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US4412895A Expired / Lapsed US ⏱️ 0.0 years remaining

System using SO2 as an anode depolarizer in a solid oxide electrolyte electrolysis cell for H2 production from steam

Assignee: Westinghouse Electric Corp
•
Filing: 1981-09-29
•
Granted: 1983-11-01
•
Expires: 2001-09-29
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Abstract

Abstract Hydrogen gas is produced from water vapor by: (1) supplying water vapor to the cathode and SO 2 to the anode of an electrolysis cell utilizing a solid oxide electrolyte which has a high oxygen ion conduction but which is impervious to H 2 and SO 2 , between the cathode and anode, to provide H 2 and a mixture of SO 2 and SO 3 , (2) passing the SO 3 into a reduction reactor operating at a temperature effective to decompose it and provide a mixture of SO 2 and O 2 , and (3) passing the SO 2 back to the anode of the electrolysis cell.

Inventors

  • 👤 Wen-Tong P. Lu

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 00:18
CPC Classifications
C; C25; C25B; C25B1/00; C25B1/01; C25B1/02

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 148 words
A method of decomposing water vapor into hydrogen and oxygen comprising the steps of: (1) supplying SO 2 gas to the anode and water vapor to the cathode of an electrolysis cell utilizing a solid oxide electrolyte between the anode and cathode of the cell, said solid oxide electrolyte having a high oxygen ion conduction, said cell operating at a temperature of between 350° C. and 1,000° C., to provide H 2 gas, and a gas mixture consisting of SO 2 gas and SO 3 gas; (2) collecting the H 2 gas; (3) passing SO 3 into a reduction reactor operating at a temperature effective to catalytically decompose the SO 3 and provide a mixture of SO 2 gas and O 2 gas; (4) collecting the O 2 gas from step (3); and (5) passing SO 2 gas to the anode of the solid oxide electrolyte electrolysis cell.
Claim 2
Independent Claim 148 words
A method of decomposing water vapor into hydrogen and oxygen comprising the steps of: (1) supplying SO 2 gas to the anode and water vapor to the cathode of an electrolysis cell utilizing a solid oxide electrolyte between the anode and cathode of the cell, said solid oxide electrolyte having a high oxygen ion conduction, said cell operating at a temperature of between 350° C. and 1,000° C., to provide H 2 gas, and a gas mixture consisting of SO 2 gas and SO 3 gas; (2) collecting the H 2 gas; (3) passing SO 3 into a reduction reactor operating at a temperature effective to catalytically decompose the SO 3 and provide a mixture of SO 2 gas and O 2 gas; (4) collecting the O 2 gas from step (3); and (5) passing SO 2 gas to the anode of the solid oxide electrolyte electrolysis cell.
Claim 3
Dependent Claim 49 words
The method of claim 1, where the solid oxide electrolyte is impervious to H 2 gas and SO 2 gas, and where SO 2 gas is separated from SO 3 gas in a gas separation means before the SO 3 is passed into the reduction reactor in step (3).
Claim 4
Dependent Claim 29 words
The method of claim 1, where the reduction reactor operates at a temperature of between about 800° C. and about 900° C., to catalytically decompose the SO 3 .
Claim 5
Dependent Claim 48 words
The method of claim 1, where, in step (4) the oxygen gas is separated from the SO 2 gas by condensing the SO 2 into a liquid, after which the liquid SO 2 is vaporized before being passed to the anode of the electrolysis cell in step (5).
Claim 6
Dependent Claim 22 words
The method of claim 1, where thermal energy for the reduction reactor is supplied, at least in part, by a nuclear reactor.
Claim 7
Dependent Claim 52 words
The method of claim 1, where the water vapor at the cathode of the cell reacts with oxygen vacancies in the lattice of the solid oxide electrolyte to produce hydrogen gas, and oxygen ions which pass across the solid electrolyte to electrochemically oxidize SO 2 gas at the anode of the cell.
Claim 8
Dependent Claim 27 words
The method of claim 1, where the solid oxide electrolyte is selected from the group consisting of stabilized zirconia, stabilized ceria, stabilized thoria and stabilized bismuth oxide.
Claim 9
Dependent Claim 15 words
The method of claim 1, where the solid oxide electrolyte is zirconia stabilized with yttria.

References Cited (Backward Citations)

US3616334A Cited
US3630879A Cited
US3888750A Cited
US3993653A Cited
US4024036A Cited
US4059496A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-10-31 1987-05-02 1987-11-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-10-31 1991-05-02 1991-11-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-10-31 1995-05-02 1995-11-01 $7700.00 Window Closed / Lapsed

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