CN202729930U - Minitype reverse osmosis system - Google Patents
Minitype reverse osmosis system Download PDFInfo
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- CN202729930U CN202729930U CN 201220437213 CN201220437213U CN202729930U CN 202729930 U CN202729930 U CN 202729930U CN 201220437213 CN201220437213 CN 201220437213 CN 201220437213 U CN201220437213 U CN 201220437213U CN 202729930 U CN202729930 U CN 202729930U
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- pipeline
- reverse osmosis
- raw water
- osmosis unit
- cartridge filter
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Abstract
The utility model belongs to the technical field of concentrated water recycling treatment, and particularly relates to a minitype reverse osmosis system which comprises a raw water tank, a raw water pump, a quartz sand filter, an active carbon filter, a resin softener and a cartridge filter, wherein the raw water tank is provided with a raw water automatic level gauge. The minitype reverse osmosis system also comprises a salt tank, a pipeline A, a reverse osmosis unit, a pure water tank, a pipeline B, a pipeline C and a pipeline D, wherein the pipeline D is sequentially provided with a regulating valve B, a flowmeter B and a return water check valve; one end of the pipeline D is connected with the pipeline B between the reverse osmosis unit and a regulating valve A; and the other end is connected with the pipeline A between the cartridge filter and a high-pressure pump. The pipeline D provided with the regulating valve B, flowmeter B and return water check valve is added, so that the concentrated water recycling rate is up to 65% which is enhanced by 15% as compared with the common minitype reverse osmosis system, the production efficiency is enhanced, and the profit of the enterprise is increased.
Description
Technical field
The utility model belongs to dense water recycling technical field, relates in particular to a kind of reverse osmosis system.
Background technology
Reverse osmosis technology is a kind of membrane separation technique that is mainly used in pure water preparation, time of the U.S., Japanology exploitation early, start from 1966 in China, until just be used widely in recent years, the principle of work of reverse osmosis technology is: utilize the selectivity of reverse osmosis membrane to see through function, when the intake pressure in the system during greater than the osmotic pressure of water, water molecules constantly pass reverse osmosis membrane then the multiparity water flow passage flow into pipe core, thereby obtain pure water.The small reverse osmosis system that is used at present dense water recycling mainly comprises raw water box, raw water pump, strainer, softening agent, high-pressure pump, reverse osmosis unit, pure water tank, its working process is: the dense water in the raw water box is at first by the effect of raw water pump flow through strainer and softening agent, and then enter reverse osmosis unit by high-pressure pump, through behind the reverse osmosis membrane in the reverse osmosis unit standard compliant pure water being recycled, remaining dense water is then discarded, because the infiltration standard of each reverse osmosis membrane is 15%-18%, the dense water rate of recovery of reverse osmosis system is the highest can only to be 50%, the rate of recovery is lower like this, thereby make the profit of enterprise also just lower, have a strong impact on the fast development of enterprise.
Summary of the invention
In order to solve the problems of the technologies described above, the invention provides the high small reverse osmosis system of a kind of rate of recovery, comprise the raw water box that connects successively, raw water pump, quartz filter, activated charcoal filter, the resin softening agent, cartridge filter, be provided with former water automatic tank gauge on the described raw water box, also comprise the salt case, pipeline A, reverse osmosis unit, pure water tank, pipeline B, pipeline C, described salt case be connected the resin softening agent and connect, described cartridge filter be connected reverse osmosis unit and connect by described pipeline A, be disposed with high-pressure pump and water inlet vacuum breaker on the described pipeline A, described reverse osmosis unit be connected pure water tank and connect by pipeline B, be disposed with variable valve A on the described pipeline C, under meter A and and be connected reverse osmosis unit connection, it is characterized in that: also comprise being disposed with variable valve B, under meter B, the pipeline D of backwater vacuum breaker, the end of described pipeline D and described reverse osmosis unit, pipeline C between the variable valve A connects, the other end and described cartridge filter, pipeline A between the high-pressure pump connects.
Be provided with the Scale inhibitors adding set between described resin softening agent and the described cartridge filter.
The beneficial effects of the utility model are: the pipeline D that is provided with variable valve B, under meter B, backwater vacuum breaker by increase, make the dense water rate of recovery reach 65%, improve 15% than common small reverse osmosis system, improve production efficiency, increased enterprise profit, in addition also accelerated the flow velocity of dense water in reverse osmosis membrane, thereby the poor polarization phenomena of purulence on reverse osmosis membrane surface have been reduced, reduce fouling tendency, prolonged the work-ing life of reverse osmosis membrane, reduced the production cost of enterprise.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Be described further below in conjunction with 1 pair of the utility model of accompanying drawing:
Among Fig. 1: 1-raw water box, the former water automatic tank gauge of 2-, 3-raw water pump, 4-quartz filter, the 5-activated charcoal filter, 6-resin softening agent, 7-salt case, 8-adds the Scale inhibitors device, the 9-cartridge filter, 10-pipeline A, 11-high-pressure pump, the 12-vacuum breaker of intaking, the 13-reverse osmosis unit, 14-pipeline D, 15-backwater vacuum breaker, 16-under meter B, 17-variable valve B, 18-pipeline C, 19-pipeline B, 20-variable valve A, 21-under meter A, 22-pure water tank.
The present embodiment is provided with the raw water box 1 that connects successively, raw water pump 3, quartz filter 4, activated charcoal filter 5, resin softening agent 6, cartridge filter 9, also be provided with former water automatic tank gauge 2, salt case 7, add Scale inhibitors device 8, pipeline A10, reverse osmosis unit 13, pure water tank 22, pipeline B19, pipeline C18, pipeline D14, former water automatic tank gauge 2 is arranged on the raw water box 1, salt case 7 is connected connection with the resin softening agent, adding Scale inhibitors device 8 is arranged between resin softening agent 6 and the cartridge filter 9, cartridge filter 9 is connected with reverse osmosis unit by pipeline A10 connection, be disposed with high-pressure pump 11 and water inlet vacuum breaker 12 on the pipeline A10, reverse osmosis unit 13 is connected with pure water tank by pipeline B19 connection, pipeline C18 one end is connected connection with reverse osmosis unit, be disposed with variable valve A20 on it, under meter A21, pipeline D14 one end and reverse osmosis unit 13, pipeline C18 between the variable valve A20 connects, the other end and cartridge filter 9,11 pipeline A10 of high-pressure pump connects, and is disposed with variable valve B17 on the pipeline D14, under meter B16, backwater vacuum breaker 15.
The implementation process of the present embodiment:
Dense water in the raw water box 1 under the effect of raw water pump 3, flow through quartz filter 4, activated charcoal filter 5, resin softening agent 6, cartridge filter 9, and then by high-pressure pump 11, the water inlet vacuum breaker 12 enter reverse osmosis unit 13, through carrying pure water tank 22 to recycle standard compliant pure water behind the reverse osmosis membrane in the reverse osmosis unit 13, remaining dense water enters reverse osmosis unit 13 by pipeline D14, pipeline A10 again, carry pure water tank 22 to recycle the standard compliant pure water that obtains for the second time, remaining dense water then carries out waste treatment.
Utilize technical scheme described in the utility model, or those skilled in the art designing similar technical scheme under the inspiration of technical solutions of the utility model, and reach above-mentioned technique effect, all is to fall into protection domain of the present utility model.
Claims (2)
1. small reverse osmosis system, comprise the raw water box (1) that connects successively, raw water pump (3), quartz filter (4), activated charcoal filter (5), resin softening agent (6), cartridge filter (9), be provided with former water automatic tank gauge (2) on the described raw water box (1), also comprise salt case (7), pipeline A (10), reverse osmosis unit (13), pure water tank (22), pipeline B (19), pipeline C (18), described salt case (7) be connected resin softening agent (6) and connect, described cartridge filter (9) be connected reverse osmosis unit (13) and connect by described pipeline A (10), be disposed with high-pressure pump (11) and water inlet vacuum breaker (12) on the described pipeline A (10), described reverse osmosis unit (13) be connected pure water tank (22) and connect by pipeline B (19), be disposed with variable valve A (20) on the described pipeline C (18), under meter A (21) and and be connected reverse osmosis unit (13) connection, it is characterized in that: also comprise being disposed with variable valve B (17), under meter B (16), the pipeline D (14) of backwater vacuum breaker (15), the end of described pipeline D (14) and described reverse osmosis unit (13), pipeline B (19) between the variable valve A (20) connects, the other end and described cartridge filter (9), pipeline A (10) between the high-pressure pump (11) connects.
2. a kind of small reverse osmosis system according to claim 1 is characterized in that: be provided with between described resin softening agent (6) and the described cartridge filter (9) and add Scale inhibitors device (8).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220437213 CN202729930U (en) | 2012-08-30 | 2012-08-30 | Minitype reverse osmosis system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220437213 CN202729930U (en) | 2012-08-30 | 2012-08-30 | Minitype reverse osmosis system |
Publications (1)
Publication Number | Publication Date |
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CN202729930U true CN202729930U (en) | 2013-02-13 |
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Family Applications (1)
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CN 201220437213 Expired - Fee Related CN202729930U (en) | 2012-08-30 | 2012-08-30 | Minitype reverse osmosis system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103951096A (en) * | 2014-04-24 | 2014-07-30 | 成都樵枫科技发展有限公司 | Purified water filtration system |
CN104891703A (en) * | 2014-09-26 | 2015-09-09 | 江苏弘盛新材料股份有限公司 | Deoxygenated and desalted water preparation system |
CN105110505A (en) * | 2015-08-26 | 2015-12-02 | 湖州升腾环境工程有限公司 | First-stage reverse osmosis device for pretreating and softening |
CN112794523A (en) * | 2020-12-22 | 2021-05-14 | 河南省大潮炭能科技有限公司 | Production equipment and production method of purified water |
-
2012
- 2012-08-30 CN CN 201220437213 patent/CN202729930U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103951096A (en) * | 2014-04-24 | 2014-07-30 | 成都樵枫科技发展有限公司 | Purified water filtration system |
CN104891703A (en) * | 2014-09-26 | 2015-09-09 | 江苏弘盛新材料股份有限公司 | Deoxygenated and desalted water preparation system |
CN105110505A (en) * | 2015-08-26 | 2015-12-02 | 湖州升腾环境工程有限公司 | First-stage reverse osmosis device for pretreating and softening |
CN112794523A (en) * | 2020-12-22 | 2021-05-14 | 河南省大潮炭能科技有限公司 | Production equipment and production method of purified water |
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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: 20130213 Termination date: 20150830 |
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EXPY | Termination of patent right or utility model |