GB1487284A – Electrolysis
– Google Patents
GB1487284A – Electrolysis
– Google Patents
Electrolysis
Info
Publication number
GB1487284A
GB1487284A
GB9388/75A
GB938875A
GB1487284A
GB 1487284 A
GB1487284 A
GB 1487284A
GB 9388/75 A
GB9388/75 A
GB 9388/75A
GB 938875 A
GB938875 A
GB 938875A
GB 1487284 A
GB1487284 A
GB 1487284A
Authority
GB
United Kingdom
Prior art keywords
anode
cathode
plate
gas
chamber
Prior art date
1974-03-09
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.)
Expired
Application number
GB9388/75A
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.)
Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
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.)
1974-03-09
Filing date
1975-03-06
Publication date
1977-09-28
1974-03-09
Priority claimed from JP49026775A
external-priority
patent/JPS50120493A/ja
1974-12-10
Priority claimed from JP14174574A
external-priority
patent/JPS5168477A/en
1975-03-06
Application filed by Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK
filed
Critical
Asahi Chemical Industry Co Ltd
1977-09-28
Publication of GB1487284A
publication
Critical
patent/GB1487284A/en
Status
Expired
legal-status
Critical
Current
Links
Espacenet
Global Dossier
Discuss
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
C25B1/00—Electrolytic production of inorganic compounds or non-metals
C25B1/01—Products
C25B1/34—Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis
C25B1/46—Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis in diaphragm cells
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
C25B1/00—Electrolytic production of inorganic compounds or non-metals
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
C25B3/00—Electrolytic production of organic compounds
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
C25B9/77—Assemblies comprising two or more cells of the filter-press type having diaphragms
Abstract
1487284 Electrolysis in diaphragm cells ASAHI KASEI KOGYO KK 6 March 1975 [9 March 1974 30 Sept 1974 10 Dec 1974] 9388/75 Heading C7B In a process for electrolysis of an aqueous electrolyte solution, e.g. for producing NaOH, Cl 2 and H 2 from saline water, LiOH, KOH, I 2 , Br2, HClO 3 , HBrO 3 , H 2 S 2 O 8 , or adiponitrile from acrylonitrile, in a diaphragm cell having a cation exchange membrane 1 to partition the cell into a cathode and an anode chamber, in which gas is generated at least at the anode 2, the internal pressure in the cathode is kept higher (e.g. 0À2 to 5m water column) than that in the anode chamber to press the membrane towards the anode, e.g. by discharging the gas generated at the anode, (such as Cl 2 ) backwardly of the anode; with gases generated being discharged backwardly of the respective electrodes the cathode chamber is larger in volume than the anode chamber. Preferably gas permeable metallic plates are used as anode and cathode, e.g. expanded, multi-rod, perforated sheet or mesh of noble metal (e.g. Ru with or without Ti) oxide coated Ti for the anode and Ni (alloy or thiocyanate) plated Fe for the cathode. As shown (Fig. 1) the anode 2 may be carried by supports 71 on a partition wall 72 (of explosion-bonded Ti and Fe plates), between the gas-ascending space and downcomer 113, spaced from the partition 111 by distance piece 73 and connected by conductor rod 112. Mineral acid, e.g. HCl, H 2 SO 4 or HNO 3 , may be added to the anolyte to maintain the pH at or below 3À5. Bipolar electrodes may be used Fig. 4 (not shown): anode 2, a Ti plate coated with (mole per cent) 55 RuO 2 -40, TiO 2 -5ZrO 2 , joined to cathode 3, an expanded Fe plate, via Ti and Fe ribs 7, 9 and a partition wall 4 formed by explosion-bonding Ti plate 5 onto Fe plate 6. NaCl and NaOH solutions are charged into anode and cathode chambers 8, 10 via nozzles 13, 15, and Cl 2 and H 2 gases are discharged via nozzles 14, 16. The anolytes and catholytes may be recycled. The cation exchange membrane may be a polymer of perfluorosulphonic acid compound, sulphonated styrene-divinyl benzene, acrylic acid-divinyl benzene, or a phosphoric acid type membrane.
GB9388/75A
1974-03-09
1975-03-06
Electrolysis
Expired
GB1487284A
(en)
Applications Claiming Priority (3)
Application Number
Priority Date
Filing Date
Title
JP49026775A
JPS50120493A
(en)
1974-03-09
1974-03-09
JP11255674
1974-09-30
JP14174574A
JPS5168477A
(en)
1974-12-10
1974-12-10
Kairyosareta denkaihoho
Publications (1)
Publication Number
Publication Date
GB1487284A
true
GB1487284A
(en)
1977-09-28
Family
ID=27285534
Family Applications (1)
Application Number
Title
Priority Date
Filing Date
GB9388/75A
Expired
GB1487284A
(en)
1974-03-09
1975-03-06
Electrolysis
Country Status (8)
Country
Link
BR
(1)
BR7501374A
(en)
CA
(1)
CA1088456A
(en)
DE
(1)
DE2510396B2
(en)
FR
(1)
FR2263034B1
(en)
GB
(1)
GB1487284A
(en)
IT
(1)
IT1034107B
(en)
NL
(1)
NL169618C
(en)
SE
(1)
SE432447B
(en)
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US4822460A
(en)
*
1984-11-05
1989-04-18
The Dow Chemical Company
Electrolytic cell and method of operation
Families Citing this family (8)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
DE2658189C2
(en)
*
1976-12-22
1979-02-15
Metallgesellschaft Ag, 6000 Frankfurt
Process for the electrochemical production of olefin oxide
USRE30864E
(en)
1977-06-27
1982-02-09
Olin Corporation
Process for electrolysis in a membrane cell employing pressure actuated uniform spacing
US4142950A
(en)
*
1977-11-10
1979-03-06
Basf Wyandotte Corporation
Apparatus and process for electrolysis using a cation-permselective membrane and turbulence inducing means
IT1118243B
(en)
*
1978-07-27
1986-02-24
Elche Ltd
MONOPOLAR ELECTROLYSIS CELL
DE2914870A1
(en)
*
1979-04-12
1980-10-30
Hoechst Ag
METHOD FOR CHLORINE AND COOLING THE ANOLYTE OF ALKALI HALOGENIDE ELECTROLYSIS
US4265719A
(en)
*
1980-03-26
1981-05-05
The Dow Chemical Company
Electrolysis of aqueous solutions of alkali-metal halides employing a flexible polymeric hydraulically-impermeable membrane disposed against a roughened surface cathode
DK501485A
(en)
*
1984-11-05
1986-05-06
Dow Chemical Co
ELECTROLYTE CELL AND METHOD OF OPERATING THE SAME
GB9224372D0
(en)
*
1992-11-20
1993-01-13
Ici Plc
Electrolytic cell and electrode therefor
Family Cites Families (3)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
GB1196631A
(en)
*
1966-05-31
1970-07-01
Monsanto Co
Electrolytic Diaphragm Cell
US3496077A
(en)
*
1967-12-18
1970-02-17
Hal B H Cooper
Electrolyzing of salt solutions
BE790369A
(en)
*
1971-10-21
1973-04-20
Diamond Shamrock Corp
METHOD AND APPARATUS FOR THE PREPARATION OF HYDROXIDES FROM HIGH PURE ALKALINE METALS IN AN ELECTROLYTIC TANK.
1975
1975-03-06
SE
SE7502502A
patent/SE432447B/en
not_active
IP Right Cessation
1975-03-06
GB
GB9388/75A
patent/GB1487284A/en
not_active
Expired
1975-03-07
NL
NLAANVRAGE7502738,A
patent/NL169618C/en
not_active
IP Right Cessation
1975-03-07
CA
CA221,570A
patent/CA1088456A/en
not_active
Expired
1975-03-07
IT
IT21049/75A
patent/IT1034107B/en
active
1975-03-07
FR
FR7507198A
patent/FR2263034B1/fr
not_active
Expired
1975-03-07
BR
BR1374/75A
patent/BR7501374A/en
unknown
1975-03-10
DE
DE2510396A
patent/DE2510396B2/en
active
Granted
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US4822460A
(en)
*
1984-11-05
1989-04-18
The Dow Chemical Company
Electrolytic cell and method of operation
Also Published As
Publication number
Publication date
NL169618B
(en)
1982-03-01
SE432447B
(en)
1984-04-02
CA1088456A
(en)
1980-10-28
FR2263034A1
(en)
1975-10-03
DE2510396A1
(en)
1975-09-11
DE2510396B2
(en)
1980-04-17
DE2510396C3
(en)
1987-01-22
NL7502738A
(en)
1975-09-11
FR2263034B1
(en)
1978-03-17
SE7502502L
(en)
1975-09-10
IT1034107B
(en)
1979-09-10
BR7501374A
(en)
1976-11-30
NL169618C
(en)
1982-08-02
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Legal Events
Date
Code
Title
Description
1978-02-08
PS
Patent sealed
1995-04-05
PE20
Patent expired after termination of 20 years
Effective date:
19950305