompanying drawing explanation
Fig. 1 is perspective view when RO reverse osmosis membrane launches in the utility model.
Fig. 2 is the schematic top plan view that the RO reverse osmosis membrane in Fig. 1 is arranged on central tube.
Wherein: 1. central tube; 11. water inlet structures; 2.RO reverse osmosis membrane; 21. filter clothes; 22. primary diaphragms; 23. filter screens; 24. secondary diaphragms.
Detailed description of the invention
Refer to Fig. 1 and Fig. 2, what Fig. 1 and Fig. 2 disclosed is a kind of structure improving RO counter-infiltration diaphragm utilization rate and flux, comprise central tube 1, also comprise some layers of RO reverse osmosis membrane 2, one end of some layers described RO reverse osmosis membrane 2 is connected with the sidewall of described central tube 1, the other end of some layers described RO reverse osmosis membrane 2 rolls together centered by described central tube 1, thus forms filter core.Some layers described RO reverse osmosis membrane 2 rolls to same direction, is provided with some water inlet structures 11 between two-layer described RO reverse osmosis membrane 2 adjacent on described central tube 1.
In the present embodiment, described RO reverse osmosis membrane 2 comprises the filter cloth 21, primary diaphragm 22, filter screen 23 and the secondary diaphragm 24 that are superimposed together successively, described primary diaphragm 22 and described secondary diaphragm 24 shift to install the both sides at described filter screen 23, and namely the length of described primary diaphragm 22 is less than the length of described secondary diaphragm 24.When rolling, described primary diaphragm 22 is in inner side, described secondary diaphragm 24 is in outside, like this after having rolled, one end away from described central tube 1 of described primary diaphragm 22 and the alignment of the one end away from described central tube 1 of described secondary diaphragm 24, namely the length of described primary diaphragm 22 one end is equal with the length of described secondary diaphragm 24 one end.The benefit of such design economizes on resources, and improves the utilization rate of described RO reverse osmosis membrane 2.
In the present embodiment, one end of described filter cloth 21 is welded on the sidewall of described central tube 1, and described water inlet structure 11 is that inlet opening is or/and intake chamber.One end of some layers described RO reverse osmosis membrane 2 is distributed on the sidewall of described central tube 1 symmetrically.
In the present embodiment, the fixing male end also comprising fixing female end and coordinate with described fixing female end, described fixing male end is fixedly connected with one end of described RO reverse osmosis membrane 2, and described fixing female end is arranged on the sidewall of described central tube 1.The benefit of such design is, be easy for installation and removal described RO reverse osmosis membrane 2, when described RO reverse osmosis membrane 2 damages, can change damage with new described RO reverse osmosis membrane 2, has saved resource and has reduced living cost.Described fixing female end is hole clipping or chute, and described fixing male end is protruding buckle or slide block.And user according to the demand of oneself, can increase or reduce the number of plies of described RO reverse osmosis membrane 2.
The utility model, the salt rejection rate that improve and the flow adding water, in same film area situation, a described RO reverse osmosis membrane structural rate skim of the prior art structure in the utility model adds water flow (in identical diaphragm area situation, RO reverse osmosis membrane 2 described in many increases one deck, just increases by the water flow of 18%).And in the process of filtering, define cross-flow filtration, water needs through described filter screen 23, described primary diaphragm 22, described secondary diaphragm 24 and described filter cloth 21, then flows to described central tube 1 from described water inlet structure 11, finally water outlet from described central tube 1.When through described filter screen 23 and described filter cloth 21, water is not that straight line is walked, it needs the shape along described filter screen 23 and described filter cloth 21 to turn back to pass through, benefit is that water increases through the route of described primary diaphragm 22 and described secondary diaphragm 24, namely contact area is equivalent to many, water so through the filtration of described primary diaphragm 22 and described secondary diaphragm 24 is also just many, improves the strainability of described RO reverse osmosis membrane structure.
Described RO reverse osmosis membrane structure also has the effect extending resistance, when the described RO reverse osmosis membrane 2 of some layers rolls together, described in top view during described RO reverse osmosis membrane structure, can find that described filter screen 23 and described filter cloth 21 are clipped between described primary diaphragm 22 and described secondary diaphragm 24 respectively, form hollow, for choked flow, namely the water inlet end of described RO reverse osmosis membrane structure makes water stop on primary diaphragm 22 and described secondary diaphragm 24 to filter, simultaneously because choked flow effect makes hydraulic pressure increase, salt rejection rate also can promote accordingly (pressure influence strainability, the larger filter effect of pressure is quite a lot of), water side choked flow forms water and filters further in described primary diaphragm 22 and described secondary diaphragm 24, there is adsorption function on the surface of described primary diaphragm 22 and described secondary diaphragm 24, can to the further impurity absorption of water.
Claims (6)
1. one kind is improved the structure of RO counter-infiltration diaphragm utilization rate and flux, comprise central tube, it is characterized in that: also comprise some layers of RO reverse osmosis membrane, described RO reverse osmosis membrane comprises the filter cloth, primary diaphragm, filter screen and the secondary diaphragm that are superimposed together successively, one end of some layers described RO reverse osmosis membrane is connected with the sidewall of described central tube, the other end of some layers described RO reverse osmosis membrane rolls together centered by described central tube, is provided with some water inlet structures between two-layer described RO reverse osmosis membrane adjacent on described central tube.
2. the structure of raising RO counter-infiltration diaphragm utilization rate according to claim 1 and flux, is characterized in that: one end of some layers described RO reverse osmosis membrane is distributed on the sidewall of described central tube symmetrically.
3. the structure of raising RO counter-infiltration diaphragm utilization rate according to claim 1 and 2 and flux, is characterized in that: described water inlet structure is inlet opening.
4. the structure of raising RO counter-infiltration diaphragm utilization rate according to claim 1 and 2 and flux, is characterized in that: described water inlet structure is intake chamber.
5. the structure of raising RO counter-infiltration diaphragm utilization rate according to claim 1 and 2 and flux, is characterized in that: one end of described filter cloth is welded on the sidewall of described central tube.
6. the structure of raising RO counter-infiltration diaphragm utilization rate according to claim 1 and 2 and flux, is characterized in that: described primary diaphragm and described secondary diaphragm shift to install in the both sides of described filter screen.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420722649.XU CN204298113U (en) | 2014-11-27 | 2014-11-27 | Improve the structure of RO counter-infiltration diaphragm utilization rate and flux |
Applications Claiming Priority (1)
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CN201420722649.XU CN204298113U (en) | 2014-11-27 | 2014-11-27 | Improve the structure of RO counter-infiltration diaphragm utilization rate and flux |
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CN204298113U true CN204298113U (en) | 2015-04-29 |
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CN201420722649.XU Expired - Fee Related CN204298113U (en) | 2014-11-27 | 2014-11-27 | Improve the structure of RO counter-infiltration diaphragm utilization rate and flux |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110893A (en) * | 2016-07-04 | 2016-11-16 | 佛山市麦克罗美的滤芯设备制造有限公司 | Water saving membrane component and filtration thereof |
CN111203102A (en) * | 2016-08-29 | 2020-05-29 | 佛山市美的清湖净水设备有限公司 | A many membrane page filter cores that is used for center tube of filter core and has it |
-
2014
- 2014-11-27 CN CN201420722649.XU patent/CN204298113U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110893A (en) * | 2016-07-04 | 2016-11-16 | 佛山市麦克罗美的滤芯设备制造有限公司 | Water saving membrane component and filtration thereof |
CN111203102A (en) * | 2016-08-29 | 2020-05-29 | 佛山市美的清湖净水设备有限公司 | A many membrane page filter cores that is used for center tube of filter core and has it |
CN111203102B (en) * | 2016-08-29 | 2022-02-22 | 佛山市美的清湖净水设备有限公司 | A many membrane page filter cores that is used for center tube of filter core and has it |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150429 Termination date: 20211127 |
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CF01 | Termination of patent right due to non-payment of annual fee |