GB303027A - Improvements in electrochemical processes - Google Patents

Improvements in electrochemical processes

Info

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
Application number
GB38100/28A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB303027A publication Critical patent/GB303027A/en
Expired legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00Operating 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.
GB38100/28A 1927-12-24 1928-12-24 Improvements in electrochemical processes Expired GB303027A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (16)

* Cited by examiner, † Cited by third party
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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