CN203212407U - Reverse osmosis system for backwashing filter by using concentrated water - Google Patents

Reverse osmosis system for backwashing filter by using concentrated water Download PDF

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Publication number
CN203212407U
CN203212407U CN 201320179688 CN201320179688U CN203212407U CN 203212407 U CN203212407 U CN 203212407U CN 201320179688 CN201320179688 CN 201320179688 CN 201320179688 U CN201320179688 U CN 201320179688U CN 203212407 U CN203212407 U CN 203212407U
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CN
China
Prior art keywords
reverse osmosis
stage
filtering device
quartz sand
concentrated water
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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
Application number
CN 201320179688
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Chinese (zh)
Inventor
付志和
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Changzhou Kaiyuan Water Treatment Technology Co Ltd
Original Assignee
Changzhou Kaiyuan Water Treatment Technology Co Ltd
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Priority to CN 201320179688 priority Critical patent/CN203212407U/en
Application granted granted Critical
Publication of CN203212407U publication Critical patent/CN203212407U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a reverse osmosis system for backwashing a filter by using concentrated water. The reverse osmosis system comprises a raw water tank, a first-stage quartz sand filtering device, a first-stage activated carbon filtering device, a first-stage reverse osmosis device, a concentrated water tank, a second-stage quartz sand filtering device and a second-stage activated carbon filtering device which are connected in sequence, wherein an antisludging agent feeding tank is arranged between the first-stage activated carbon filtering device and the first-stage reverse osmosis device; a filter washing pump is arranged between the concentrated water tank and the second-stage quartz sand filtering device. By utilizing the reverse osmosis system, a reverse osmosis concentrated water side is prevented from scaling, the film washing frequency is reduced, the service life of the film is prolonged, and the production efficiency is improved; as the first-stage reverse osmosis concentrated water is temporarily stored up to positively and reversely wash a quartz sand filter and an activated carbon filter, the water resource is sufficiently and effectively utilized.

Description

Utilize the reverse osmosis system of dense water backwashing strainer
Technical field
The utility model relates to the technical field of water treating equipment, especially a kind of reverse osmosis system that utilizes dense water backwashing strainer.
Background technology
At known water-treatment technology field, after former water process quartz sand filtration device and the activated charcoal filter pre-treatment, ion wherein is difficult to be removed, after the pre-treatment water outlet enters the first-stage reverse osmosis system again, former water flows to the other end in a side of film from an end, water molecules sees through the film surface, arrive opposite side from former water side, and ion is just stayed an original side, along with former water is progressively concentrated, water molecules is constantly taken away from former water, and the saltiness of staying in the former water progressively increases, and namely former water progressively is concentrated, and finally becomes dense water, discharge from device, dense water is subjected to concentrate the various ionic concns in back and will be multiplied.Ca in the natural water source 2+, Mg 2+, Ba 2+, Sr 2+, HCO 3 -, SO 4 2-, SiO 3 2-Long-pending generally all less than its equilibrium constant Deng the concentration of the ion that tends to fouling, do not occur so do not have fouling, but after concentrating, therefore the long-pending equilibrium constant that all might substantially exceed of the concentration of various ions can produce serious fouling.In case the film fouling, the flow that produces water will descend, and water quality also can descend, and at this moment just must shut down that timely membrane element is cleaned, and has reduced the efficient of production and the life-span that membrane element uses.
After former water enters the first-stage reverse osmosis system simultaneously, water outlet is divided into two-way, one the tunnel is that pure water supplies with the water spot water or enter next stage to handle, one the tunnel is the dense water after the reverse osmosis membrane processing, and dense water often concentrates several times than the ion content of former water, and the dense water yield is very big, very difficult backflow is handled again, overwhelming majority's pure water equipment system all directly enters trench with it, and water resources is in short supply day by day now, need carry out fully effectively utilizing to water resources.
The utility model content
The technical problems to be solved in the utility model is: in order to solve the problem that proposes in the above-mentioned background technology, the utility model provides a kind of reverse osmosis system that utilizes dense water backwashing strainer, it can prevent that the reverse osmosis concentrated water side from producing fouling, reduce the number of times that film cleans, increase the life-span of film, enhance productivity; By the dense water interim storage of first-stage reverse osmosis is got up, be used for quartz sand filtration device and activated charcoal filter are just being washed and backwash, water resources has been carried out fully effectively utilizing.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of reverse osmosis system that utilizes dense water backwashing strainer, comprise the raw water box, one-level quartz sand filtration device, one-level active carbon filtering device, first-stage reverse osmosis device, dense water tank, secondary quartz sand filtration device and the secondary active carbon filtering device that connect in turn, be provided with the Scale inhibitors dosing tank between one-level active carbon filtering device and the first-stage reverse osmosis device, be provided with the strainer flushing pump between dense water tank and the secondary quartz sand filtration device.
Further: the Scale inhibitors dosing tank has dosing pump.
The beneficial effects of the utility model: the reverse osmosis system of dense water backwashing strainer that utilizes of the present utility model is by before entering reverse osmosis at pretreated former water, add high efficiency scale inhibitor special, to prevent that the reverse osmosis concentrated water side from producing fouling, can reduce the number of times that film cleans like this, increase the life-span of film, enhance productivity, have practical value.By the dense water interim storage of first-stage reverse osmosis is got up, be used for quartz sand filtration device and activated charcoal filter are just being washed and backwash, water resources has been carried out fully effectively utilizing.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is structural representation of the present utility model.
Among the figure: 1. raw water box, 2. one-level quartz sand filtration device, 3. one-level active carbon filtering device, 4. first-stage reverse osmosis device, 5. dense water tank, 6. secondary quartz sand filtration device, 7. secondary active carbon filtering device, 8. Scale inhibitors dosing tank, 9. dosing pump.10. strainer flushing pump.
Embodiment
The reverse osmosis system that utilizes dense water backwashing strainer as shown in Figure 1, comprise the raw water box 1 that connects in turn, one-level quartz sand filtration device 2, one-level active carbon filtering device 3, first-stage reverse osmosis device 4, dense water tank 5, secondary quartz sand filtration device 6 and secondary active carbon filtering device 7, be provided with Scale inhibitors dosing tank 8 between one-level active carbon filtering device 3 and the first-stage reverse osmosis device 4, Scale inhibitors dosing tank 8 wherein has dosing pump 9, before entering reverse osmosis at pretreated former water, add high efficiency scale inhibitor special, to prevent that the reverse osmosis concentrated water side from producing fouling, can reduce the number of times that film cleans like this, increase the life-span of film, enhance productivity, have practical value.
Be provided with strainer flushing pump 10 between dense water tank 5 and the secondary quartz sand filtration device 6, by the dense water interim storage of first-stage reverse osmosis is got up, be used for secondary quartz sand filtration device 6 and secondary active carbon filtering device 7 are just being washed and backwash, water resources has been carried out fully effectively utilizing.

Claims (2)

1. reverse osmosis system that utilizes dense water backwashing strainer, it is characterized in that: comprise the raw water box (1) that connects in turn, one-level quartz sand filtration device (2), one-level active carbon filtering device (3), first-stage reverse osmosis device (4), dense water tank (5), secondary quartz sand filtration device (6) and secondary active carbon filtering device (7), be provided with Scale inhibitors dosing tank (8) between one-level active carbon filtering device (3) and the first-stage reverse osmosis device (4), be provided with strainer flushing pump (10) between dense water tank (5) and the secondary quartz sand filtration device (6).
2. the reverse osmosis system that utilizes dense water backwashing strainer according to claim 1, it is characterized in that: described Scale inhibitors dosing tank (8) has dosing pump (9).
CN 201320179688 2013-04-11 2013-04-11 Reverse osmosis system for backwashing filter by using concentrated water Expired - Fee Related CN203212407U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320179688 CN203212407U (en) 2013-04-11 2013-04-11 Reverse osmosis system for backwashing filter by using concentrated water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320179688 CN203212407U (en) 2013-04-11 2013-04-11 Reverse osmosis system for backwashing filter by using concentrated water

Publications (1)

Publication Number Publication Date
CN203212407U true CN203212407U (en) 2013-09-25

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320179688 Expired - Fee Related CN203212407U (en) 2013-04-11 2013-04-11 Reverse osmosis system for backwashing filter by using concentrated water

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CN (1) CN203212407U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104944529A (en) * 2015-07-16 2015-09-30 李达信 Reverse osmosis water purifier
CN105621534A (en) * 2014-11-06 2016-06-01 佛山市顺德区美的饮水机制造有限公司 High-pressure energy accumulation backwash filtration equipment
CN108640343A (en) * 2018-05-14 2018-10-12 北京赛科康仑环保科技有限公司 A kind for the treatment of process for industrial wastewater near-zero release
CN112645486A (en) * 2020-11-26 2021-04-13 河南晶锐冷却技术股份有限公司 Spraying water supplementing system and method for converter valve external cooling system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105621534A (en) * 2014-11-06 2016-06-01 佛山市顺德区美的饮水机制造有限公司 High-pressure energy accumulation backwash filtration equipment
CN105621534B (en) * 2014-11-06 2020-06-05 佛山市顺德区美的饮水机制造有限公司 High-pressure energy-storage backwashing filtering equipment
CN104944529A (en) * 2015-07-16 2015-09-30 李达信 Reverse osmosis water purifier
CN108640343A (en) * 2018-05-14 2018-10-12 北京赛科康仑环保科技有限公司 A kind for the treatment of process for industrial wastewater near-zero release
CN112645486A (en) * 2020-11-26 2021-04-13 河南晶锐冷却技术股份有限公司 Spraying water supplementing system and method for converter valve external cooling system

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130925

Termination date: 20150411

EXPY Termination of patent right or utility model