EP0071740A1 - Cellule électrolytique monopolaire du type filtre-presse - Google Patents

Cellule électrolytique monopolaire du type filtre-presse Download PDF

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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Withdrawn
Application number
EP82105699A
Other languages
German (de)
English (en)
Inventor
Helmut Ing. Grad. Schmitt
Bernd Dr. Dipl.-Ing. Strasser
Helmuth Dipl.-Ing. Schurig
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ThyssenKrupp Industrial Solutions AG
Original Assignee
Uhde GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Uhde GmbH filed Critical Uhde GmbH
Publication of EP0071740A1 publication Critical patent/EP0071740A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70Assemblies comprising two or more cells
    • C25B9/73Assemblies 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)
EP82105699A 1981-08-04 1982-06-28 Cellule électrolytique monopolaire du type filtre-presse Withdrawn EP0071740A1 (fr)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (2)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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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PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

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Effective date: 19830622

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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.