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US4816353A Expired / Lapsed US ⏱️ 0.0 years remaining

Integrated fuel cell and fuel conversion apparatus

Assignee: UTC Power Corp
•
Filing: 1986-05-14
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Granted: 1989-03-28
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Expires: 2006-05-14
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Abstract

Abstract An apparatus for making hydrogen from a hydrocarbon feedstock and steam using heat stored in a vessel followed by the regeneration of the vessel to restore the heat. Regeneration is done by preheating within the vessel a hydrogen purge gas and steam. Downstream of the conventional reform catalyst, the preheated gases are mixed with an oxygen containing gas so that they combust within the vessel in a fuel lean mode and heat material disposed in the vessel. This is the heat which is used in converting the hydrogen feedstock to hydrogen. The addition of steam in the regeneration process to recover the heat remaining in the vessel following the hydrogen make cycle simplifies reactor bed design and improves operational flexibility. Incorporation of a regeneratable sulfur absorber in the vessel facilitates the removal of up to 90% of the feedstock sulfur.

Inventors

  • 👤 Ronald J. Wertheim
  • 👤 Richard A. Sederquist

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 08:57
CPC Classifications
H; H01; H01M; H01M8/00; H01M8/06; H01M8/0662; C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B3/50; C01B3/56; H01M8/0606; H01M8/0612; C01B2203/00; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0465; C01B2203/0485; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/50; Y02P; Y02P70/00; Y02P70/50

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 266 words
A fuel cell system comprising: (a) a fuel cell including a fuel electrode, an oxygen electrode, and an electrolyte disposed therebetween; (b) a pair of reaction vessels, each being adapted to alternately make a hydrogen containing gas and to be regenerated, each of said reaction vessels having an upstream end and a downstream end, each vessel having disposed therein, in sequence from its upstream to downstream end, a first volume of inert packing material containing no reform catalyst, a second volume of material including a first region comprising a regenerable sulfur absorber of oxides of zinc, oxides of iron, zinc ferrite, oxides of chromium, oxides, of copper, oxides of vanadium, oxides of tungsten or mixtures thereof and a second region downstream of said first region comprising reform catalyst material, and a third volume of material; (c) means for alternately directing a hydrocarbon feedstock and steam first into said first volume of one of said vessels and then into said first volume of the other of said vessels; (d) means for directing the hydrogen containing gas produced in the one of said vessels receiving said feedstock and steam into said fuel electrode of said fuel cell and for directing the exhaust from said fuel electrode and steam into said third volume of material in the other of said vessels; (e) means for directing an oxygen containing gas into said vessels including an inlet means upstream of said second region of reform catalyst; and (f) each of said vessels including combustion products outlet means at its upstream end for exhausting combustion products therefrom during regeneration of each vessel.
Claim 2
Dependent Claim 266 words
A fuel cell system comprising: (a) a fuel cell including a fuel electrode, an oxygen electrode, and an electrolyte disposed therebetween; (b) a pair of reaction vessels, each being adapted to alternately make a hydrogen containing gas and to be regenerated, each of said reaction vessels having an upstream end and a downstream end, each vessel having disposed therein, in sequence from its upstream to downstream end, a first volume of inert packing material containing no reform catalyst, a second volume of material including a first region comprising a regenerable sulfur absorber of oxides of zinc, oxides of iron, zinc ferrite, oxides of chromium, oxides, of copper, oxides of vanadium, oxides of tungsten or mixtures thereof and a second region downstream of said first region comprising reform catalyst material, and a third volume of material; (c) means for alternately directing a hydrocarbon feedstock and steam first into said first volume of one of said vessels and then into said first volume of the other of said vessels; (d) means for directing the hydrogen containing gas produced in the one of said vessels receiving said feedstock and steam into said fuel electrode of said fuel cell and for directing the exhaust from said fuel electrode and steam into said third volume of material in the other of said vessels; (e) means for directing an oxygen containing gas into said vessels including an inlet means upstream of said second region of reform catalyst; and (f) each of said vessels including combustion products outlet means at its upstream end for exhausting combustion products therefrom during regeneration of each vessel.

References Cited (Backward Citations)

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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) 1992-03-27 1992-09-26 1993-03-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-03-27 1996-09-26 1997-03-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-03-27 2000-09-26 2001-03-28 $7700.00 Window Closed / Lapsed

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