CN2752273Y - Chlorine dioxide compound disinfectant generator - Google Patents
Chlorine dioxide compound disinfectant generator Download PDFInfo
- Publication number
- CN2752273Y CN2752273Y CN 200420069271 CN200420069271U CN2752273Y CN 2752273 Y CN2752273 Y CN 2752273Y CN 200420069271 CN200420069271 CN 200420069271 CN 200420069271 U CN200420069271 U CN 200420069271U CN 2752273 Y CN2752273 Y CN 2752273Y
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- China
- Prior art keywords
- anode
- chlorine dioxide
- utility
- model
- cooling water
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Abstract
The utility model discloses a chlorine dioxide compound disinfectant generator. The utility model is used for the sterilization, the algae removal, the discoloring, the odor removal, the COD and BOD index reduction, etc. on various industrial sewage, industrial circulating water, drinking water, hospital sewage and domestic sewage. A quartz micropore permeable diaphragm is arranged between an anode and a cathode, and the anode, the cathode and the quartz diaphragm are all the tube type and are in concentric arrangement. A cooling water inlet and a cooling water outlet are arranged in an anode center tube. The service life of the anode of the utility model can improve by more than ten times. The utility model has the advantages of no scale formation in electrolysis, low failure rate, easy control on use conditions, convenient maintenance and servicing, good cooling effect and enhancement of electrolysis efficiency. The current efficiency is larger than 95 percents, the salt utilization rate achieves more than 95 percents, the chlorine content can achieve 88-90%, and chlorine dioxide and other disinfection gases O2 and O3 occupy 10-12%. The disinfection effect is enhanced, and the operation cost is low.
Description
Technical field
The utility model relates to the electrolysis chlorine dioxide compound disinfectant generator of aspects such as a kind of sterilization that is widely used in all types of industries sewage, industrial circulating water, tap water, hospital sewage, sanitary sewage, algae removal, decolouring, taste removal, reduction COD, BOD index.
Background technology
Existing electrolysis chlorine dioxide generator, the subject matter of existence are that electrode is easy to damage, be easy to fouling, failure rate height during electrolysis, mainly are the outer no barrier films of electrode.Reported at present at the electrode skin and established asbestos diaphragm or ionic membrane barrier film, it can make electrode life lengthening, but the life-span that asbestos diaphragm uses is short, efficient is low, its barrier film is made also difficulty, yield rate is low, be difficult for promoting the use of; Ionic membrane barrier film then production cost height, working conditions harshness, maintaining difficulty, product also is difficult to promote the use of.Do not have independently cooling water system design in the prior art, cause electrolyzer temperature too high, cooling performance is not ideal, easily causes structure deteriorate, and electrolytic efficiency is lower, and general current efficiency has only about 80%.
The utility model content
The purpose of this utility model is to provide that a kind of failure rate is low, long service life, electrolytic efficiency height, can produce ClO simultaneously
2, CL
2, O
2, O
3The electrolysis chlorine dioxide compound disinfectant generator.
The utility model comprises strong brine import, strainer, softening agent, by electrolyzer, cooling water intakeoutfall, leakage fluid dram that anode and negative electrode are formed, it is characterized in that between anode and negative electrode, being provided with the quartz micropores permeable membrane.
Anode, negative electrode, quartzy barrier film are tubular type and install with one heart;
Entrance of cooling water is located in anodes centre's pipe.
In real work, can be designed to different models, concrete numerical value such as following table according to different requirements:
HLS-B series electrolysis chlorine dioxide compound disinfectant generator processing parameter
The utility model adopts the quartz micropores permeable membrane, and for asbestos diaphragm or ionic membrane barrier film, it is also convenient that its long service life, making are easily, yield rate is high, working conditions is easy to control, maintaining, so be easy to promote the use of.It can make anodic improve more than ten times work-ing life after deliberation, and non flouling behaviour during electrolysis, failure rate are low.The utility model is installed with one heart owing to anode, negative electrode adopt tubular type simultaneously, and cooling water intakeoutfall all is located in anodes centre's pipe, and good cooling results, electrolytic efficiency improve greatly, and current efficiency can be greater than 95%, and the salt utilization ratio reaches more than 95%; Cl content reaches 88-90%, and dioxide peroxide and other sterilization property gas O2, O3 account for 10-12%, have improved sterilisation effect greatly, and running cost is low.
Description of drawings
Fig. 1 is the utility model external structure synoptic diagram;
Fig. 2 is the electrode system schema.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment 1
With reference to accompanying drawing 1:
1 is strainer, and 2 is softening agent, and 3 is the electrolyzer of being made up of anode and negative electrode.
With reference to accompanying drawing 2:
Present embodiment electrolyzer quantity is four, anode 4 in the electrolyzer and negative electrode 5 are installed with one heart for tubular type, in the middle of anode 4 and negative electrode 5, be provided with quartz micropores permeable membrane 6, strong brine enters electrolyzer by salt water inlet 7, when electrolyzer feeds direct current, electrochemical reaction and chemical reaction take place, and produce ClO in the electrolytic process
2, CL
2, O
2, O
3Composite disinfectant, composite disinfectant is discharged from exporting 10, water coolant flows out from the outlet 9 of negative electrode outer wall after be located at import 8 in anodes centre's pipe and flow to and cool off again; Can obtain the two refrigerative effects of cathode and anode like this, reacted alkali lye is discharged from leakage fluid dram 11.The current efficiency of present embodiment is greater than 95%.The salt utilization ratio reaches more than 95%; Cl content reaches 88%, and dioxide peroxide and other sterilization property gas O2, O3 account for 12%.
Claims (3)
1. chlorine dioxide compound disinfectant generator comprises strong brine import, strainer, softening agent, by electrolyzer, cooling water intakeoutfall, leakage fluid dram that anode, negative electrode are formed, it is characterized in that being provided with between anode and negative electrode the quartz micropores permeable membrane.
2. electrolysis chlorine dioxide compound disinfectant generator according to claim 1 is characterized in that anode, negative electrode, quartzy barrier film are tubular type and installation with one heart.
3. chlorine dioxide generator according to claim 1 is characterized in that cooling water intakeoutfall is located in anodes centre's pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420069271 CN2752273Y (en) | 2004-11-26 | 2004-11-26 | Chlorine dioxide compound disinfectant generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420069271 CN2752273Y (en) | 2004-11-26 | 2004-11-26 | Chlorine dioxide compound disinfectant generator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2752273Y true CN2752273Y (en) | 2006-01-18 |
Family
ID=35913682
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200420069271 Expired - Fee Related CN2752273Y (en) | 2004-11-26 | 2004-11-26 | Chlorine dioxide compound disinfectant generator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2752273Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103060836A (en) * | 2013-02-01 | 2013-04-24 | 湖南海尔斯环境工程有限公司 | Chlorine dioxide composite disinfectant generator employing electrolytic process |
CN104674296A (en) * | 2015-03-16 | 2015-06-03 | 张学武 | Electrolytic chlorine dioxide generator and electrolytic cell |
-
2004
- 2004-11-26 CN CN 200420069271 patent/CN2752273Y/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103060836A (en) * | 2013-02-01 | 2013-04-24 | 湖南海尔斯环境工程有限公司 | Chlorine dioxide composite disinfectant generator employing electrolytic process |
CN103060836B (en) * | 2013-02-01 | 2016-05-11 | 宋力 | A kind of electrolysis chlorine dioxide compound disinfectant generator |
CN104674296A (en) * | 2015-03-16 | 2015-06-03 | 张学武 | Electrolytic chlorine dioxide generator and electrolytic cell |
CN104674296B (en) * | 2015-03-16 | 2017-11-14 | 张学武 | A kind of electrolysis chlorine dioxide generator and electrolytic cell |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060118 Termination date: 20101126 |