GB1487284A

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

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