(19) |
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(11) |
EP 0 328 818 A3 |
(12) |
EUROPEAN PATENT APPLICATION |
(88) |
Date of publication A3: |
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06.12.1989 Bulletin 1989/49 |
(43) |
Date of publication A2: |
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23.08.1989 Bulletin 1989/34 |
(22) |
Date of filing: 01.12.1988 |
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(51) |
International Patent Classification (IPC)4: C25B 1/26 |
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(84) |
Designated Contracting States: |
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AT DE ES FR GB IT SE |
(30) |
Priority: |
16.02.1988 CA 558945
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(71) |
Applicant: Sterling Canada, Inc. |
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Houston, Texas 77002-4312 (US) |
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(72) |
Inventors: |
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- Lipsztajn, Marek
Rexdale
Ontario M9V 4K2 (CA)
- McGilvery, James Duncan
Etobicoke
Ontario M9C 1P7 (CA)
- Twardowski, Zbigniew
Mississauga
Ontario L4W 3W7 (CA)
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(74) |
Representative: W.P. THOMPSON & CO. |
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Eastcheap House
Central Approach Letchworth,
Hertfordshire SG6 3DS Letchworth,
Hertfordshire SG6 3DS (GB) |
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(54) |
Production of chlorine dioxide in an electrolytic cell |
(57) Chlorine dioxide is produced electrolytically in the cathode compartment of an electrolytic
cell using a three-dimensional high surface-area cathode. The cathode compartment
is separated from an anode compartment by a cation-exchange membrane. Sodium chlorate
is reacted with hydrogen ions and chloride ions in the cathode compartment and chlorine
dioxide is vented from the cathode compartments. Chlorine co-produced with the chlorine
dioxide is reduced at the cathode to provide chloride ions for the reaction while
electrolytically-produced hydrogen ions are transferred across the membrane from the
anode compartment to the cathode compartment to provide hydrogen ions for the reaction.