CN205109417U - Reverse osmosis membrane's anti - washing unit - Google Patents
Reverse osmosis membrane's anti - washing unit Download PDFInfo
- Publication number
- CN205109417U CN205109417U CN201520899259.4U CN201520899259U CN205109417U CN 205109417 U CN205109417 U CN 205109417U CN 201520899259 U CN201520899259 U CN 201520899259U CN 205109417 U CN205109417 U CN 205109417U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- osmosis membrane
- inlet pipeline
- elevated tank
- main frame
- 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.)
- Expired - Fee Related
Links
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 73
- 239000012528 membrane Substances 0.000 title claims abstract description 37
- 238000005406 washing Methods 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 238000010926 purge Methods 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract 1
- 238000011010 flushing procedure Methods 0.000 description 7
- 238000001764 infiltration Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
Abstract
The utility model provides a reverse osmosis membrane's anti - washing unit, belongs to reverse osmosis equipment technical field for online reverse osmosis membrane to among the reverse osmosis system of water treatment carries out the back flush. Its technical scheme is: at the top of reverse osmosis unit host computer installation high flush tank, high flush tank is connected through the cavity at the reverse osmosis membrane back in back flush water intake pipe and the reverse osmosis unit host computer, installs control flap in back flush water intake pipe and high flush tank water intake pipe respectively, can implement the back flush to reverse osmosis membrane through above -mentioned device. The utility model discloses the in -process that washes is being carried out reverse osmosis membrane, just washing with back flush hocket, can show improvement washing effect, reduce the filth to reverse osmosis membrane's pollution, extension reverse osmosis membrane's cleaning interval, improve reverse osmosis membrane's life, reduction in production cost improves economic benefits. The utility model has the advantages of simple structure, control be convenient, need not to increase power equipment, the running cost is low, there is the fine value of using widely.
Description
Technical field
The utility model relates to a kind of device online reverse osmosis membrane in the counter-infiltration system of water treatment being carried out to backwash, belongs to reverse osmosis equipment technical field.
Background technology
Reverse osmosis technology is because itself being applied to the advanced treating field in sewage disposal just more and more to the stalling characteristic of the excellence of pollutant in water.Usual sewage is still difficult in the water quality after conventional biochemical treatment the influent quality requirement reaching counter-infiltration system, and this just proposes challenge to the application of counter-infiltration system, operation and maintenance.At present, in the prior art, reverse osmosis membrane on-line rinsing all adopts membrane surface flushing, and namely flushing water utilizes flow shear to rinse along face.And the obstinate pollution layer that reverse osmosis membrane is in use formed due to long-term accumulated is attached to film surface; high-velocity flow is only relied on to rinse; be difficult to reach the effect as milipore filter backwash normal shutdown in flushing process; and the distinctive membrane structure of reverse osmosis membrane requires that back pressure must not exceed film producer limit value; otherwise; will cause damage to film, therefore can not adopt the back-flushing method of milipore filter.How effective cleaning is carried out to reverse osmosis membrane and become technical problem urgently to be resolved hurrily at present.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of back purge system of reverse osmosis membrane, this back purge system can realize the backwash to reverse osmosis membrane, reaches to improve developing result, delay dirt to the pollution of reverse osmosis membrane, the object extending the cleaning frequency.
The technical scheme solved the problems of the technologies described above is:
A kind of back purge system of reverse osmosis membrane, it comprises elevated tank, backwash inlet pipeline, elevated tank inlet pipeline, elevated tank is placed on the top of reverse osmosis unit main frame, one end of backwash inlet pipeline is connected with elevated tank, the other end of backwash inlet pipeline is connected to the side of reverse osmosis unit main frame, backwash water intaking valve is installed in backwash inlet pipeline, the water inlet that backwash inlet pipeline is connected with reverse osmosis unit main frame is positioned in the reverse osmosis unit main frame chamber sidewall at the reverse osmosis membrane back side, elevated tank inlet pipeline is had to connect elevated tank at the opposite side of reverse osmosis unit main frame, water intaking valve and check-valves are installed in elevated tank inlet pipeline, one end that elevated tank inlet pipeline is connected with reverse osmosis unit main frame is connected on the water producing pipe road of reverse osmosis unit main frame.
The back purge system of above-mentioned reverse osmosis membrane, is provided with liquid level gauge in described elevated tank.
The back purge system of above-mentioned reverse osmosis membrane, the junction on described elevated tank inlet pipeline and water producing pipe road is being produced on the water producing pipe road between water valve and reverse osmosis unit main frame.
The beneficial effects of the utility model are:
The utility model installs elevated tank above reverse osmosis unit main frame, elevated tank is connected with the chamber at the reverse osmosis membrane back side in reverse osmosis unit main frame by backwash inlet pipeline, in backwash inlet pipeline and elevated tank inlet pipeline, respectively by-pass valve control is installed, backwash can be implemented to reverse osmosis membrane by said apparatus.The utility model is in the process of rinsing reverse osmosis membrane, just rinsing and hocketing with backwash, developing result can be significantly improved, reduce the pollution of dirt to reverse osmosis membrane, the cleaning frequency of prolongation reverse osmosis membrane, improve the service life of reverse osmosis membrane, reduce production cost, increase economic efficiency.The utility model have structure simple, control convenient, without the need to increasing power-equipment, advantage that operating cost is low, have good popularizing value.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure mark as follows: reverse osmosis unit main frame 1, just rinse inlet pipeline 2, just rinse water intaking valve 3, concentrated water discharge pipeline 4, concentrated water discharge valve 5, water producing pipe road 6, product water valve 7, elevated tank 8, backwash inlet pipeline 9, backwash water intaking valve 10, elevated tank inlet pipeline 11, water intaking valve 12, check-valves 13, liquid level gauge 14.
Detailed description of the invention
Show in figure, reverse osmosis unit main frame 1 is connected with and just rinses inlet pipeline 2, concentrated water discharge pipeline 4, water producing pipe road 6, just rinse in inlet pipeline 2, concentrated water discharge pipeline 4 and water producing pipe road 6 be separately installed with just rinse water intaking valve 3, concentrated water discharge valve 5 and produce water valve 7.Just rinse inlet pipeline 2, concentrated water discharge pipeline 4 and water producing pipe road 6 and can complete just flushing to the reverse osmosis membrane in reverse osmosis unit main frame 1.
Show in figure, the utility model is installed on main reverse osmosis unit main frame 1.The utility model is made up of elevated tank 8, backwash inlet pipeline 9, elevated tank inlet pipeline 11, at backwash inlet pipeline 9, backwash water intaking valve 10 is installed, elevated tank inlet pipeline 11 is installed into water valve 12, check-valves 13, elevated tank 8 is provided with liquid level gauge 14.
Show in figure, elevated tank 8 is placed on the top of reverse osmosis unit main frame 1, the backwash inlet pipeline 9 of elevated tank 8 is connected to the side of reverse osmosis unit main frame 1 by backwash water intaking valve 10, the water inlet that backwash inlet pipeline 9 is connected with reverse osmosis unit main frame 1 is positioned in reverse osmosis unit main frame 1 chamber sidewall at the reverse osmosis membrane back side.Elevated tank inlet pipeline 11 is had to connect elevated tank 8 at the opposite side of reverse osmosis unit main frame 1.
Show in figure, one end that elevated tank inlet pipeline 11 is connected with reverse osmosis unit main frame 1 is connected on the water producing pipe road 6 of reverse osmosis unit main frame 1, and the junction on elevated tank inlet pipeline 11 and water producing pipe road 6 is being produced on the water producing pipe road 6 between water valve 7 and reverse osmosis unit main frame 1.
Show in figure, liquid level gauge 14 is installed in elevated tank 8.
The course of work of the present utility model is as follows:
Counter-infiltration system starts; first carry out start to rinse; the water stage processed is transferred to after flushing terminates; when water processed terminates; open the water intaking valve 12 of elevated tank inlet pipeline 11 before not yet shutting down, regulate reverse osmosis produced water valve 7 that water is introduced elevated tank 8, specify liquid level to close reverse osmosis produced water valve 7 when water level reaches; then orderly closedown, carries out shutting down just rinsing.Just rinsing and terminating the just flushing water intaking valve 3 that inlet pipeline 2 is just being rinsed in rear closedown, opening the backwash water intaking valve 10 of backwash inlet pipeline 9 and the concentrated water discharge valve 5 of concentrated water discharge pipeline 4, carry out reverse osmosis membrane backwash.Backwash terminates, and closes backwash water intaking valve 10, transfers to and just rinsing, will peel off or go out system through the pollutant that backwash has become loose, transfers normal water processed to or shuts down stand-by.
Claims (3)
1. the back purge system of a reverse osmosis membrane, it is characterized in that: it comprises elevated tank (8), backwash inlet pipeline (9), elevated tank inlet pipeline (11), elevated tank (8) is placed on the top of reverse osmosis unit main frame (1), one end of backwash inlet pipeline (9) is connected with elevated tank (8), the other end of backwash inlet pipeline (9) is connected to the side of reverse osmosis unit main frame (1), backwash water intaking valve (10) is installed in backwash inlet pipeline (9), the water inlet that backwash inlet pipeline (9) is connected with reverse osmosis unit main frame (1) is positioned in reverse osmosis unit main frame (1) chamber sidewall at the reverse osmosis membrane back side, elevated tank inlet pipeline (11) is had to connect elevated tank (8) at the opposite side of reverse osmosis unit main frame (1), water intaking valve (12) and check-valves (13) are installed in elevated tank inlet pipeline (11), one end that elevated tank inlet pipeline (11) is connected with reverse osmosis unit main frame (1) is connected on the water producing pipe road (6) of reverse osmosis unit main frame (1).
2. the back purge system of reverse osmosis membrane according to claim 1, is characterized in that: be provided with liquid level gauge (14) in described elevated tank (8).
3. the back purge system of reverse osmosis membrane according to claim 2, is characterized in that: the junction of described elevated tank inlet pipeline (11) and water producing pipe road (6) is positioned on the water producing pipe road (6) of producing between water valve (7) and reverse osmosis unit main frame (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520899259.4U CN205109417U (en) | 2015-11-12 | 2015-11-12 | Reverse osmosis membrane's anti - washing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520899259.4U CN205109417U (en) | 2015-11-12 | 2015-11-12 | Reverse osmosis membrane's anti - washing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205109417U true CN205109417U (en) | 2016-03-30 |
Family
ID=55565066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520899259.4U Expired - Fee Related CN205109417U (en) | 2015-11-12 | 2015-11-12 | Reverse osmosis membrane's anti - washing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205109417U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110171871A (en) * | 2019-07-07 | 2019-08-27 | 淄博格瑞水处理工程有限公司 | High-recovery reverse osmosis equipment with high desalinization ratio |
-
2015
- 2015-11-12 CN CN201520899259.4U patent/CN205109417U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110171871A (en) * | 2019-07-07 | 2019-08-27 | 淄博格瑞水处理工程有限公司 | High-recovery reverse osmosis equipment with high desalinization ratio |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Reverse osmosis membrane's anti - washing unit Effective date of registration: 20160823 Granted publication date: 20160330 Pledgee: Bank of Cangzhou Limited by Share Ltd Tangshan branch Pledgor: Hebei GOLDENCOAST Environmental Technology Co. Ltd.|Tangshan Jianye coast Environmental Protection Engineering Co. Ltd. Registration number: 2016990000728 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20170912 Granted publication date: 20160330 Pledgee: Bank of Cangzhou Limited by Share Ltd Tangshan branch Pledgor: HEBEI GOLD COAST ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD.|TANGSHAN HAIAN JIANYE ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. Registration number: 2016990000728 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160330 Termination date: 20191112 |