专利摘要:
An improved anode element for monopolar filter-press electrolysis cells comprises providing said anode element with an integral hollow member positioned above the upper surface of said anode element. Preferably, said hollow member is formed as an integral extension of the electrode frame, said hollow member having an outlet for withdrawing chlorine gas and being adapted to permit continuous fluid contact with said anode element, said hollow member being further adapted to provide sufficient hydrostatic pressure in said anode element for optimal liquid flow through the diaphragm over the entire operating cycle of the electrolysis cell.
公开号:SU950191A3
申请号:SU792770402
申请日:1979-05-18
公开日:1982-08-07
发明作者:Мозе Лучиано;Шурих Хельмут;Штрассер Бернд
申请人:Хукер Кемикалз Энд Пластикс Корп.(Фирма);
IPC主号:
专利说明:

The invention relates to the construction of filter press monopolar diaphragm electrolyzers, which are widely used in the electrolysis of solutions of cooking salt, to produce hydrogen, chlorine and alkali.
A perforated box-shaped anode for filterpress monopole Q diaphragm electrolysers is known. The diaphragm separates the cathode and anode chambers and thereby prevents the mixing of gases. To ensure continuous electrolysis through the diaphragm into the cathode chamber, it is necessary to maintain a uniform flow of liquid. For this purpose, various levels of liquid in the anodic and cathodic chambers 1 are maintained in the known electrolyzer.
However, during operation, the diaphragm changes its resistance to the solution and it is necessary to maintain an overpressure. 25
The aim of the invention is to increase the efficiency of the electrolyzer by providing a uniform rate of electrolyte flow through the diaphragm.
This goal is achieved by the fact that the perforated box-shaped anode for filterpress monopolar diaphragm electrolyte jets is equipped with a camera mounted on it and communicating with it.
The presence of a chamber / mounted on the anode allows the level of the liquid in the anode chamber to be adjusted in such a way as to maintain an appropriate flow of electrolyte through the diaphragm during the entire operating time of the electrolyzer.
The chamber can be made as one unit with the anode and serve as its continuation. The gas released at the anode is removed through the chamber through an outlet line. The height of the hollow element is selected in accordance with the resistance of the applied membrane or diaphragm. A preferred option is when the Kgmer height is 300-800 mm, for the case of asbestos diaphragms.
The drawing shows a schematic diaphragm electrolyzer.
In the box perforated anodes 1 pipe 2 serves the electrolyte. Through the side perforated
the walls of the anodes 1 electrolyte flows into the cathode chambers 3. The box-shaped perforated anodes 1 are equipped with chambers 4, connected to the box-shaped anodes 1, Chambers 4 are mounted on the anodes 1. Between the anodes 1 and the cathode 5 cameras 3 a diaphragm 5 is placed. in the anodes 1 due to the chambers 4 set higher than in the cathode chambers 3.10
When using a membrane electrolyzer, the solution is transported to the cathode chamber 3 through the holes in the membranes.
In the electrolysis cell operating. | -5 thus, establish the same fluid levels in the anode and cathode chambers, i.e. chamber 4 does not contain liquid under conditions.
Thus, the use of predn of anode design for filter presses electrolyzers allows
to conduct electrolysis more efficiently due to a more uniform flow of electrolyte through the diaphragm during the electrolysis process.
权利要求:
Claims (1)
[1]
1. Yakimenko L.M., Moddalevska I.D. Tkkhek Z.A. Electrolysis of water, M., Himi, 1970, p.95 (prototype).
类似技术:
公开号 | 公开日 | 专利标题
US4069129A|1978-01-17|Electrolytic cell
FR2433060A1|1980-03-07|
KR20010075597A|2001-08-09|High pressure electrolyser module
JPH0293088A|1990-04-03|Method and device for water electrolysis
US4108742A|1978-08-22|Electrolysis
CA1190511A|1985-07-16|Method of operating a liquid-gas electrochemical cell
EP1528126A1|2005-05-04|An integrated electrolyser module with an internal gas/liquid separator
SU950191A3|1982-08-07|Perforated box-shapled anode
WO2007046730A2|2007-04-26|Water electrochemical processing device
JPS5743992A|1982-03-12|Electrolyzing method for alkali chloride
RU2005131463A|2007-04-20|METHOD FOR PRODUCING CHLORINE AND CHLORINE-CONTAINING OXIDIZERS AND INSTALLATION FOR ITS IMPLEMENTATION
SU1286109A3|1987-01-23|Monopolar electrolyzer
US4036717A|1977-07-19|Method for concentration and purification of a cell liquor in an electrolytic cell
CA1117473A|1982-02-02|Electrolytic cell
US4568433A|1986-02-04|Electrolytic process of an aqueous alkali metal halide solution
RU51613U1|2006-02-27|DEVICE FOR ELECTROCHEMICAL TREATMENT OF WATER OR AQUEOUS SOLUTIONS
KR840008389A|1984-12-14|Electrolyzer |
RU2126461C1|1999-02-20|Method of chlorine-caustic electrolysis and diaphragm cell
US4981563A|1991-01-01|Electrolysis cell and method of producing chlorine
SU439307A1|1974-08-15|Electrolyzer
US2340254A|1944-01-25|Method of electrolysis
JPS57194273A|1982-11-29|Production of hydrogen
US4273630A|1981-06-16|Process for the start-up of membrane cells for the electrolysis of aqueous salt solutions
US4085015A|1978-04-18|Electrolysis cell liquor emission control process
US4290863A|1981-09-22|Process for electrolysis of brine by mercury cathodes
同族专利:
公开号 | 公开日
NO791628L|1979-11-20|
BR7903119A|1979-12-11|
JPS54152676A|1979-12-01|
DE2821978A1|1979-11-22|
CA1134780A|1982-11-02|
US4263119A|1981-04-21|
SE7904378L|1979-11-20|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

US1963959A|1933-01-23|1934-06-26|Howard E Dorsey|Electrolytic gas producing device|
BE502876A|1950-05-08|
BE791675A|1971-12-06|1973-05-21|Solvay|IMPROVEMENTS TO HOLLOW METAL ANODES FOR ELECTROLYSIS CELLS WITH VERTICAL ELECTRODES, AND CELL EQUIPPED WITH ANODES OF THIS TYPE|
JPS5235030B2|1973-04-19|1977-09-07|
US4118306A|1976-02-02|1978-10-03|Diamond Shamrock Technologies S. A.|Anode constructions for electrolysis cells|
US4177116A|1977-06-30|1979-12-04|Oronzio DeNora Implanti Elettrochimici S.p.A.|Electrolytic cell with membrane and method of operation|JPS5678875U|1979-11-14|1981-06-26|
US4767511A|1987-03-18|1988-08-30|Aragon Pedro J|Chlorination and pH control system|
US4875988A|1988-08-05|1989-10-24|Aragon Pedro J|Electrolytic cell|
US5348664A|1992-10-28|1994-09-20|Stranco, Inc.|Process for disinfecting water by controlling oxidation/reduction potential|
US5427658A|1993-10-21|1995-06-27|Electrosci Incorporated|Electrolytic cell and method for producing a mixed oxidant gas|
US7390399B2|2004-12-21|2008-06-24|Siemens Water Technologies Holding Corp.|Water treatment control systems and methods of use|
US20060169646A1|2005-02-03|2006-08-03|Usfilter Corporation|Method and system for treating water|
US7905245B2|2005-09-30|2011-03-15|Siemens Water Technologies Corp.|Dosing control system and method|
DE102011010558A1|2011-02-07|2012-08-09|Thyssenkrupp Uhde Gmbh|Composite material|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE19782821978|DE2821978A1|1978-05-19|1978-05-19|ANODE ELEMENT FOR MONOPOLAR ELECTROLYSIS CELLS ARRANGED IN THE LIKE OF A FILTER PRESS|
[返回顶部]