CN201605202U - Manpower accumulation type electric desalting device - Google Patents
Manpower accumulation type electric desalting device Download PDFInfo
- Publication number
- CN201605202U CN201605202U CN2009202655820U CN200920265582U CN201605202U CN 201605202 U CN201605202 U CN 201605202U CN 2009202655820 U CN2009202655820 U CN 2009202655820U CN 200920265582 U CN200920265582 U CN 200920265582U CN 201605202 U CN201605202 U CN 201605202U
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- China
- Prior art keywords
- reverse osmosis
- water
- desalination
- electronic
- pressure pump
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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
The utility model discloses a manpower accumulation type electric desalting device, and aims to provide a manpower accumulation type electric desalting device which has relaxed operation, steady water preparation and excellent quality of produced water, and comprises an electric desalination system, wherein the electric desalination system comprises an electric water supply pump (1), a filter device (2), a high pressure pump (3) and a reverse osmosis desalination device (4) which are orderly connected, and a cleaning box (5) is connected between the high pressure pump (3) and the reverse osmosis desalination device (4) in parallel. The manpower accumulation type electric desalting device further comprises a manual desalination system, wherein the manual desalination system comprises a manual generator (6), an accumulator (7) and a mini-type high pressure pump (8), a water inlet end of the mini-type high pressure pump (8) is connected with a water outlet end of the cleaning box (5), and the water outlet end of the mini-type high pressure pump (8) is connected with the water inlet end of the reverse osmosis desalination device (4). The manpower accumulation type electric desalting device can be widely applied for the desalination fields of brackish water and sea water.
Description
Technical field
The utility model relates to the electronic desalting plant of a kind of manpower energy storage type.
Background technology
The reverse osmosis desalination technical matters is one of desalination techniques of at present commonly used, best results, and it is used widely in seawater, desalination field; The patent No. that the applicant provides is: 01215499.7 electronic and dual-use manual desalination by reverse osmosis device can be at navigation or other mal-condition; because chance failure or outage etc. cause under the situation of the light machine shutdown of system; for emergent and lifesaving need; system is light fast to utilize hand gear quickly and easily, and the fresh water that earns a bare living in time is provided.Yet, in actual applications, above-mentioned desalting equipment is by the raise working pressure of reverse osmosis membrane assembly of manpower pitcher pump because the pitcher pump discontinuity, the rotating speed of pump neglect fast neglect slow, easily cause effluent quality poor, and the labour intensity of requiring great effort in operation is big, and when emergency, operator are more tired out, manually system water will be more painstaking this moment, and system water effect is more undesirable.
In sum, existing electronic and dual-use manual desalination by reverse osmosis device in use, exist manpower labour intensity big, produce the unsettled technological deficiency of water water quality.
The utility model content
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, provide a kind of and operate easily when manual state, and system water is stable more and the good electronic desalting plant of manpower energy storage type of product water water quality.
The technical scheme that the utility model adopted is: the utility model comprises electronic desalination system, described electronic desalination system comprises the electronic working shaft that connects successively, filtration unit, high-pressure pump, the desalination by reverse osmosis device, be parallel with cleaning case between described high-pressure pump and the described desalination by reverse osmosis device, the electronic desalting plant of described manpower energy storage type also comprises manual desalination system, described manual desalination system comprises the man-power generator that connects successively, store battery, micro-high-pressure pump, the water intake end of described micro-high-pressure pump is connected with the water side of described cleaning case, and the water side of described micro-high-pressure pump is connected with the water intake end of described desalination by reverse osmosis device.
Described desalination by reverse osmosis device comprises first-stage reverse osmosis membrane module, two-pass reverse osmosis membrane module, the manual two-pass reverse osmosis assembly that connects successively, and the water side of described micro-high-pressure pump is connected with the water intake end of described two-pass reverse osmosis membrane module.
Described filtration unit comprises more medium filter, activated carbon adsorber, the accurate filter that connects successively.
Described first-stage reverse osmosis membrane module also is connected with one-level concentrated water spout, one-level fresh water mouth, and described one-level concentrated water spout is provided with tensimeter and relief valve.
Described two-pass reverse osmosis membrane module also is connected with secondary concentrated water spout, pressure vessel, and described secondary concentrated water spout is provided with tensimeter and relief valve, is provided with under meter between described two-pass reverse osmosis membrane module and the described pressure vessel.
Be provided with tensimeter and relief valve between described cleaning case and the described manual two-pass reverse osmosis membrane module.
Described manual two-pass reverse osmosis membrane module also is connected with fresh-water tank, is provided with under meter, ball valve between described manual two-pass reverse osmosis membrane module and the fresh-water tank.
The beneficial effects of the utility model are: because the utility model not only comprises electronic desalination system, under the situation that possesses the electricity consumption condition, can cross described electronic desalination system to brackish water, seawater etc. are desalinated processing, in addition, the utility model also comprises manual desalination system, described manual desalination system comprises the man-power generator that connects successively, store battery, micro-high-pressure pump, the water intake end of described micro-high-pressure pump is connected with the water side of described cleaning case, the water side of described micro-high-pressure pump is connected with the water intake end of described desalination by reverse osmosis device, therefore, under the environment that does not possess the electricity consumption condition, can meet an urgent need by described manual desalination system and prepare fresh water, and when described manual desalination system is worked, utilize the manpower acting, kinetic energy is imported described man-power generator, by described man-power generator kinetic energy is converted into electric energy and imports described store battery into, balancedly provide work required electric energy by described store battery to described micro-high-pressure pump, make described micro-high-pressure pump smooth working, product water is even, effectively ensure good product water water quality, and, described man-power generator can adopt shaking or various ways such as foot-operated to carry out the kinetic energy input, and is less demanding to manpower labour intensity, can soon can be slow, when muscle power is better, can accelerate generating speed, the electric energy of surplus is deposited in the store battery, physical when relatively poor, then slow down generating speed, utilize the electric energy of the storage in the store battery evenly to power to the micro pressure pump, therefore, when utilizing manual desalination system to prepare fresh water, manpower labour intensity is low, and operation easily.
Description of drawings
Fig. 1 is a structured flowchart of the present utility model;
Fig. 2 is a structure connection diagram of the present utility model.
Embodiment
As shown in Figure 1 and Figure 2, the utility model comprises electronic desalination system, described electronic desalination system comprises electronic working shaft 1, filtration unit 2, high-pressure pump 3, the desalination by reverse osmosis device 4 that connects successively, and described filtration unit 2 comprises more medium filter 21, activated carbon adsorber 22, the accurate filter 23 that connects successively; Described desalination by reverse osmosis device 4 comprises first-stage reverse osmosis membrane module 41, two-pass reverse osmosis membrane module 42, the manual two-pass reverse osmosis assembly 43 that connects successively, described first-stage reverse osmosis membrane module 41 also is connected with one-level concentrated water spout 411, one-level fresh water mouth 412, and described one-level concentrated water spout 411 is provided with tensimeter 01 and relief valve 02; Described two-pass reverse osmosis membrane module 42 also is connected with secondary concentrated water spout 421, pressure vessel 422, and described secondary concentrated water spout 421 is provided with tensimeter 01 and relief valve 02, is provided with under meter 03 between described two-pass reverse osmosis membrane module 42 and the described pressure vessel 422; Described manual two-pass reverse osmosis membrane module 43 also is connected with fresh-water tank 431, is provided with under meter 03, ball valve 04 between described manual two-pass reverse osmosis membrane module 43 and the fresh-water tank 431; Be parallel with cleaning case 5 between the manual two-pass reverse osmosis membrane module 43 of described high-pressure pump 3 and described desalination by reverse osmosis device 4, be provided with tensimeter 01 and relief valve 02 between described cleaning case 5 and the described manual two-pass reverse osmosis membrane module 42; The utility model also comprises manual desalination system, described manual desalination system comprises man-power generator 6, store battery 7, the micro-high-pressure pump 8 that connects successively, the water intake end of described micro-high-pressure pump 8 is connected with the water side of described cleaning case 5, and the water side of described micro-high-pressure pump 8 is connected with the water intake end of described desalination by reverse osmosis device 4.
Under the situation that possesses the electricity consumption condition, when utilizing electronic desalination system described in the utility model that brackish water or seawater are desalinated, its workflow is: described electronic working shaft 1 is connected power supply and is supplied water, former water is through the more medium filter 21 in the described filtration unit 2, activated carbon adsorber 22, accurate filter 23 filters successively, the first-stage reverse osmosis membrane module 41 that enters described desalination by reverse osmosis device 4 through described high-pressure pump 3 pressurizations is desalinated processing then, the dense water that is produced is discharged from described one-level concentrated water spout 411, product water after former water is desalinated through one-level can reach national domestic water water quality requirement, can feed described one-level fresh water mouth 412 directly uses as domestic water, also can feed described two-pass reverse osmosis membrane module 42 and carry out secondary desalination processing, the dense water that produces is discharged from described two concentrated water spouts 411, can feed described pressure vessel 422 through the product water after the secondary desalination and directly drink.
Do not possessing the electricity consumption condition in emergency circumstances, when utilizing manual desalination system described in the utility model that brackish water or seawater are desalinated, its workflow is: utilize manpower directly or indirectly to described man-power generator 6 actings, kinetic energy is imported described man-power generator 6, the kinetic energy input time can be adopted shaking or various ways such as foot-operated, kinetic energy is converted into electric energy and imports described store battery 7 into by described man-power generator 6, balancedly provide work required electric energy by described store battery 7 again to described micro-high-pressure pump 8, make described micro-high-pressure pump 8 carry out water supply work, the water intake end of described micro-high-pressure pump 8 is connected with described cleaning case 5 by ball valve 04, described cleaning case 5 is as the bin of former water at this moment, former water feeds described two-pass reverse osmosis membrane module 42 by described micro-high-pressure pump 8 and desalinates processing, the dense water that produces is discharged from described secondary concentrated water spout 421, desalination product water enters described manual two-pass reverse osmosis membrane module 43 and carries out the secondary desalination, the dense water that is produced is low more than the concentration of seawater, therefore feeding described cleaning case 5 desalinates as former water again, save resource, product water after described manual two-pass reverse osmosis membrane module 43 desalinations feeds described fresh-water tank 431 and uses, and manual desalination system produces water in carrying out the desalination process even, water quality is good.
During, desalination ability drop relatively poor when the light effect of desalination system system, can clean desalination system by in described cleaning case 5, placing scavenging solution, its cleaning process is: scavenging solution enters described high-pressure pump 3 from described cleaning case 5, provide pressure by described high-pressure pump 3, scavenging solution enters described reverse osmosis unit, and to the first-stage reverse osmosis membrane module 41 of described reverse osmosis unit, two-pass reverse osmosis membrane module 42, manually two-pass reverse osmosis assembly 43 inside are washed away, and reach the cleaning purpose.
The utility model can be widely used in brackish water, sea water desaltination field.
Claims (7)
1. electronic desalting plant of manpower energy storage type, comprise electronic desalination system, described electronic desalination system comprises the electronic working shaft (1) that connects successively, filtration unit (2), high-pressure pump (3), desalination by reverse osmosis device (4), be parallel with cleaning case (5) between described high-pressure pump (3) and the described desalination by reverse osmosis device (4), it is characterized in that: the electronic desalting plant of described manpower energy storage type also comprises manual desalination system, described manual desalination system comprises the man-power generator (6) that connects successively, store battery (7), micro-high-pressure pump (8), the water intake end of described micro-high-pressure pump (8) is connected with the water side of described cleaning case (5), and the water side of described micro-high-pressure pump (8) is connected with the water intake end of described desalination by reverse osmosis device (4).
2. the electronic desalting plant of manpower energy storage type according to claim 1, it is characterized in that: described desalination by reverse osmosis device comprises first-stage reverse osmosis membrane module (41), two-pass reverse osmosis membrane module (42), the manual two-pass reverse osmosis assembly (43) that connects successively, and the water side of described micro-high-pressure pump (8) is connected with the water intake end of described two-pass reverse osmosis membrane module (42).
3. the electronic desalting plant of manpower energy storage type according to claim 1 and 2 is characterized in that: described filtration unit (2) comprises more medium filter (21), activated carbon adsorber (22), the accurate filter (23) that connects successively.
4. the electronic desalting plant of manpower energy storage type according to claim 3, it is characterized in that: described first-stage reverse osmosis membrane module (41) also is connected with the dense water of one-level (411), one-level fresh water mouth (412), and described one-level concentrated water spout (411) is provided with tensimeter (01) and relief valve (02).
5. the electronic desalting plant of manpower energy storage type according to claim 3, it is characterized in that: described two-pass reverse osmosis membrane module (42) also is connected with secondary concentrated water spout (421), pressure vessel (422), described secondary concentrated water spout (421) is provided with tensimeter (01) and relief valve (02), is provided with under meter (03) between described two-pass reverse osmosis membrane module (42) and the described pressure vessel (422).
6. the electronic desalting plant of manpower energy storage type according to claim 3 is characterized in that: be provided with tensimeter (01) and relief valve (02) between described cleaning case (5) and the described manual two-pass reverse osmosis membrane module (42).
7. the electronic desalting plant of manpower energy storage type according to claim 6, it is characterized in that: described manual two-pass reverse osmosis membrane module (43) also is connected with fresh-water tank (431), is provided with under meter (03), ball valve (04) between described manual two-pass reverse osmosis membrane module (43) and the fresh-water tank (431).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202655820U CN201605202U (en) | 2009-12-25 | 2009-12-25 | Manpower accumulation type electric desalting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202655820U CN201605202U (en) | 2009-12-25 | 2009-12-25 | Manpower accumulation type electric desalting device |
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| Publication Number | Publication Date |
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| CN201605202U true CN201605202U (en) | 2010-10-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2009202655820U Expired - Fee Related CN201605202U (en) | 2009-12-25 | 2009-12-25 | Manpower accumulation type electric desalting device |
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| CN (1) | CN201605202U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103382039A (en) * | 2012-05-06 | 2013-11-06 | 厦门锐思达机电科技有限公司 | Emergency seawater desalination device |
| CN103991978A (en) * | 2014-06-05 | 2014-08-20 | 张筱秋 | Copper alloy external thread reef fresh water high pressure membrane permeation device |
-
2009
- 2009-12-25 CN CN2009202655820U patent/CN201605202U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103382039A (en) * | 2012-05-06 | 2013-11-06 | 厦门锐思达机电科技有限公司 | Emergency seawater desalination device |
| CN103991978A (en) * | 2014-06-05 | 2014-08-20 | 张筱秋 | Copper alloy external thread reef fresh water high pressure membrane permeation device |
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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: 20101013 Termination date: 20181225 |
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| CF01 | Termination of patent right due to non-payment of annual fee |