CN2061177U - Electrolytic chlorine dioxide generator - Google Patents
Electrolytic chlorine dioxide generator Download PDFInfo
- Publication number
- CN2061177U CN2061177U CN 89209620 CN89209620U CN2061177U CN 2061177 U CN2061177 U CN 2061177U CN 89209620 CN89209620 CN 89209620 CN 89209620 U CN89209620 U CN 89209620U CN 2061177 U CN2061177 U CN 2061177U
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- CN
- China
- Prior art keywords
- electrolytic
- diaphragm
- utility
- electrolysis
- tube
- 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.)
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Abstract
The utility model relates to an electrolytic chlorine dioxide generator which overcomes the defects of inconvenient installment, short usage time of a diaphragm and low electrolytic efficiency, etc. existing in the prior art. The utility model provides the electrolytic chlorine dioxide generator with simple installation and high electrolytic efficiency. The utility model comprises a titanium alloy anode pipe, a tube-shaped neutral ion diaphragm a titanium steel cathode casing, an air inlet, a delivery outlet, the electrolytic inner and the outer chambers, a support frame, etc; Wherein, the anode tube is arranged in the tube-shaped neutral ion diaphragm, and the ion diaphragm is arranged in the titanium steel cathode casing; the electrolytic inner and the outer chambers are arranged among the anode tube, the tube-shaped neutral ion diaphragm and the titanium steel cathode casing. The utility model has the advantages of great gas production, long service life, unease hung dirt of the diaphragm, simple structure and free from the limit of installing direction.
Description
The utility model relates to a kind of chlorine dioxide generating device.
The generating unit of current electrolysis dioxide peroxide as shown in Figure 1, it is that U.S. TETRAVALENT company (tetravalence company) produces, and it includes compositions such as stainless steel cathode shell, graphite rod electrode (neutrality), titanium alloy reticulated plate electrode (anode), inside and outside tank room.Have four apertures in the side of cathode shell, and paste barrier film with silica gel.During installation, web plate shape electrode must parallel with graphite rod (face that is web plate faces ion diaphragm).Otherwise electrolytic efficiency is low.Its shortcoming is that electrolytic efficiency is lower, gas production rate little (chlorine yield 40 Grams Per Hours), and barrier film is hung dirt easily, be subject to the charcoal dirt obstruction that ionization is come out simultaneously, can't use, inconvenience is installed, membranous work-ing life is short, and the mistress must use the salt solution of aquae destillata dilution in the electrolysis.
The utility model provides a kind of simple installation, the generating unit of the dioxide peroxide that electrolytic efficiency is high.
Technical solution of the present utility model is: structure as shown in Figure 2.It includes the Ti-alloy anode pipe, titanium steel cathode shell, tubular neutral ion barrier film, connecting ear, upper cover plate, inlet mouth, air outlet, row's hydrogen mouth, mistress in the electrolysis, support etc.Wherein the Ti-alloy anode pipe is installed in the tubular ion diaphragm, between certain interval is arranged, form the electrolysis inner room, during installation not the recipient to restriction (can 360 ° of installations).Tubular neutral ion barrier film is installed in the cathode shell, between have certain interval to form the electrolysis mistress.In the tube ion diaphragm of garden, inlet mouth and air outlet are installed.Salt solution is contained in mistress in the electrolysis, after the electrolysis, by the ion diaphragm exchange sodium ion is separated to the mistress, sends by the discharge outlet of cathode shell bottom again.The big I of the drum diameter of tubular ion diaphragm is decided according to electrolysis output.
Principle of work of the present utility model is: electrolytic solution (salt solution) is put into the electrolysis mistress.Carry out electrolysis by the neutral ion barrier film, produce multiple gaseous oxidizers such as dioxide peroxide, chlorine, hydrogen peroxide, ozone.The neutral ion barrier film forms an electricity and builds in electrolytic process, unidirectional conducting is separated sodium ion.The electrolysis inner room produces multiple gaseous oxidizer (comprising dioxide peroxide) under electric field and membranous effect.Export by delivery port.
Because the utility model has adopted annular garden tubular neutral ion barrier film and sheath, this just makes the diel surface increase, thereby has improved electrolytic efficiency (chlorine yield).Cathode shell has adopted titanium steel simultaneously, strengthens erosion resistance, and is in light weight.
Description of drawings:
Fig. 1 is the structural representation of the electrolysis chlorine dioxide generating device of U.S. tetravalence company production.
Fig. 2 is a structural representation of the present utility model.
Ti-alloy anode pipe 1, neutral ion barrier film 2, connecting ear 3, cathode shell 4, upper cover plate 5, inlet mouth 6, delivery port 7, venting port 8, mistress's discharge outlet 9, electrolysis inner room 10, electrolysis mistress 11, support 12, inner core 13, retaining plate 14, web plate shape electrode 15, graphite rod electrode 16, ion dividing plate 17.
The utility model has the advantages that: compare with tetravalence company like product, in the situation that enclosure volume equates, the electrolytic efficiency height, gas production big (chlorine yield is 300 Grams Per Hours), the neutral ion barrier film is not affected by condition of water quality, dirt not easy to hang, long service life, simple in structure, simple installation.
Claims (1)
- A kind of electrolysis chlorine dioxide generating device, include Ti-alloy anode pipe 1, tubular neutral ion barrier film 2, connecting ear 3, titanium steel cathode shell 4, upper cover plate 5, inlet mouth 6, delivery port 7, venting port 8, mistress's discharge outlet 9, electrolysis inner room 10, electrolysis mistress 11, support 12 is characterized in that Ti-alloy anode pipe 1 is installed in the tubular neutral ion barrier film 2, gap between them is an electrolysis inner room 10, tubular neutral ion barrier film 2 is arranged in the titanium steel cathode shell 4, and the gap between them is electrolysis mistress 11, and inlet mouth 6 is arranged in the tubular ion diaphragm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89209620 CN2061177U (en) | 1989-10-18 | 1989-10-18 | Electrolytic chlorine dioxide generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89209620 CN2061177U (en) | 1989-10-18 | 1989-10-18 | Electrolytic chlorine dioxide generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2061177U true CN2061177U (en) | 1990-08-29 |
Family
ID=4866138
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 89209620 Withdrawn CN2061177U (en) | 1989-10-18 | 1989-10-18 | Electrolytic chlorine dioxide generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2061177U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102812160A (en) * | 2010-03-19 | 2012-12-05 | 大幸药品株式会社 | Electrolyzer |
| CN104674296A (en) * | 2015-03-16 | 2015-06-03 | 张学武 | Electrolytic chlorine dioxide generator and electrolytic cell |
| CN110325668A (en) * | 2016-12-16 | 2019-10-11 | 马里奥·皮卡 | For producing the method and electrolytic cell of detergent and disinfectant liquid |
-
1989
- 1989-10-18 CN CN 89209620 patent/CN2061177U/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102812160A (en) * | 2010-03-19 | 2012-12-05 | 大幸药品株式会社 | Electrolyzer |
| 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 |
| CN110325668A (en) * | 2016-12-16 | 2019-10-11 | 马里奥·皮卡 | For producing the method and electrolytic cell of detergent and disinfectant liquid |
| CN110325668B (en) * | 2016-12-16 | 2022-07-29 | 马里奥·皮卡 | Method and electrolytic cell for producing detergent and disinfectant liquids |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |