EP0071740A1 - Cellule électrolytique monopolaire du type filtre-presse - Google Patents
Cellule électrolytique monopolaire du type filtre-presse Download PDFInfo
- Publication number
- EP0071740A1 EP0071740A1 EP82105699A EP82105699A EP0071740A1 EP 0071740 A1 EP0071740 A1 EP 0071740A1 EP 82105699 A EP82105699 A EP 82105699A EP 82105699 A EP82105699 A EP 82105699A EP 0071740 A1 EP0071740 A1 EP 0071740A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- anode
- plates
- seals
- cathode plates
- active part
- 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.)
- Withdrawn
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
Definitions
- the invention relates to a monopolar electrolytic filter press cell which is suitable for the electrolysis of an aqueous, halide-containing electrolyte (brine) in order to produce an aqueous alkali metal hydroxide solution (cell liquid) and halogen and hydrogen.
- the cell consists of the two end pressure plates with tension anchors, a large number of alternately arranged anolyte and catholyte chambers, the electrolyte chambers, each made up of two anode and cathode plates, each separated by a flat ion-permeable element, the membrane.
- an electrolytic membrane cell which, in the manner of the filter press cells, consists of a large number of anode and cathode plates lined up with intermediate membranes and spacer plates.
- the anode and cathode plates according to the invention also have a non-conductive part which is provided with passages for the formation of channels for the supply and discharge of the process media.
- the process media flow from the channels into the electrolyte chambers or from the electrolyte chambers into the channels via specially corrugated passages.
- the thickness of the spacer plates between each membrane and anode plate or cathode plate defines the intended distance between two membranes.
- the membrane cell described is characterized by a large number of different components with a large number of sealing points.
- the invention has for its object to reduce the variety of different elements and thus the variety of sealing points.
- the advantages achieved by the invention are, in particular, that the number of components is significantly reduced, so that the number of sealing points also and that the cell can be easily manufactured and assembled.
- Anode plate 1 and cathode plate 2 are metal plates made of different materials and have an openwork, finely divided, ie . H. for liquid and gas permeable structure.
- the non-active part 6 is not broken, but dense, except for the at least four passages 7, 8, 9 and 10 for the process media brine, cell liquid, halogen and hydrogen.
- the electrolytically inactive part of the plates still has the current conducting part 1 for the connection of the current-carrying elements.
- the membrane 3 between the plates 1 and 2 prevents electrical contact between the two plates and creates the reaction spaces for the brine and the cell fluid.
- the material of the membrane 3 is any suitable cation exchange material with appropriate storage or coating.
- the seals 4 are usually made of an elastomeric material, such as. B. natural or synthetic rubber.
- the seal 4 receives four passages 14, 15, 16 and 17 with transverse bores 18, 19 to the corresponding reaction spaces in a known manner.
- the electrolysis cell is assembled in a known manner with the aid of end plates and tie rods, the end plates themselves being able to be inactive or already as an anode or cathode Act.
- the alternating series of a plurality of two anode plates, which form the anolyte chambers 12, the membrane and the two cathode plates, which form the catholyte chambers 13, form the monopolar electrolytic filter press cell.
- the passages in the plates in combination with the seals between the plates and around the inner edges of the plates, form the individual channels for the process media.
- the passages 7 in the lower part of the plates form the channel 20 for the supply of the brine into the cell and, via the transverse bore 18, the transmission into the anolyte chamber 12.
- Cell liquid is formed via the channel 21, which is formed by the passages 8 with the corresponding seals and is connected to the catholyte chambers via the transverse bore 19.
- halogen is discharged together with used brine and hydrogen with alkali metal hydroxide.
- the seals 4 around the chambers and channels are such that, on the one hand, they act absolutely tight against the other cell part and, on the other hand, do not create any electrical contact between the anode and cathode plates.
- the inventive design of plates, membranes and seals consequently create the electrolyte chambers and the channels with the necessary open connections to one another.
- the non-active part 6 of the anode and cathode plates can be bent plane-parallel and offset from the active part 5. This ensures that the seal 4, e.g. as double U-shaped, approximately the same thickness sealing lips or webs.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813130742 DE3130742A1 (de) | 1981-08-04 | 1981-08-04 | Monopolare elektrolytische filterpressenzelle |
DE3130742 | 1981-08-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0071740A1 true EP0071740A1 (fr) | 1983-02-16 |
Family
ID=6138506
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP82105699A Withdrawn EP0071740A1 (fr) | 1981-08-04 | 1982-06-28 | Cellule électrolytique monopolaire du type filtre-presse |
Country Status (6)
Country | Link |
---|---|
US (1) | US4432858A (fr) |
EP (1) | EP0071740A1 (fr) |
JP (1) | JPS5830307A (fr) |
AR (1) | AR231845A1 (fr) |
BR (1) | BR8204561A (fr) |
DE (1) | DE3130742A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0145259B1 (fr) * | 1983-11-14 | 1988-10-19 | Imperial Chemical Industries Plc | Procédé pour l'électrolyse d'une solution aqueuse d'un chlorure de métal alcalin |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8308187D0 (en) * | 1983-03-24 | 1983-05-05 | Ici Plc | Electrolytic cell |
US5104532A (en) * | 1989-09-15 | 1992-04-14 | Exxon Research And Engineering Company | Flat stack permeator |
US5064514A (en) * | 1990-03-30 | 1991-11-12 | Olin Corporation | Apparatus for the production of chloric acid |
DE4206843C2 (de) * | 1992-03-04 | 1994-03-24 | Heraeus Elektrochemie | Elektrochemische Zellen zur Durchführung elektrochemischer Prozesse |
US5316644A (en) * | 1992-06-19 | 1994-05-31 | United Technologies Corporation | High pressure electrochemical cell structure |
DE19544585C1 (de) * | 1995-11-30 | 1997-06-26 | Dornier Gmbh | Elektrolyseur mit flüssigem Elektrolyten |
EP1077499A3 (fr) * | 1999-08-17 | 2005-10-05 | Schmidlin Labor + Service AG | Electrolyse ou pile à combustible, électrode d'électrolyse ou de pile à combustible et procédé d'electrolyse ou de pile à combustible |
US20030089619A1 (en) * | 2000-02-22 | 2003-05-15 | Sunil Jayasekera | Process and apparatus for recovery of cyanide and metals |
CN101832963B (zh) * | 2009-10-19 | 2012-11-21 | 江阴市生一氯碱设备制造有限公司 | 电位试验电解槽的制备方法 |
RU2447930C1 (ru) * | 2010-10-27 | 2012-04-20 | Государственное образовательное учреждение высшего профессионального образования "Тамбовский государственный технический университет" (ГОУ ВПО ТГТУ) | Электробаромембранный аппарат плоскокамерного типа |
CN102618881A (zh) * | 2011-01-31 | 2012-08-01 | 张敦杰 | 电解槽 |
RU2622659C1 (ru) * | 2016-05-04 | 2017-06-19 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Тамбовский государственный технический университет" ФГБОУ ВО ТГТУ | Электробаромембранный аппарат плоскокамерного типа |
JP1603130S (fr) * | 2017-07-04 | 2018-05-07 | ||
RU2668866C1 (ru) * | 2017-10-16 | 2018-10-03 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Тамбовский государственный технический университет" (ФГБОУ ВО "ТГТУ") | Электробаромембранный аппарат плоскокамерного типа с охлаждением разделяемого раствора |
CN109704442B (zh) * | 2017-10-26 | 2021-07-16 | 中国科学院大连化学物理研究所 | 一种用于海水酸化装置的电极板结构 |
EP3699323A1 (fr) * | 2019-02-20 | 2020-08-26 | Hymeth ApS | Système d'électrodes |
USD925482S1 (en) * | 2019-04-03 | 2021-07-20 | Constantine E. Kafantaris | Home electrolyzer |
RU2718402C1 (ru) * | 2019-10-29 | 2020-04-02 | Федеральное государственное бюджетное образовательное учреждение высшего образования «Тамбовский государственный технический университет» (ФГБОУ ВО «ТГТУ») | Электробаромембранный аппарат плоскокамерного типа |
RU2744408C1 (ru) * | 2020-07-07 | 2021-03-09 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Тамбовский государственный технический университет"(ФГБОУ ВО "ТГТУ) | Электробаромембранный аппарат плоскокамерного типа |
KR102274879B1 (ko) * | 2020-08-19 | 2021-07-08 | (주)테크윈 | 전기분해조용 전극구조체 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2809332A1 (de) * | 1977-03-04 | 1978-10-12 | Ici Ltd | Elektrolytische membranzelle |
DE3028171A1 (de) * | 1979-07-31 | 1981-03-26 | Asahi Kasei Kogyo K.K., Osaka | Elektrolyse-zelle vom filterpressentyp |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3657099A (en) * | 1969-05-07 | 1972-04-18 | Asahi Chemical Ind | Electrolytic cell for producing adiponitrile by electrolytic hydrodimerization of acrylonitrile |
US4339324A (en) * | 1980-12-03 | 1982-07-13 | Henes Products Corp. | Polycell gas generator |
-
1981
- 1981-08-04 DE DE19813130742 patent/DE3130742A1/de not_active Withdrawn
-
1982
- 1982-06-28 EP EP82105699A patent/EP0071740A1/fr not_active Withdrawn
- 1982-07-27 US US06/402,312 patent/US4432858A/en not_active Expired - Fee Related
- 1982-08-03 BR BR8204561A patent/BR8204561A/pt unknown
- 1982-08-03 AR AR290195A patent/AR231845A1/es active
- 1982-08-04 JP JP57135282A patent/JPS5830307A/ja active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2809332A1 (de) * | 1977-03-04 | 1978-10-12 | Ici Ltd | Elektrolytische membranzelle |
DE3028171A1 (de) * | 1979-07-31 | 1981-03-26 | Asahi Kasei Kogyo K.K., Osaka | Elektrolyse-zelle vom filterpressentyp |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0145259B1 (fr) * | 1983-11-14 | 1988-10-19 | Imperial Chemical Industries Plc | Procédé pour l'électrolyse d'une solution aqueuse d'un chlorure de métal alcalin |
Also Published As
Publication number | Publication date |
---|---|
JPS5830307A (ja) | 1983-02-22 |
AR231845A1 (es) | 1985-03-29 |
BR8204561A (pt) | 1983-07-26 |
US4432858A (en) | 1984-02-21 |
DE3130742A1 (de) | 1983-02-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB IT LI NL SE |
|
17P | Request for examination filed |
Effective date: 19830622 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: UHDE GMBH |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
|
18W | Application withdrawn |
Withdrawal date: 19850406 |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: SCHURIG, HELMUTH, DIPL.-ING. Inventor name: STRASSER, BERND, DR. DIPL.-ING. Inventor name: SCHMITT, HELMUT, ING. GRAD. |