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US5342702A
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Synergistic process for the production of carbon dioxide using a cogeneration reactor
Assignee: Integrated Energy Development Corp
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Filing: 1993-01-05
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Granted: 1994-08-30
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Expires: 2013-01-05
Abstract
Abstract A synergistic process for the production of carbon dioxide comprises preparing a feed stream comprising an organic combustible fuel and hydrogen; introducing the feed stream and air into a cogeneration reactor for combusting the feed stream and producing steam, electricity and stack gases containing carbon dioxide; using at least a portion of said electricity to electrolyze water to produce hydrogen and oxygen; recovering the hydrogen and oxygen and recycling at least a portion of the hydrogen for preparation of the feed stream; and, recovering the carbon dioxide from the stack gases.
Inventors
- 👤 Norman J. MacGregor
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 13:52
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; C01; C01B; C01B32/00; C01B32/50; F; F01; F01K; F01K25/00; F01K25/005; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y10; Y10S; Y10S204/00; Y10S204/04
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
121 words
A synergistic cogeneration process for the production of carbon dioxide, oxygen and hydrogen comprising the steps of: (a) preparing a feed stream comprising an organic combustible fuel and hydrogen; (b) introducing said feed stream and air into a cogeneration reactor for combusting said feed stream and producing steam, electricity and stack gases containing carbon dioxide, said reactor having a generator and means for combusting said feed stream drivingly connected to said generator via shaft means; (c) using electricity to electrolyze water to produce hydrogen and oxygen; (d) recovering said hydrogen from step (c) and recycling at least a portion of said hydrogen to step (a) for preparation of said feed stream; and, (e) recovering said carbon dioxide from said stack gases.
Claim 2
Dependent Claim
121 words
A synergistic cogeneration process for the production of carbon dioxide, oxygen and hydrogen comprising the steps of: (a) preparing a feed stream comprising an organic combustible fuel and hydrogen; (b) introducing said feed stream and air into a cogeneration reactor for combusting said feed stream and producing steam, electricity and stack gases containing carbon dioxide, said reactor having a generator and means for combusting said feed stream drivingly connected to said generator via shaft means; (c) using electricity to electrolyze water to produce hydrogen and oxygen; (d) recovering said hydrogen from step (c) and recycling at least a portion of said hydrogen to step (a) for preparation of said feed stream; and, (e) recovering said carbon dioxide from said stack gases.
Claim 3
Dependent Claim
16 words
The process as claimed in claim 1 wherein said organic combustible fuel is a gaseous fuel.
Claim 4
Dependent Claim
13 words
The process as claimed in claim 2 wherein said gaseous fuel comprises methane.
Claim 5
Dependent Claim
14 words
The process as claimed in claim 3 wherein said gaseous fuel is natural gas.
Claim 6
Dependent Claim
34 words
The process as claimed in claim 3 wherein said oxygen is recovered from electrolysis step (c) and at least a portion of said oxygen is recycled to step (b) for introduction into said reactor.
Claim 7
Dependent Claim
26 words
The process as claimed in claim 5 wherein at least a portion of said electricity used to power electrolysis step (c) is produced in off-peak time.
Claim 8
Dependent Claim
23 words
The process as claimed in claim 6 wherein said feed stream comprises from about 10% to about 20% hydrogen on a volume basis.
Claim 9
Dependent Claim
19 words
The process as claimed in claim 7 wherein said feed stream contains about 15% hydrogen on a volume basis.
Claim 10
Dependent Claim
27 words
The process as claimed in claim 7 wherein said feed stream is combusted in air and from about 0% to about 30% oxygen on a volume basis.
Claim 11
Dependent Claim
23 words
The process as claimed in claim 9 wherein said feed stream is combusted with air and about 15% oxygen on a volume basis.
Claim 12
Dependent Claim
33 words
The process as claimed in claim 9 further comprising the step of adding at least a portion of said carbon dioxide recovered in the step (e) to a methanol synthesizer to produce methanol.
Claim 13
Dependent Claim
26 words
The process as claimed in claim 11 further compressing the step of reforming at least a portion of said methanol to produce methyl tertiary butyl ether.
Claim 14
Dependent Claim
16 words
The process as claimed in claim 11 wherein said cogeneration reactor is a single cycle cogenerator.
Claim 15
Dependent Claim
16 words
The process as claimed in claim 11 wherein said cogeneration reactor is a combined cycle cogenerator.
Claim 16
Dependent Claim
28 words
The process as claimed in claim 9 wherein at least a portion of said steam is added to a fermenter together with an alcohol precursor to produce ethanol.
Claim 17
Dependent Claim
26 words
The process as claimed in claim 15 further comprising the step of reforming at least a portion of said ethanol to produce ethanyl tertiary butyl ether.
Claim 18
Dependent Claim
136 words
A synergistic cogeneration process for the production of methanol comprising the steps of: (a) preparing a feed stream comprising an organic combustible fuel and hydrogen; (b) introducing said feed stream and air into a cogeneration reactor for combusting said feed stream and producing steam, electricity and stack gases containing carbon dioxide, said reactor having a generator and means for combusting said feed stream drivingly connected to said generator via shaft means; (c) electrolyzing water to produce hydrogen and oxygen; (d) recovering said hydrogen from step (c) and recycling at least a portion of said hydrogen to step (a) for preparation of said feed stream; (e) recovering said carbon dioxide from said stack gases; and, (f) adding at least a portion of said carbon dioxide recovered in the step (e) to a methanol synthesizer to produce methanol.
Claim 19
Dependent Claim
136 words
A synergistic cogeneration process for the production of methanol comprising the steps of: (a) preparing a feed stream comprising an organic combustible fuel and hydrogen; (b) introducing said feed stream and air into a cogeneration reactor for combusting said feed stream and producing steam, electricity and stack gases containing carbon dioxide, said reactor having a generator and means for combusting said feed stream drivingly connected to said generator via shaft means; (c) electrolyzing water to produce hydrogen and oxygen; (d) recovering said hydrogen from step (c) and recycling at least a portion of said hydrogen to step (a) for preparation of said feed stream; (e) recovering said carbon dioxide from said stack gases; and, (f) adding at least a portion of said carbon dioxide recovered in the step (e) to a methanol synthesizer to produce methanol.
Claim 20
Dependent Claim
34 words
The process as claimed in claim 17 wherein said oxygen is recovered from electrolysis step (c) and at least a portion of said oxygen is recycled to step (b) for introduction into said reactor.
Claim 21
Dependent Claim
16 words
The process as claimed in claim 18 wherein said organic combustible fuel is a gaseous fuel.
Claim 22
Dependent Claim
24 words
The process as claimed in claim 19 wherein a portion of the electricity produced in step (c) is used to power electrolysis step (c).
Claim 23
Dependent Claim
26 words
The process as claimed in claim 17 wherein at least a portion of said electricity used to power electrolysis step (c) is produced in off-peak time.
References Cited (Backward Citations)
US2482284A
Cited
US3095699A
Cited
US4592762A
Cited
US4810417A
Cited
US4534772A
Cited
US4773981A
Cited
US5023276A
Cited
US4528811A
Cited
US4699632A
Cited
US5026529A
Cited
US5132007A
Cited
US4899544A
Cited
US4833170A
Cited
US4942734A
Cited
US5025631A
Cited
US5070016A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1997-08-29 | 1998-02-28 | 1998-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2001-08-29 | 2002-02-28 | 2002-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2005-08-29 | 2006-02-28 | 2006-08-30 | $7700.00 | Window Closed / Lapsed |