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CN201801433U - Concentrated water recovering system - Google Patents

Concentrated water recovering system Download PDF

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Publication number
CN201801433U
CN201801433U CN2010202840909U CN201020284090U CN201801433U CN 201801433 U CN201801433 U CN 201801433U CN 2010202840909 U CN2010202840909 U CN 2010202840909U CN 201020284090 U CN201020284090 U CN 201020284090U CN 201801433 U CN201801433 U CN 201801433U
Authority
CN
China
Prior art keywords
water
dense water
reverse osmosis
dense
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 - Lifetime
Application number
CN2010202840909U
Other languages
Chinese (zh)
Inventor
侯绪华
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.)
Huarun C'estbon drinks (China) Co. Ltd.
Original Assignee
Huanrun Estbon Food & Beverage (shenzhen) Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Huanrun Estbon Food & Beverage (shenzhen) Co Ltd filed Critical Huanrun Estbon Food & Beverage (shenzhen) Co Ltd
Priority to CN2010202840909U priority Critical patent/CN201801433U/en
Application granted granted Critical
Publication of CN201801433U publication Critical patent/CN201801433U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

A concentrated water recovering system comprises a concentrated water recovering tank, a concentrated water high-pressure pump and a reverse osmosis device which are connected in sequence through a pipeline; and a scale inhibitor adding device for preventing concentrated water from scaling and a pH adjusting device for adjusting the pH value of the concentrated water are arranged between the concentrated water recovering tank and the concentrated water high-pressure pump. After recovering and reprocessing concentrated water, the concentrated water recovering system can produce water which meets the use requirements and can be reused, and is recovered into a raw water tank or is used as production water. Therefore, the water production efficiency of a purified water production system is improved, and water resource is saved.

Description

Dense water reclamation system
Technical field
The utility model relates to the dense water reclamation system in a kind of pure water production process.
Background technology
It is comparatively general that reverse osmosis unit is used to produce pure water, it has the water quality treatment wide ranges, it is good to produce water water quality, characteristics such as environmental protection, but because reverse osmosis unit is along with the carrying out of demineralising process, influenced by multiple factors such as dense polarization of reverse osmosis face and osmotic pressure, determined the current operation scheme of reverse osmosis unit to move for the cross-flow mode, thereby reverse osmosis unit need discharge a certain amount of dense water (be generally flooding quantity 25%), usually the reverse osmosis concentrated water salinity is very high, be about 4 times of former water, because meeting, it does not produce and the domestic water requirement, so conventional pure water Production Flow Chart is directly drained the dense water of this part as waste water, cause waste with water resources.
Summary of the invention
The technical problems to be solved in the utility model is to overcome the deficiency that above-mentioned prior art exists, and a kind of dense water reclamation system is provided, and it has improved the producing water ratio of pure water production system, has saved water resources.
For solving the problems of the technologies described above, the utility model provides a kind of dense water reclamation system, comprise:, between dense water return water tank and dense water high-pressure pump, be provided with the PH setting device of the Scale inhibitors throwing device and the dense water ph value of adjustment of the dense water fouling of control with dense water return water tank, dense water high-pressure pump and the reverse osmosis unit that pipeline is linked in sequence.
Further, described dense water reclamation system also comprises a sterilizing unit, and it is arranged on the product water rising pipe place of described reverse osmosis unit.
Further, described dense water reclamation system also comprises an electrical control cubicles, and it electrically connects with described dense water return water tank, described dense water high-pressure pump, described reverse osmosis unit, described Scale inhibitors throwing device and described PH setting device respectively.
Further, be provided with the high voltage protective switch respectively, also be provided with tensimeter at the rising pipe place of described dense water high-pressure pump at the water inlet pipe and the rising pipe place of described dense water high-pressure pump.
Further, the product water rising pipe of described reverse osmosis unit is provided with rate of flow meter, tensimeter and conductivity table, is provided with tensimeter and rate of flow meter on the dense water rising pipe of described reverse osmosis unit.
Useful technique effect of the present utility model is: this dense water reclamation system with dense water reclaim handle again after, make that producing water satisfies the water requirement, can utilize again and be recycled to raw water box or as water of productive use.After dropping into dense water reclamation system, the total rate of recovery of pure water production system can be promoted to more than 90%, has improved producing water ratio greatly, has saved water resources; Simultaneously, remain waters such as the dense water in 10% left and right sides can clean as plant area, greening, finally reach the purpose of " zero " discharging.
Description of drawings
Fig. 1 is the structural representation of the dense water reclamation system of the utility model.
Embodiment
Fig. 1 is the structural representation of the dense water reclamation system of the utility model, as shown in the figure, this dense water reclamation system comprises: the dense water return water tank 1, dense water high-pressure pump 2 and the reverse osmosis unit 3 that are linked in sequence with pipeline, the rising pipe of dense water return water tank 1 links to each other with the water inlet pipe of dense water high-pressure pump 2, and the rising pipe of dense water high-pressure pump 2 links to each other with the water inlet pipe of reverse osmosis unit 3.
In order to reduce the settling in the reverse osmosis unit, this dense water reclamation system is provided with a Scale inhibitors throwing device 4 between dense water return water tank 1 and dense water high-pressure pump 2, scale deposition thing in its may command reverse osmosis unit, effectively control lime carbonate, Calucium Silicate powder and the fouling of calcium sulfate dirt, thus improve water production rate and produce quality.
Also be provided with a PH setting device 5 between dense water return water tank 1 and dense water high-pressure pump 2, it is in order to improve the pH value of intaking before the reverse osmosis unit 3, with a small amount of CO that exists in the dense water 2Be converted into HCO 3Deng negatively charged ion, be beneficial to it and in reverse osmosis unit 3, remove.
This dense water reclamation system also comprises an electrical control cubicles 6, it electrically connects with dense water return water tank 1, dense water high-pressure pump 2, reverse osmosis unit 3, Scale inhibitors throwing device 4 and PH setting device 5 respectively, moves by preset program to control dense water return water tank 1, dense water high-pressure pump 2, reverse osmosis unit 3, Scale inhibitors throwing device 4 and PH setting device 5.
Water inlet pipe and rising pipe place in dense water high-pressure pump 2 are provided with high voltage protective switch P S respectively, also are provided with tensimeter PI at the rising pipe place of dense water high-pressure pump 2.The product water rising pipe of reverse osmosis unit 3 is provided with rate of flow meter FI, tensimeter PI and conductivity table CI, is provided with tensimeter PI and rate of flow meter FI on the dense water rising pipe of reverse osmosis unit 3.
On the product water water pipe of reverse osmosis unit 3, also be provided with to producing the water germ-resistant sterilizing unit (not shown) that carries out disinfection, to satisfy the requirement of water.
The working process of this dense water reclamation system is as follows: the dense water of the RO in the pure water production system is pooled in the dense water return water tank 1, the water outlet of dense water collection box 1 is after adding Scale inhibitors and regulating pH value, squeeze in the reverse osmosis unit 3 through dense water high-pressure pump 2, to remove the salinity in the dense water, make water outlet reach former water water inlet requirement, water outlet enters sterilisation system to reach the water requirement, realizes dense Water reuse utilization, saves production cost.
The above only is a preferable possible embodiments of the present utility model, and unrestricted protection domain of the present utility model, and the equivalent structure that all utilization the utility model specification sheetss and accompanying drawing content have been done changes, and all is included in the protection domain of the present utility model.

Claims (5)

1. dense water reclamation system, it is characterized in that, comprise:, between dense water return water tank and dense water high-pressure pump, be provided with the PH setting device of the Scale inhibitors throwing device and the dense water ph value of adjustment of the dense water fouling of control with dense water return water tank, dense water high-pressure pump and the reverse osmosis unit that pipeline is linked in sequence.
2. dense water reclamation system as claimed in claim 1 is characterized in that, also comprises a sterilizing unit, and it is arranged on the product water rising pipe place of described reverse osmosis unit.
3. dense water reclamation system as claimed in claim 1, it is characterized in that, also comprise an electrical control cubicles, it electrically connects with described dense water return water tank, described dense water high-pressure pump, described reverse osmosis unit, described Scale inhibitors throwing device and described PH setting device respectively.
4. dense water reclamation system as claimed in claim 1 is characterized in that, is provided with the high voltage protective switch respectively at the water inlet pipe and the rising pipe place of described dense water high-pressure pump, also is provided with tensimeter at the rising pipe place of described dense water high-pressure pump.
5. dense water reclamation system as claimed in claim 1 is characterized in that, the product water rising pipe of described reverse osmosis unit is provided with rate of flow meter, tensimeter and conductivity table, is provided with tensimeter and rate of flow meter on the dense water rising pipe of described reverse osmosis unit.
CN2010202840909U 2010-08-06 2010-08-06 Concentrated water recovering system Expired - Lifetime CN201801433U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202840909U CN201801433U (en) 2010-08-06 2010-08-06 Concentrated water recovering system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202840909U CN201801433U (en) 2010-08-06 2010-08-06 Concentrated water recovering system

Publications (1)

Publication Number Publication Date
CN201801433U true CN201801433U (en) 2011-04-20

Family

ID=43870949

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202840909U Expired - Lifetime CN201801433U (en) 2010-08-06 2010-08-06 Concentrated water recovering system

Country Status (1)

Country Link
CN (1) CN201801433U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102815810A (en) * 2011-06-10 2012-12-12 通用电气公司 Desalination system and desalination method
CN102897949A (en) * 2012-10-15 2013-01-30 邯郸市奥博水处理有限公司 Drug special for reverse-osmosis concentrate water zero emission and use method thereof
CN106145263A (en) * 2015-04-28 2016-11-23 至砾机电设备(上海)有限公司 A kind of reverse osmosis concentrated reusing device for waste water and method
CN110054306A (en) * 2019-04-02 2019-07-26 南通常安能源有限公司 A kind of reverse osmosis concentrated water process recovery system of steam power plant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102815810A (en) * 2011-06-10 2012-12-12 通用电气公司 Desalination system and desalination method
CN102815810B (en) * 2011-06-10 2015-04-22 通用电气公司 Desalination system and desalination method
CN102897949A (en) * 2012-10-15 2013-01-30 邯郸市奥博水处理有限公司 Drug special for reverse-osmosis concentrate water zero emission and use method thereof
CN106145263A (en) * 2015-04-28 2016-11-23 至砾机电设备(上海)有限公司 A kind of reverse osmosis concentrated reusing device for waste water and method
CN110054306A (en) * 2019-04-02 2019-07-26 南通常安能源有限公司 A kind of reverse osmosis concentrated water process recovery system of steam power plant

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: CHINA RESOURCES C'ESTBON BEVERAGE (CHINA) CO., LTD

Free format text: FORMER NAME: HUANRUN ESTBON FOOD + BEVERAGE (SHENZHEN) CO., LTD.

CP03 Change of name, title or address

Address after: 518000 Guangdong city of Shenzhen province Nanshan District Fifth Industrial Zone Lang mountain C'estbon Food & Beverage Park

Patentee after: Huarun C'estbon drinks (China) Co. Ltd.

Address before: 518000, No. 22, Lang Lang Road, North Zone, Nanshan District hi tech Zone, Shenzhen, Guangdong

Patentee before: Huanrun Estbon Food & Beverage (Shenzhen) Co., Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20110420