CN205275366U - Desalinized water device - Google Patents
Desalinized water device Download PDFInfo
- Publication number
- CN205275366U CN205275366U CN201521108170.8U CN201521108170U CN205275366U CN 205275366 U CN205275366 U CN 205275366U CN 201521108170 U CN201521108170 U CN 201521108170U CN 205275366 U CN205275366 U CN 205275366U
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- China
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- bed
- water
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- water tank
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- 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 provides a desalinized water device, it includes multi -media filter (1), activated carbon filter (2), ultrafiltration system (3), super water filter tank (4), elevator pump (5), reverse osmosis system (6), horizontal water tank (7), sun bed (8), cloudy bed (9), muddy bed (10), desalination water tank (11), solenoid valve (12), three solenoid valve (13), specific conductivity apparatus (14) and PLC controller, the utility model discloses the advantage is: improve the desalinized water negative and positive bed rate of utilization and desalinized water quality, the desalinized water workshop section reliability and the ability to ward off risks obtain improving. (B /)
Description
Technical field
This utility model relates to desalted water field, is specifically related to a kind of removal bitter and fishiness.
Background technology
At present, factory fetches water in the Changjiang river, raw water quality is extremely unstable, and the equipment operation maintenance such as ultrafiltration, reverse osmosis needs very fine, and early stage to produce desalted water flow process all linked with one another, indispensable, any appliance breaks down and will result directly in desalted water stopping production, finally affects acid making system and normally produces. Meanwhile, because the duration of service such as reverse osmosis, ultrafiltration is longer, disposal ability is limited, causes negative and positive bed load weight, ultimately results in desalted water electrical conductivity higher, exports electrical conductivity once anion bed and just need to negative and positive bed resin be regenerated more than 5 �� s/cm.
Utility model content
The purpose of this utility model is aiming at present, factory fetches water in the Changjiang river, raw water quality is extremely unstable, and the equipment operation maintenance such as ultrafiltration, reverse osmosis needs very fine, and early stage to produce desalted water flow process all linked with one another, indispensable, any appliance breaks down and will result directly in desalted water stopping production, finally affects acid making system and normally produces. Meanwhile, because the duration of service such as reverse osmosis, ultrafiltration is longer, disposal ability is limited, cause negative and positive bed load weight, ultimately result in desalted water electrical conductivity higher, export electrical conductivity more than the 5 �� s/cm deficiency that just negative and positive bed resin need to be regenerated once anion bed, and a kind of removal bitter and fishiness is provided.
This utility model includes more medium filter, active carbon filter, ultrafiltration system, ultrafiltration water tank, elevator pump, counter-infiltration system, horizontal water tank, cation bed, anion bed, mixed bed, desalination water tank, electromagnetic valve, three-way magnetic valve, water conductivity analyzer and PLC, the outlet of more medium filter communicates with the water inlet of active carbon filter, the outlet of active carbon filter communicates with the water inlet of ultrafiltration system, the outlet of ultrafiltration system communicates with the water inlet of ultrafiltration water tank, the outlet of ultrafiltration water tank is communicated with the water inlet of counter-infiltration system by electromagnetic valve, the outlet of counter-infiltration system communicates with the water inlet of horizontal water tank, the outlet of horizontal water tank communicates with the water inlet of cation bed, the outlet of cation bed communicates with the water inlet of anion bed, the outlet of anion bed is communicated with the water inlet of desalination water tank and mixed bed respectively by three-way magnetic valve, the outlet of mixed bed communicates with the water inlet of desalination water tank, water conductivity analyzer is arranged on the outlet of anion bed, the outlet of ultrafiltration water tank communicates with the water inlet of cation bed also by elevator pump, counter-infiltration system and water conductivity analyzer electrically connect with PLC respectively through input module, PLC controls elevator pump respectively through output module, the opening and closing of electromagnetic valve and three-way magnetic valve.
This utility model advantage is: improving desalted water negative and positive bed utilization rate and desalted water quality, desalted water workshop section reliability and the ability to ward off risks are improved.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Detailed description of the invention
As it is shown in figure 1, this utility model includes more medium filter 1, active carbon filter 2, ultrafiltration system 3, ultrafiltration water tank 4, elevator pump 5, counter-infiltration system 6, horizontal water tank 7, cation bed 8, anion bed 9, mixed bed 10, desalination water tank 11, electromagnetic valve 12, three-way magnetic valve 13, water conductivity analyzer 14 and PLC, the outlet of more medium filter 1 communicates with the water inlet of active carbon filter 2, the outlet of active carbon filter 2 communicates with the water inlet of ultrafiltration system 3, the outlet of ultrafiltration system 3 communicates with the water inlet of ultrafiltration water tank 4, the outlet of ultrafiltration water tank 4 is communicated by the water inlet of electromagnetic valve 12 with counter-infiltration system 6, the outlet of counter-infiltration system 6 communicates with the water inlet of horizontal water tank 7, the outlet of horizontal water tank 7 communicates with the water inlet of cation bed 8, the outlet of cation bed 8 communicates with the water inlet of anion bed 9, the outlet of anion bed 9 is communicated with the water inlet of desalination water tank 11 and mixed bed 10 respectively by three-way magnetic valve 13, the outlet of mixed bed 10 communicates with the water inlet of desalination water tank 11, water conductivity analyzer 14 is arranged on the outlet of anion bed 9, the outlet of ultrafiltration water tank 4 communicates also by the water inlet of elevator pump 5 with cation bed 8, counter-infiltration system 6 and water conductivity analyzer 14 electrically connect with PLC respectively through input module, PLC controls elevator pump 5 respectively through output module, the opening and closing of electromagnetic valve 12 and three-way magnetic valve 13.
Working method: medium filter 1 under normal circumstances, active carbon filter 2, ultrafiltration system 3, ultrafiltration water tank 4, counter-infiltration system 6, horizontal water tank 7, cation bed 8, anion bed 9 and desalination water tank 11 run in order successively, when counter-infiltration system 6 breaks down, PLC controls electromagnetic valve 12 and closes, elevator pump 5 is opened, water in ultrafiltration water tank 4 is delivered directly in cation bed 8 and carries out operation below, when water from anion bed 9 out, water conductivity analyzer 14 detects that water conductivity is when 0-5 �� s/cm, three-way magnetic valve 13 enters one end valve opening of desalination water tank 11, can be delivered directly in desalination water tank 11, but detect that water conductivity is when 5-50 �� s/cm to water conductivity analyzer 14, PLC controls three-way magnetic valve 13 and enters the other end valve opening of mixed bed 10, and enter one end valve closing of desalination water tank 11, the water making anion bed 9 is delivered directly in mixed bed 10, then pass through after mixed bed 10 removes electron ion and be transported to again in desalination water tank 11.
Claims (1)
1. a removal bitter and fishiness, it is characterized in that it includes more medium filter (1), active carbon filter (2), ultrafiltration system (3), ultrafiltration water tank (4), elevator pump (5), counter-infiltration system (6), horizontal water tank (7), cation bed (8), anion bed (9), mixed bed (10), desalination water tank (11), electromagnetic valve (12), three-way magnetic valve (13), water conductivity analyzer (14) and PLC, the outlet of more medium filter (1) communicates with the water inlet of active carbon filter (2), the outlet of active carbon filter (2) communicates with the water inlet of ultrafiltration system (3), the outlet of ultrafiltration system (3) communicates with the water inlet of ultrafiltration water tank (4), the outlet of ultrafiltration water tank (4) is communicated by the water inlet of electromagnetic valve (12) with counter-infiltration system (6), the outlet of counter-infiltration system (6) communicates with the water inlet of horizontal water tank (7), the outlet of horizontal water tank (7) communicates with the water inlet of cation bed (8), the outlet of cation bed (8) communicates with the water inlet of anion bed (9), the outlet of anion bed (9) is communicated with the water inlet of desalination water tank (11) and mixed bed (10) respectively by three-way magnetic valve (13), the outlet of mixed bed (10) communicates with the water inlet of desalination water tank (11), water conductivity analyzer (14) is arranged on the outlet of anion bed (9), the outlet of ultrafiltration water tank (4) communicates also by the water inlet of elevator pump (5) with cation bed (8), counter-infiltration system (6) and water conductivity analyzer (14) electrically connect with PLC respectively through input module, PLC controls elevator pump (5) respectively through output module, the opening and closing of electromagnetic valve (12) and three-way magnetic valve (13).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521108170.8U CN205275366U (en) | 2015-12-29 | 2015-12-29 | Desalinized water device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521108170.8U CN205275366U (en) | 2015-12-29 | 2015-12-29 | Desalinized water device |
Publications (1)
Publication Number | Publication Date |
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CN205275366U true CN205275366U (en) | 2016-06-01 |
Family
ID=56059959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201521108170.8U Expired - Fee Related CN205275366U (en) | 2015-12-29 | 2015-12-29 | Desalinized water device |
Country Status (1)
Country | Link |
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CN (1) | CN205275366U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109987739A (en) * | 2017-12-29 | 2019-07-09 | 杭州水处理技术研究开发中心有限公司 | A kind of container-type seawater desalination system |
-
2015
- 2015-12-29 CN CN201521108170.8U patent/CN205275366U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109987739A (en) * | 2017-12-29 | 2019-07-09 | 杭州水处理技术研究开发中心有限公司 | A kind of container-type seawater desalination system |
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Legal Events
Date | Code | Title | Description |
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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 | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 Termination date: 20181229 |