Patent US4733528A successfully refreshed from Google Patents.
US4733528A
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Energy recovery
Assignee: Imperial Chemical Industries Ltd
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Filing: 1986-05-30
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Granted: 1988-03-29
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Expires: 2006-05-30
Abstract
Abstract Energy is recovered from low calorific value gas by means of a gas turbine. Heat is recovered from the turbine exhaust by indirect heat exchange with water. The resultant hot water is used to saturate the fuel and, optionally, also the combustion air, and/or to aid regeneration of an absorbent used in a wet process to remove carbon dioxide from the gas prior to combustion. Preferably the low calorific value gas is waste gas from a PSA process used to remove impurities in the production of a hydrogen-containing gas stream from a raw gas made by primary/secondary steam reforming a hydrocarbon feedstock at superatmospheric pressure and the turbine drives the secondary reformer air compressor.
Inventors
- 👤 Alwyn Pinto
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 13:30
CPC Classifications
F; F02; F02C; F02C3/00; F02C3/20; F02C3/30; C; C01; C01B; C01B3/00; C01B3/02; C01B3/025; C01B3/32; C01B3/34; C01B3/48; C01B3/50; C01B3/56; F01; F01K; F01K21/00; F01K21/04; F01K21/047; F02C3/22; B; B01; B01D; B01D2256/00; B01D2256/16; B01D2257/00; B01D2257/10; B01D2257/102; B01D2257/108; B01D2257/11; B01D2257/50; B01D2257/502; B01D2257/504; B01D2257/70; B01D2257/702; B01D2257/7022; B01D2257/7025; B01D2259/00; B01D2259/40; B01D2259/40001; B01D2259/416; B01D53/00; B01D53/02; B01D53/04; B01D53/047; C01B2203/00; C01B2203/02; C01B2203/0205; C01B2203/0227; C01B2203/0233; C01B2203/0244; C01B2203/025; C01B2203/0261; C01B2203/0283; C01B2203/0288; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0435; C01B2203/044; C01B2203/0445; C01B2203/0465; C01B2203/047; C01B2203/0475; C01B2203/0495; C01B2203/06; C01B2203/068; C01B2203/08; C01B2203/0805; C01B2203/0811; C01B2203/0816; C01B2203/0822; C01B2203/0827; C01B2203/0833; C01B2203/0838; C01B2203/0844; C01B2203/0866; C01B2203/0872; C01B2203/0883; C01B2203/10; C01B2203/1005; C01B2203/1023; C01B2203/1041; C01B2203/1047; C01B2203/1052; C01B2203/1064; C01B2203/107; C01B2203/1076; C01B2203/12; C01B2203/1205; C01B2203/1211; C01B2203/1217; C01B2203/1223; C01B2203/1235; C01B2203/1241; C01B2203/1258; C01B2203/1276; C01B2203/14; C01B2203/142; C01B2203/143; C01B2203/146; C01B2203/147; C01B2203/148; C01B2203/80; C01B2203/82; Y; Y02; Y02C; Y02C20/00; Y02C20/20; Y02C20/40; Y02E; Y02E20/00; Y02E20/32; Y02P; Y02P20/00; Y02P20/10; Y02P20/151; Y02P20/156
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
215 words
A process for the recovery of energy by the production of shaft power from a fuel gas comprising: carbon dioxide; and at least one combustible gas selected from: methane; hydrogen; and carbon monoxide; said fuel gas having a composition such that its calorific value is below 1100 BTU/scf (41 MJ.m -3 ) and containing at least 20% by volume of carbon dioxide; said process comprising: (a) contacting said gas with an aqueous solution of an absorbent for carbon dioxide, whereby carbon dioxide is absorbed from said gas into said absorbent solution and the resultant carbon dioxide depleted gas is saturated with water vapor; (b) separating the saturated carbon dioxide-depleted gas from said absorbent, so as to give a saturated carbon dioxide depleted gas having a calorific value of 15 to 1100 BTU/scf (0.6 to 41 MJ.m -3 ); (c) regenerating said absorbent by heating, and returning the regenerated absorbent to step (a); (d) compressing air in a compressor; (e) combusting said carbon dioxide-depleted gas with said compressed air in a combustion zone; (f) expanding the resultant combustion products in an expander driving said compressor and producing the shaft power; and (g) recovering heat from the turbine exhaust gas by indirect heat exchange and using said recovered heat to heat the absorbent in the regeneration thereof.
Claim 2
Dependent Claim
215 words
A process for the recovery of energy by the production of shaft power from a fuel gas comprising: carbon dioxide; and at least one combustible gas selected from: methane; hydrogen; and carbon monoxide; said fuel gas having a composition such that its calorific value is below 1100 BTU/scf (41 MJ.m -3 ) and containing at least 20% by volume of carbon dioxide; said process comprising: (a) contacting said gas with an aqueous solution of an absorbent for carbon dioxide, whereby carbon dioxide is absorbed from said gas into said absorbent solution and the resultant carbon dioxide depleted gas is saturated with water vapor; (b) separating the saturated carbon dioxide-depleted gas from said absorbent, so as to give a saturated carbon dioxide depleted gas having a calorific value of 15 to 1100 BTU/scf (0.6 to 41 MJ.m -3 ); (c) regenerating said absorbent by heating, and returning the regenerated absorbent to step (a); (d) compressing air in a compressor; (e) combusting said carbon dioxide-depleted gas with said compressed air in a combustion zone; (f) expanding the resultant combustion products in an expander driving said compressor and producing the shaft power; and (g) recovering heat from the turbine exhaust gas by indirect heat exchange and using said recovered heat to heat the absorbent in the regeneration thereof.
Claim 3
Dependent Claim
23 words
A process according to claim 1 wherein the carbon dioxide depleted gas has a calorific value below 300 BTU/scf (11 MJ/m -3 ).
Claim 4
Dependent Claim
15 words
A process according to claim 1 wherein the carbon dioxide depleted gas is combusted catalytically.
Claim 5
Dependent Claim
22 words
A process according to claim 1 wherein the fuel gas is compressed prior to combustion by a compressor driven by said turbine.
Claim 6
Dependent Claim
12 words
A process according to claim 1 wherein the fuel gas contains hydrogen.
Claim 7
Dependent Claim
25 words
A process according to claim 5 wherein the low calorific value gas is waste gas from a pressure swing adsorption process producing a hydrogen-containing product.
Claim 8
Dependent Claim
36 words
A process according to claim 6 wherein the raw gas fed to the pressure swing adsorption process is made by reacting, at superatmospheric pressure, a carbonaceous feedstock with an oxygen-containing gas, and, optionally, also with steam.
Claim 9
Dependent Claim
60 words
A process according to claim 7 wherein the carbonaceous feedstock is a hydrocarbon feedstock and is catalytically primary steam reformed, the resultant primary reformed gas, containing an excess of steam, is mixed with an oxygen-containing gas and subjected to catalytic secondary steam reforming, and the heat required for the primary steam reforming is supplied by the secondary reformer outlet gas.
Claim 10
Dependent Claim
26 words
A process according to claim 8 wherein the turbine provides the power required to compress the oxygen-containing gas used in the reaction with the carbonaceous feedstock.
Claim 11
Dependent Claim
35 words
A process according to claim 9 wherein the process conditions are selected such that there is approximate equality between the power required to compress the oxygen-containing gas and the net power output of the turbine.
Claim 12
Dependent Claim
41 words
A process according to claim 1 wherein the carbon dioxide depleted gas is saturated with steam by direct heat exchange with hot water heated by indirect heat exchange of the turbine exhaust gas with water under sufficient pressure to prevent boiling.
Claim 13
Dependent Claim
39 words
A process according to claim 1, wherein the compressed air is saturated with steam by direct heat exchange with hot water heated by indirect heat exchange of the turbine exhaust gas with water under sufficient pressure to prevent boiling.
Claim 14
Dependent Claim
31 words
A process according to claim 1, wherein the compressed air and/or the carbon dioxide depleted gas is heated, prior to entering the combustion zone, by heat exchange with the turbine effluent.
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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) | 1991-03-29 | 1991-09-28 | 1992-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-03-29 | 1995-09-28 | 1996-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-03-29 | 1999-09-28 | 2000-03-29 | $7700.00 | Window Closed / Lapsed |