GB303027A - Improvements in electrochemical processes - Google Patents
Improvements in electrochemical processesInfo
- Publication number
- GB303027A GB303027A GB38100/28A GB3810028A GB303027A GB 303027 A GB303027 A GB 303027A GB 38100/28 A GB38100/28 A GB 38100/28A GB 3810028 A GB3810028 A GB 3810028A GB 303027 A GB303027 A GB 303027A
- Authority
- GB
- United Kingdom
- Prior art keywords
- steam
- oxygen
- gas
- pressure
- vapour
- 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.)
- Expired
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
-
- 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
- C25B15/00—Operating or servicing cells
Abstract
303,027. Citovich, E. Dec. 24, 1927, [Convention date]. Gas cells.-Electrolytic processes are carried out with an aqueous electrolyte at a temperature between 100‹ C. and the critical temperature. Under these conditions the processes are reversible and the products may be made to recombine with generation of electrical power. The process may be carried out in a high-pressure apparatus of the filter-press type the elements a of which are of a circular periphery. The end cells are supported rigidlv; the intermediate joints are rendered gas-tight by thermal expansion. The electrodes d are of fine copper or other gauze. Pipes c are provided for the introduction of electrolyte and reaction materials and for withdrawal of products. In an example, an alkaline solution is electrolyzed at 300‹ C. to produce hydrogen and oxygen which are collected in highpressure receivers initially filled. with steam at the cell-pressure the steam being gradually displaced. By slightly raising the temperature the steam-presure is raised so as to cause gas to reenter the electrode chambers; the reaction thereupon proceeds in the opposite direction and the apparatus functions as a galvanic battery. The anode may be in contact with carbon monoxide or other reducing gas or vapour or with an organic substance such as an oil which is oxidized bv the electrolytic action. A solid fuel in powdered form may be suspended in the anolyte and oxidized during electrolysis. A solid or liquid fuel may be heated with water and a catalyst such as a dissolved salt or copper turnings in an auxiliary high-pressure vessel to form a gaseous fuel which is then led to the anode. In another example air is led to the cathode; the oxygen is converted to water vapour and pure nitrogen remains. In the generation of oxygen an oxidizing electrode of ferric oxide or copper oxide may be employed. Precious metals, alloys, iron. nickel, oxides, sulphides, and graphite may be used as electrodes. Calcium chloride may be dissolved in the electrolyte to reduce the vapour pressure.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE303027X | 1927-12-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB303027A true GB303027A (en) | 1929-10-24 |
Family
ID=6109323
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB38100/28A Expired GB303027A (en) | 1927-12-24 | 1928-12-24 | Improvements in electrochemical processes |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB303027A (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3103473A (en) * | 1963-09-10 | Method for the electrochemical reduction of compounds | ||
US3103474A (en) * | 1963-09-10 | Electrowinning of metals from electrolytes | ||
US3215562A (en) * | 1961-12-22 | 1965-11-02 | Air Prod & Chem | Fuel cell with screen electrodes |
DE1212177B (en) * | 1956-10-05 | 1966-03-10 | Nat Res Dev | Fuel element |
DE1216261B (en) * | 1963-10-09 | 1966-05-12 | Siemens Ag | Method and device for the electrochemical production of nitrogen-hydrogen protective gases |
US3256504A (en) * | 1961-01-11 | 1966-06-14 | Fidelman Morris | Galvanic hydrogen producer |
DE1220401B (en) * | 1961-05-03 | 1966-07-07 | Demag Elektrometallurgie Gmbh | Process for the production of synthesis gas for ammonia synthesis and of ammonia |
US3342717A (en) * | 1962-09-20 | 1967-09-19 | Pullman Inc | Electrochemical cell |
US3401099A (en) * | 1966-04-27 | 1968-09-10 | Air Prod & Chem | Electrolytic method of gas separation |
US3401100A (en) * | 1964-05-26 | 1968-09-10 | Trw Inc | Electrolytic process for concentrating carbon dioxide |
US3458412A (en) * | 1966-03-30 | 1969-07-29 | Matsushita Electric Ind Co Ltd | Electrolytic process of preparing pure hydrogen |
US3481847A (en) * | 1964-09-21 | 1969-12-02 | Olin Mathieson | Electrolytic process of making chlorine |
US3489670A (en) * | 1964-07-29 | 1970-01-13 | Gen Electric | Process for gas purification |
US3996118A (en) * | 1972-05-11 | 1976-12-07 | The Mead Corporation | Method for promoting reduction-oxidation of electrolytically produced gases |
-
1928
- 1928-12-24 GB GB38100/28A patent/GB303027A/en not_active Expired
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3103473A (en) * | 1963-09-10 | Method for the electrochemical reduction of compounds | ||
US3103474A (en) * | 1963-09-10 | Electrowinning of metals from electrolytes | ||
DE1212177B (en) * | 1956-10-05 | 1966-03-10 | Nat Res Dev | Fuel element |
US3256504A (en) * | 1961-01-11 | 1966-06-14 | Fidelman Morris | Galvanic hydrogen producer |
DE1220401B (en) * | 1961-05-03 | 1966-07-07 | Demag Elektrometallurgie Gmbh | Process for the production of synthesis gas for ammonia synthesis and of ammonia |
US3215562A (en) * | 1961-12-22 | 1965-11-02 | Air Prod & Chem | Fuel cell with screen electrodes |
US3379627A (en) * | 1962-09-20 | 1968-04-23 | Pullman Inc | Process for the manufacture of oxygencontaining derivatives of olefins in an electrochemical cell |
US3342717A (en) * | 1962-09-20 | 1967-09-19 | Pullman Inc | Electrochemical cell |
US3347759A (en) * | 1963-10-09 | 1967-10-17 | Siemens Ag | Electrochemical method and apparatus for producing a protective gas mixture consisting of nitrogen and hydrogen |
DE1216261B (en) * | 1963-10-09 | 1966-05-12 | Siemens Ag | Method and device for the electrochemical production of nitrogen-hydrogen protective gases |
US3401100A (en) * | 1964-05-26 | 1968-09-10 | Trw Inc | Electrolytic process for concentrating carbon dioxide |
US3489670A (en) * | 1964-07-29 | 1970-01-13 | Gen Electric | Process for gas purification |
US3481847A (en) * | 1964-09-21 | 1969-12-02 | Olin Mathieson | Electrolytic process of making chlorine |
US3458412A (en) * | 1966-03-30 | 1969-07-29 | Matsushita Electric Ind Co Ltd | Electrolytic process of preparing pure hydrogen |
US3401099A (en) * | 1966-04-27 | 1968-09-10 | Air Prod & Chem | Electrolytic method of gas separation |
US3996118A (en) * | 1972-05-11 | 1976-12-07 | The Mead Corporation | Method for promoting reduction-oxidation of electrolytically produced gases |
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