US5079105A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Device for conversion of chemical energy from hydrocarbons into electric energy by an electrochemical high-temperature process
Assignee: ABB Asea Brown Boveri Ltd
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Filing: 1990-05-17
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Granted: 1992-01-07
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Expires: 2010-05-17
Abstract
Abstract Device for the conversion of chemical energy of hydrocarbons into electric energy by plate-shaped high-temperature fuel cells, arranged like a stack around a central reaction space, on the basis of zirconium oxide as solid electrolyte, wherein gas jet pumps are provided for the transport and mixing of a part of the O 2 excess and ballast gas with the gaseous oxygen carrier, as well as for the transport and mixing of a part of the fuel excess and the reaction products with the gaseous fuel, and a central perforated feed pipe and a perforated body with catalyst coating are provided such that endothermic conversion reactions are performed within the central reaction space.
Inventors
- 👤 Ulf Bossel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 21:26
CPC Classifications
H; H01; H01M; H01M8/00; H01M8/06; H01M8/0606; H01M8/0612; H01M8/0625; H01M8/24; H01M8/241; H01M8/2425; H01M8/2432; H01M8/2465; H01M8/247; H01M8/249; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/50
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
169 words
Device for the conversion of chemical energy of hydrocarbons into electric energy by an electrochemical high-temperature process, on the basis of zirconium oxide as a solid electrolyte, said device comprising: a plurality of flat ceramic fuel cells arranged in a plurality of stacks around a central reaction space, wherein the endothermic conversion reactions: CH.sub.4 +CO.sub.2 →2CO+2H.sub.2 and CH.sub.4 +H.sub.2 O→CO+3H.sub.2 are performed; each of said fuel cells being acted on one side by a gaseous oxygen carrier and being acted on the other side by a gaseous fuel; at least one gas jet pump per each individual stack of fuel cells for transporting and mixing a part of an O 2 excess and ballast gas with the gaseous oxygen carrier; a central gas jet pump for transporting and mixing a part of a fuel excess and gaseous reaction products CO 2 and H 2 O with the gaseous fuel; and a central perforated feed pipe for the gaseous fuel, said central perforated feed pipe extending into said reaction space.
Claim 2
Dependent Claim
169 words
Device for the conversion of chemical energy of hydrocarbons into electric energy by an electrochemical high-temperature process, on the basis of zirconium oxide as a solid electrolyte, said device comprising: a plurality of flat ceramic fuel cells arranged in a plurality of stacks around a central reaction space, wherein the endothermic conversion reactions: CH.sub.4 +CO.sub.2 →2CO+2H.sub.2 and CH.sub.4 +H.sub.2 O→CO+3H.sub.2 are performed; each of said fuel cells being acted on one side by a gaseous oxygen carrier and being acted on the other side by a gaseous fuel; at least one gas jet pump per each individual stack of fuel cells for transporting and mixing a part of an O 2 excess and ballast gas with the gaseous oxygen carrier; a central gas jet pump for transporting and mixing a part of a fuel excess and gaseous reaction products CO 2 and H 2 O with the gaseous fuel; and a central perforated feed pipe for the gaseous fuel, said central perforated feed pipe extending into said reaction space.
Claim 3
Dependent Claim
67 words
Device according to claim 1, wherein four individual stacks of said fuel cells are positioned in a heat-insulated container symmetrically around said central reaction space with said central perforated feed pipe for the gaseous fuel; and wherein an intermediate space between said fee pipe and said individual stacks is filled with a perforated hollow cylindrical body, whose surface is coated with a catalyst accelerating the conversion reactions.
Claim 4
Dependent Claim
53 words
Device according to claim 2, wherein at least one feed pipe for feeding the gaseous oxygen carrier is positioned in a sector between two adjacent individual stacks, and wherein at least one discharge pipe for the removal of the O 2 excess and the ballast gas is positioned adjacent to said feed pipe.
Claim 5
Dependent Claim
58 words
Device according to claim 3, wherein a strip-shaped ceramic body having a T-shaped angular profile is located between two adjacent individual stacks, said strip-shaped ceramic body comprising recesses in which said feed pipe and said discharge pipe are respectively positioned, wherein an active part of said device comprising several individual stacks is held together by said ceramic bodies.
Claim 6
Dependent Claim
32 words
Device according to claim 4, wherein a longitudinal axis of said ceramic body and axes of said feed pipe and said discharge pipe are perpendicular to a horizontal plane of said device.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1995-01-06 | 1995-07-08 | 1996-01-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-01-06 | 1999-07-08 | 2000-01-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-01-06 | 2003-07-08 | 2004-01-07 | $7700.00 | Window Closed / Lapsed |