CN204111473U - The anti-scale inhibition system of a kind of sea water purifier protection against corrosion - Google Patents
The anti-scale inhibition system of a kind of sea water purifier protection against corrosion Download PDFInfo
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- CN204111473U CN204111473U CN201420578186.4U CN201420578186U CN204111473U CN 204111473 U CN204111473 U CN 204111473U CN 201420578186 U CN201420578186 U CN 201420578186U CN 204111473 U CN204111473 U CN 204111473U
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Abstract
The utility model relates to the anti-scale inhibition system of a kind of protection against corrosion, the anti-scale inhibition system of especially a kind of sea water purifier protection against corrosion.It has to connect between seawater original water inlet end and quartz filter pipeline for for the former water of seawater is through the iron(ic) chloride device of row flocculation reaction; To connect and between iron(ic) chloride device and quartz filter, pipeline is used for carrying out disinfection the sterilant device of sterilization for the former water of seawater; Connecting pipeline between activated charcoal filter and two-stage precision strainer is that the former water of seawater carries out reduction reaction and neutralizes reductive agent device more than oxygenant; And to connect and between two-stage precision strainer and RO film filter, pipeline is used for the former water of further purification seawater and prevents it from causing the antiscaling device of in advance scale inhibition to RO film filter.Prevent RO film filter from blocking in advance, extend the work-ing life of sea water purifier, save maintenance and repair cost.The utility model is used for for carrying out the anti-scale inhibition process of protection against corrosion to the former water of seawater in seawater cleaning process.
Description
Technical field
The utility model relates to the anti-scale inhibition system of a kind of protection against corrosion, the anti-scale inhibition system of especially a kind of sea water purifier protection against corrosion.
Background technology
At present, along with reaching its maturity of reverse osmosis technology, utilizing reverse osmosis technology to desalinate seawater is a kind of way of supplying water increasing gross amount of water resources, solves the important channel of China island and coastal water-deficient region fresh water problem in short supply, ensures the optimal selection of oceangoing voyage ships water supply.In embrane method purifying sea water systematic procedure, before the former water of seawater enters RO film, removal suspended substance and colloid to be carried out to the former water of seawater, reduce turbidity, scale inhibition, chlorination and except the process such as chlorine residue, prevent RO film surface scale, dirty stifled cause product water circulation to reduce, and prevent decay and the degraded of RO mould material.How making the former water of seawater obtain effectively purifying before entering RO film is ensure seawer quality, extends the key in sea water purifier work-ing life.
Summary of the invention
The purpose of this utility model is for overcoming above-mentioned the deficiencies in the prior art, provides a kind of sea water purifier protection against corrosion anti-scale inhibition system.The former aqueous suspension particulate of seawater, macrobead organism is made to produce flocculation by iron(ic) chloride device at seawater original water inlet end, for fully being filtered, for the filter effect playing quartz filter and activated charcoal filter to greatest extent provides safeguard in the follow-up quartz filter of seawater raw water filtration and activated charcoal filter.By sterilant device, the former water of seawater is carried out disinfection sterilization, ensure that seawater cleaning quality reaches standard for drinking.By the oxidizing substance in the former water of reductive agent device reduction seawater and unnecessary chlorine, eliminate medicament unnecessary in the former water of seawater, the particulate matter in the former water of seawater is eliminated further by Scale inhibitors device, prevent RO film filter from blocking in advance, improve the working efficiency of RO film filter, extend the work-ing life of sea water purifier, save maintenance and repair cost.
For achieving the above object, the utility model adopts following technical proposals:
The anti-scale inhibition system of a kind of sea water purifier protection against corrosion, it has to connect between seawater original water inlet end and quartz filter pipeline for for the former water of seawater is through the iron(ic) chloride device of row flocculation reaction; To connect and between iron(ic) chloride device and quartz filter, pipeline is used for carrying out disinfection the sterilant device of sterilization for the former water of seawater; Connecting pipeline between activated charcoal filter and two-stage precision strainer is that the former water of seawater carries out reduction reaction and neutralizes reductive agent device more than oxygenant; And to connect and between two-stage precision strainer and RO film filter, pipeline is used for the former water of further purification seawater and prevents it from causing the antiscaling device of in advance scale inhibition to RO film filter.
Preferably, described iron(ic) chloride device comprises iron(ic) chloride device volume pump, the square dosing tank of iron(ic) chloride device, iron(ic) chloride device first control valve, iron(ic) chloride device second control valve and iron(ic) chloride device the 3rd control valve, the input terminus of described iron(ic) chloride device volume pump is connected with the square dosing tank of iron(ic) chloride device by pipeline, described iron(ic) chloride device first control valve and iron(ic) chloride device second control valve are connected on the connecting pipeline between iron(ic) chloride device volume pump and the square dosing tank of iron(ic) chloride device, described iron(ic) chloride device the 3rd control valve is placed on the pipeline between iron(ic) chloride device volume pump output terminal connection seawater original water inlet end and quartz filter.
Preferably, described sterilant device comprises sterilant device volume pump, the square dosing tank of sterilant device, sterilant device first control valve, sterilant device second control valve and sterilant device the 3rd control valve, the input terminus of described sterilant device volume pump is connected with the square dosing tank of sterilant device by pipeline, described sterilant device first control valve and sterilant device second control valve are connected on the connecting pipeline between sterilant device volume pump and the square dosing tank of sterilant device, described sterilant device the 3rd control valve is placed on the pipeline between sterilant device volume pump output terminal connection iron(ic) chloride device and quartz filter.
Preferably, described reductive agent device comprises reductive agent device volume pump, the square dosing tank of reductive agent device, reductive agent device first control valve, reductive agent device second control valve and reductive agent device the 3rd control valve, the input terminus of described reductive agent device volume pump is connected with the square dosing tank of reductive agent device by pipeline, described reductive agent device first control valve and reductive agent device second control valve are connected on the connecting pipeline between reductive agent device volume pump and the square dosing tank of reductive agent device, described reductive agent device the 3rd control valve is placed on the pipeline between reductive agent device volume pump output terminal connection activated charcoal filter and two-stage precision strainer.
Preferably, described Scale inhibitors device comprises Scale inhibitors device volume pump, the square dosing tank of Scale inhibitors device, Scale inhibitors device first control valve, Scale inhibitors device second control valve and Scale inhibitors device the 3rd control valve, the input terminus of described Scale inhibitors device volume pump is connected with the square dosing tank of Scale inhibitors device by pipeline, described Scale inhibitors device first control valve and Scale inhibitors device second control valve are connected on the connecting pipeline between Scale inhibitors device volume pump and the square dosing tank of Scale inhibitors device, described Scale inhibitors device the 3rd control valve is placed on the pipeline between Scale inhibitors device volume pump output terminal connection two-stage precision strainer and RO film filter.
The beneficial effects of the utility model are: the utility model is reasonable in design, first the former aqueous suspension particulate of seawater, macrobead organism is made to produce flocculation by iron(ic) chloride device at seawater original water inlet end, for fully being filtered, for the filter effect playing quartz filter and activated charcoal filter to greatest extent provides safeguard in the follow-up quartz filter of seawater raw water filtration and activated charcoal filter.By sterilant device, the former water of seawater is carried out disinfection sterilization, ensure that seawater cleaning quality reaches standard for drinking.By the oxidizing substance in the former water of reductive agent device reduction seawater and unnecessary chlorine, eliminate medicament unnecessary in the former water of seawater, the particulate matter in the former water of seawater is eliminated further by Scale inhibitors device, prevent RO film filter from blocking in advance, improve the working efficiency of RO film filter, extend the work-ing life of sea water purifier, save maintenance and repair cost.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Wherein 1 seawater original water inlet end, 2 quartz filters, 3 activated charcoal filters, 4 two-stage precision strainers, 5 RO film filters, 6 iron(ic) chloride devices, 6-1 iron(ic) chloride device volume pump, the square dosing tank of 6-2 iron(ic) chloride device, 6-3 iron(ic) chloride device first control valve, 6-4 iron(ic) chloride device second control valve, 6-5 iron(ic) chloride device the 3rd control valve, 7 sterilant devices, 7-1 sterilant device volume pump, the square dosing tank of 7-2 sterilant device, 7-3 sterilant device first control valve, 7-4 sterilant device second control valve, 7-5 sterilant device the 3rd control valve, 8 reductive agent devices, 8-1 reductive agent device volume pump, the square dosing tank of 8-2 reductive agent device, 8-3 reductive agent device first control valve, 8-4 reductive agent device second control valve, 8-5 reductive agent device the 3rd control valve, 9 Scale inhibitors devices, 9-1 Scale inhibitors device volume pump, the square dosing tank of 9-2 Scale inhibitors device, 9-3 Scale inhibitors device first control valve, 9-4 Scale inhibitors device second control valve, 9-5 Scale inhibitors device the 3rd control valve.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated.
The anti-scale inhibition system of a kind of sea water purifier protection against corrosion, it has to connect between seawater original water inlet end 1 and quartz filter 2 pipeline for for the former water of seawater is through the iron(ic) chloride device 6 of row flocculation reaction; To connect and between iron(ic) chloride device 6 and quartz filter 2, pipeline is used for carrying out disinfection the sterilant device 7 of sterilization for the former water of seawater; Connecting pipeline between activated charcoal filter 3 and two-stage precision strainer 4 is that the former water of seawater carries out reduction reaction and neutralizes reductive agent device 8 more than oxygenant; And to connect and between two-stage precision strainer 4 and RO film filter 5, pipeline is used for the former water of further purification seawater and prevents it from causing the antiscaling device 9 of in advance scale inhibition to RO film filter.
On technique scheme basis, described iron(ic) chloride device 6 comprises iron(ic) chloride device volume pump 6-1, the square dosing tank 6-2 of iron(ic) chloride device, iron(ic) chloride device first control valve 6-3, iron(ic) chloride device second control valve 6-4 and iron(ic) chloride device the 3rd control valve 6-5, the input terminus of described iron(ic) chloride device volume pump 6-1 is connected by the square dosing tank 6-2 of pipeline and iron(ic) chloride device, described iron(ic) chloride device first control valve 6-3 and iron(ic) chloride device second control valve 6-4 is connected on the connecting pipeline between iron(ic) chloride device volume pump 6-1 and the square dosing tank 6-2 of iron(ic) chloride device, described iron(ic) chloride device the 3rd control valve 6-5 is placed on the pipeline between iron(ic) chloride device volume pump 6-1 output terminal connection seawater original water inlet end 1 and quartz filter 2.
On technique scheme basis, described sterilant device 7 comprises sterilant device volume pump 7-1, the square dosing tank 7-2 of sterilant device, sterilant device first control valve 7-3, sterilant device second control valve 7-4 and sterilant device the 3rd control valve 7-5, the input terminus of described sterilant device volume pump 7-1 is connected by the square dosing tank 7-2 of pipeline and sterilant device, described sterilant device first control valve 7-3 and sterilant device second control valve 7-4 is connected on the connecting pipeline between sterilant device volume pump 7-1 and the square dosing tank 7-2 of sterilant device, described sterilant device the 3rd control valve 7-5 is placed on the pipeline between sterilant device volume pump 7-1 output terminal connection iron(ic) chloride device 6 and quartz filter 2.
On technique scheme basis, described reductive agent device 8 comprises reductive agent device volume pump 8-1, the square dosing tank 8-2 of reductive agent device, reductive agent device first control valve 8-3, reductive agent device second control valve 8-4 and reductive agent device the 3rd control valve 8-5, the input terminus of described reductive agent device volume pump 8-1 is connected by the square dosing tank 8-2 of pipeline and reductive agent device, described reductive agent device first control valve 8-3 and reductive agent device second control valve 8-4 is connected on the connecting pipeline between reductive agent device volume pump 8-1 and the square dosing tank 8-2 of reductive agent device, described reductive agent device the 3rd control valve 8-5 is placed on the pipeline between reductive agent device volume pump 8-1 output terminal connection activated charcoal filter 3 and two-stage precision strainer 4.
On technique scheme basis, described Scale inhibitors device 9 comprises Scale inhibitors device volume pump 9-1, the square dosing tank 9-2 of Scale inhibitors device, Scale inhibitors device first control valve 9-3, Scale inhibitors device second control valve 9-4 and Scale inhibitors device the 3rd control valve 9-5, the input terminus of described Scale inhibitors device metering 9-1 is connected by the square dosing tank 9-2 of pipeline and Scale inhibitors device, described Scale inhibitors device first control valve 9-3 and Scale inhibitors device second control valve 9-4 is connected on the connecting pipeline between Scale inhibitors device volume pump 9-1 and the square dosing tank 9-2 of Scale inhibitors device, described Scale inhibitors device the 3rd control valve 9-5 is placed on the pipeline between Scale inhibitors device volume pump 9-1 output terminal connection two-stage precision strainer 4 and RO film filter 5.
By reference to the accompanying drawings embodiment of the present utility model is described although above-mentioned; but the restriction not to the utility model protection domain; one of ordinary skill in the art should be understood that; on the basis of the technical solution of the utility model, those skilled in the art do not need to pay various amendment or distortion that creative work can make still within protection domain of the present utility model.
Claims (5)
1. the anti-scale inhibition system of sea water purifier protection against corrosion, is characterized in that: it has to connect between seawater original water inlet end and quartz filter pipeline for for the former water of seawater is through the iron(ic) chloride device of row flocculation reaction; To connect and between iron(ic) chloride device and quartz filter, pipeline is used for carrying out disinfection the sterilant device of sterilization for the former water of seawater; Connecting pipeline between activated charcoal filter and two-stage precision strainer is that the former water of seawater carries out reduction reaction and neutralizes reductive agent device more than oxygenant; And to connect and between two-stage precision strainer and RO film filter, pipeline is used for the former water of further purification seawater and prevents it from causing the antiscaling device of in advance scale inhibition to RO film filter.
2. the anti-scale inhibition system of a kind of sea water purifier protection against corrosion as claimed in claim 1, it is characterized in that: described iron(ic) chloride device comprises iron(ic) chloride device volume pump, the square dosing tank of iron(ic) chloride device, iron(ic) chloride device first control valve, iron(ic) chloride device second control valve and iron(ic) chloride device the 3rd control valve, the input terminus of described iron(ic) chloride device volume pump is connected with the square dosing tank of iron(ic) chloride device by pipeline, described iron(ic) chloride device first control valve and iron(ic) chloride device second control valve are connected on the connecting pipeline between iron(ic) chloride device volume pump and the square dosing tank of iron(ic) chloride device, described iron(ic) chloride device the 3rd control valve is placed on the pipeline between iron(ic) chloride device volume pump output terminal connection seawater original water inlet end and quartz filter.
3. the anti-scale inhibition system of a kind of sea water purifier protection against corrosion as claimed in claim 1, it is characterized in that: described sterilant device comprises sterilant device volume pump, the square dosing tank of sterilant device, sterilant device first control valve, sterilant device second control valve and sterilant device the 3rd control valve, the input terminus of described sterilant device volume pump is connected with the square dosing tank of sterilant device by pipeline, described sterilant device first control valve and sterilant device second control valve are connected on the connecting pipeline between sterilant device volume pump and the square dosing tank of sterilant device, described sterilant device the 3rd control valve is placed on the pipeline between sterilant device volume pump output terminal connection iron(ic) chloride device and quartz filter.
4. the anti-scale inhibition system of a kind of sea water purifier protection against corrosion as claimed in claim 1, it is characterized in that: described reductive agent device comprises reductive agent device volume pump, the square dosing tank of reductive agent device, reductive agent device first control valve, reductive agent device second control valve and reductive agent device the 3rd control valve, the input terminus of described reductive agent device volume pump is connected with the square dosing tank of reductive agent device by pipeline, described reductive agent device first control valve and reductive agent device second control valve are connected on the connecting pipeline between reductive agent device volume pump and the square dosing tank of reductive agent device, described reductive agent device the 3rd control valve is placed on the pipeline between reductive agent device volume pump output terminal connection activated charcoal filter and two-stage precision strainer.
5. the anti-scale inhibition system of a kind of sea water purifier protection against corrosion as claimed in claim 1, it is characterized in that: described Scale inhibitors device comprises Scale inhibitors device volume pump, the square dosing tank of Scale inhibitors device, Scale inhibitors device first control valve, Scale inhibitors device second control valve and Scale inhibitors device the 3rd control valve, the input terminus of described Scale inhibitors device volume pump is connected with the square dosing tank of Scale inhibitors device by pipeline, described Scale inhibitors device first control valve and Scale inhibitors device second control valve are connected on the connecting pipeline between Scale inhibitors device volume pump and the square dosing tank of Scale inhibitors device, described Scale inhibitors device the 3rd control valve is placed on the pipeline between Scale inhibitors device volume pump output terminal connection two-stage precision strainer and RO film filter.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420578186.4U CN204111473U (en) | 2014-10-08 | 2014-10-08 | The anti-scale inhibition system of a kind of sea water purifier protection against corrosion |
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| CN201420578186.4U CN204111473U (en) | 2014-10-08 | 2014-10-08 | The anti-scale inhibition system of a kind of sea water purifier protection against corrosion |
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| CN204111473U true CN204111473U (en) | 2015-01-21 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540938A (en) * | 2016-02-18 | 2016-05-04 | 佛山市雅洁源科技股份有限公司 | High-salinity water processing device |
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- 2014-10-08 CN CN201420578186.4U patent/CN204111473U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540938A (en) * | 2016-02-18 | 2016-05-04 | 佛山市雅洁源科技股份有限公司 | High-salinity water processing device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 266510 9 Songhua River Road, Qingdao economic and Technological Development Zone, Shandong Patentee after: QINGDAO ZHONGCHE HUAXUAN WATER Co.,Ltd. Address before: 266510 9 Songhua River Road, Qingdao economic and Technological Development Zone, Shandong Patentee before: CSR Qingdao Huaxuan Water Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 266510 9 Songhua River Road, Qingdao economic and Technological Development Zone, Shandong Patentee after: Qingdao CRRC Times New Energy Material Technology Co.,Ltd. Address before: 266510 9 Songhua River Road, Qingdao economic and Technological Development Zone, Shandong Patentee before: QINGDAO ZHONGCHE HUAXUAN WATER Co.,Ltd. |