CN201713394U - Reverse osmosis seawater desalination equipment - Google Patents

Reverse osmosis seawater desalination equipment Download PDF

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Publication number
CN201713394U
CN201713394U CN2010202197045U CN201020219704U CN201713394U CN 201713394 U CN201713394 U CN 201713394U CN 2010202197045 U CN2010202197045 U CN 2010202197045U CN 201020219704 U CN201020219704 U CN 201020219704U CN 201713394 U CN201713394 U CN 201713394U
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CN
China
Prior art keywords
reverse osmosis
desalting equipment
osmosis seawater
seawater desalting
pressure pump
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
Application number
CN2010202197045U
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Chinese (zh)
Inventor
李雄春
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Individual
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Individual
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Publication date
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Priority to CN2010202197045U priority Critical patent/CN201713394U/en
Application granted granted Critical
Publication of CN201713394U publication Critical patent/CN201713394U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model relates to the field of seawater desalination technology, in particular to reverse osmosis seawater desalination equipment comprising a water supply pump, a filter, a high-pressure pump and a reverse osmosis membrane module, wherein the water supply pump is connected with the filter through a first channel; the filter is connected with the high-pressure pump through a second channel; the high-pressure pump is connected with the reverse osmosis membrane module through a third channel; and a fresh water outlet pipe of the reverse osmosis membrane module is connected with a water pipe. The utility model has the benefits that the fresh water prepared by the reverse osmosis seawater desalination equipment can be directly drunk by people.

Description

Reverse osmosis seawater desalting equipment
Technical field:
The utility model relates to field of sea water desalting technology, refers in particular to a kind of reverse osmosis seawater desalting equipment.
Background technology:
21st century is the century of water, and China is one of country of water scarcity in the world, and along with industrial boom, water consumption is increasing, and a lot of areas are because insufficient water sources has constituted important restraining factors to industrial development.Freshwater resources are one of necessary resources of human survival, and at present, the water resources in a lot of rivers all is subjected to pollution in various degree, badly influences people's existence.What water resources was the widest in the world is the sea, still, contains a large amount of salinities in the seawater, therefore seawater can not directly be drunk, if the salinity in the seawater can be removed, makes seawater be cleaned into fresh water, then can increase the source of fresh water greatly, keep people's orthobiosis.Because the seawater resources of China are abundant, want water to the sea, produce fresh water with seawater and satisfy industrial production and domestic water, be the development trend that China's water resources makes full use of.The fresh water that existing sea water desalting equipment is produced out can't directly be drunk, and promotes the use of thereby be difficult to big area, and then can't satisfy the demand in market.
In sum, there is the improved place of some needs in sea water desalting equipment at present, and the applicant also is in this purpose just and creates design the utility model.
The utility model content:
Technical problem to be solved in the utility model is exactly the deficiency that overcomes above-mentioned existence, and a kind of reverse osmosis seawater desalting equipment is provided.
For solving the problems of the technologies described above, the utility model has adopted following technical scheme: this reverse osmosis seawater desalting equipment comprises: working shaft, strainer, high-pressure pump, reverse osmosis membrane assembly, wherein, working shaft is by first channel and strainer, strainer is connected with high-pressure pump by second passage, high-pressure pump is connected with reverse osmosis membrane assembly by third channel, and the fresh water rising pipe of reverse osmosis membrane assembly is connected with water pipe.
Be connected with sterilizer on the described fresh water rising pipe.
The dense water rising pipe of described reverse osmosis membrane assembly, fresh water rising pipe are connected with a cleaning water tank respectively, and the cleaning water tank is connected with high-pressure pump by four-way.
Described strainer comprises: be connected in sand-bed filter, secondary filter, security personnel's filter on the first channel successively.
Described sand-bed filter is connected with the cleaning water tank by the five-way road.
Be connected with a fresh water storage tank on the described water pipe.
This reverse osmosis seawater desalting equipment also comprises a controlling box.
Described sterilizer is a ultraviolet sterilizer.
Described high-pressure pump is a high pressure plunger pump.
The beneficial effects of the utility model are: can directly drink for people by the fresh water that the utility model is produced out.
Description of drawings:
Fig. 1 is a synoptic diagram of the present utility model.
Embodiment:
See shown in Figure 1, the utility model comprises: working shaft 1, strainer 2, high-pressure pump 3, six reverse osmosis membrane assemblies 4, a sterilizer 5 and are used to control the controlling box of this reverse osmosis seawater desalting equipment, wherein, high-pressure pump 3 is a high pressure plunger pump, and sterilizer 5 is a ultraviolet sterilizer.
Particularly:
Above-mentioned working shaft 1 is by first channel 6 and strainer 2, strainer 2 is connected with high-pressure pump 3 by second passage 7, high-pressure pump 3 is connected with reverse osmosis membrane assembly 4 by third channel 8, and the fresh water rising pipe 9 of reverse osmosis membrane assembly 4 is connected with sterilizer 5, and sterilizer 5 is connected with water pipe 14.Be connected with a fresh water storage tank 15 that is used to store fresh water on this water pipe 14.The dense water rising pipe 10 of this reverse osmosis membrane assembly 4, fresh water rising pipe 9 respectively with clean water tank 11 and be connected, and clean water tank 11 and pass through four-way 12 and be connected with high-pressure pump 3, be connected with first ball valve 16 on the four-way 12.Be connected with first tensimeter 17, variable valve 18, first flow meter 19, second ball valve 20 on the dense water rising pipe 10 between this reverse osmosis membrane assembly 4 and the cleaning water tank 11.
Above-mentioned strainer 2 comprises: be connected in sand-bed filter 21 on the first channel 6, two secondary filters 22, two security personnel's filters 23 successively.This sand-bed filter 21 is connected with cleaning water tank 11 by five-way road 13.Be connected with second tensimeter 24, second flange 42 on the first channel 6 between this working shaft 1 and the sand-bed filter 21, sand-bed filter 21 and on the first channel 6 between the secondary filter 22 in left side, be connected with the 3rd tensimeter 25, high-pressure pump 3 and on the first channel 6 between the secondary filter 22 on right side, be connected with the 4th tensimeter 26, the 3rd ball valve 27, pressure switch 28.Be connected with first vacuum breaker 29, first flange 30, the 4th ball valve 31 on the five-way road 13 between sand-bed filter 21 and the cleaning water tank 11.Be connected with first tensimeter 17, variable valve 18, first flow meter 19, the 5th ball valve 32 on the dense water rising pipe 10 that is connected with five-way road 13.Be connected with electric contact table 33, conductivity apparatus 34, second under meter 35, the 6th ball valve 36 on the fresh water rising pipe 9 that five-way road 13 is connected.Be connected with above-mentioned electric contact table 33, above-mentioned conductivity apparatus 34, above-mentioned second under meter 35, the 7th ball valve 37, first magnetic valve 38, second magnetic valve 39 on the fresh water rising pipe 9 that five-way road 13 is connected.Be connected with above-mentioned electric contact table 33, above-mentioned conductivity apparatus 34, above-mentioned second under meter 35, above-mentioned the 7th ball valve 37, above-mentioned first magnetic valve 38, above-mentioned the 6th ball valve 36 on the fresh water rising pipe 9 that five-way road 13 is connected.
The water outlet place of above-mentioned six reverse osmosis membrane assemblies 4 is provided with sampling tap, vacuum breaker respectively, with clean the fresh water rising pipe 9 that water tank 11 is connected on be connected with above-mentioned electric contact table 33, above-mentioned conductivity apparatus 34, above-mentioned second under meter 35, second magnetic valve 39, the 8th ball valve 40.Be connected with thief hole 41 on the fresh water rising pipe 9 between permeable membrane element 4 and the sterilizer 5.
Certainly, the above only is embodiment of the present utility model, be not to limit the utility model practical range, all equivalences of doing according to the described structure of the utility model claim, feature and principle change or modify, and all should be included in the utility model claim.

Claims (9)

1. reverse osmosis seawater desalting equipment, it is characterized in that: it comprises working shaft (1), strainer (2), high-pressure pump (3), reverse osmosis membrane assembly (4), wherein, working shaft (1) is by first channel (6) and strainer (2), strainer (2) is connected with high-pressure pump (3) by second passage (7), high-pressure pump (3) is connected with reverse osmosis membrane assembly (4) by third channel (8), and the fresh water rising pipe (9) of reverse osmosis membrane assembly (4) is connected with water pipe (14).
2. reverse osmosis seawater desalting equipment according to claim 1 is characterized in that: be connected with sterilizer (5) on the described fresh water rising pipe (9).
3. reverse osmosis seawater desalting equipment according to claim 2, it is characterized in that: the dense water rising pipe (10) of described reverse osmosis membrane assembly (4), fresh water rising pipe (9) are connected with a cleaning water tank (11) respectively, and cleaning water tank (11) is connected with high-pressure pump (3) by four-way (12).
4. reverse osmosis seawater desalting equipment according to claim 3 is characterized in that: described strainer (2) comprising: be connected in sand-bed filter (21), secondary filter (22), security personnel's filter (23) on the first channel (6) successively.
5. reverse osmosis seawater desalting equipment according to claim 4 is characterized in that: described sand-bed filter (21) is connected with cleaning water tank (11) by five-way road (13).
6. reverse osmosis seawater desalting equipment according to claim 5 is characterized in that: be connected with a fresh water storage tank (15) on the described water pipe (14).
7. reverse osmosis seawater desalting equipment according to claim 6 is characterized in that: this reverse osmosis seawater desalting equipment also comprises a controlling box.
8. reverse osmosis seawater desalting equipment according to claim 7 is characterized in that: described sterilizer (5) is a ultraviolet sterilizer.
9. reverse osmosis seawater desalting equipment according to claim 8 is characterized in that: described high-pressure pump (3) is a high pressure plunger pump.
CN2010202197045U 2010-06-04 2010-06-04 Reverse osmosis seawater desalination equipment Expired - Fee Related CN201713394U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202197045U CN201713394U (en) 2010-06-04 2010-06-04 Reverse osmosis seawater desalination equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202197045U CN201713394U (en) 2010-06-04 2010-06-04 Reverse osmosis seawater desalination equipment

Publications (1)

Publication Number Publication Date
CN201713394U true CN201713394U (en) 2011-01-19

Family

ID=43459394

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202197045U Expired - Fee Related CN201713394U (en) 2010-06-04 2010-06-04 Reverse osmosis seawater desalination equipment

Country Status (1)

Country Link
CN (1) CN201713394U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105461124A (en) * 2014-08-26 2016-04-06 李雄春 Equipment capable of converting seawater into mineral direct drinking water
CN105565531A (en) * 2016-03-04 2016-05-11 宁波淳源环保科技有限公司 Efficient reverse osmosis seawater desalting plant
CN106428504A (en) * 2016-10-31 2017-02-22 河北科技大学 Small reverse osmosis seawater desalting device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105461124A (en) * 2014-08-26 2016-04-06 李雄春 Equipment capable of converting seawater into mineral direct drinking water
CN105565531A (en) * 2016-03-04 2016-05-11 宁波淳源环保科技有限公司 Efficient reverse osmosis seawater desalting plant
CN106428504A (en) * 2016-10-31 2017-02-22 河北科技大学 Small reverse osmosis seawater desalting device

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110119

Termination date: 20130604