US5048284A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of operating gas turbines with reformed fuel
Assignee: Imperial Chemical Industries Ltd
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Filing: 1989-07-11
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Granted: 1991-09-17
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Expires: 2009-07-11
Abstract
Abstract At least during some part-load operation of a gas turbine wherein a fuel gas is combusted with air with the formation of a flame and the combustion products are let down through a turbine, the fuel gas comprises the product of a stage of catalytic autothermal steam reforming of a light hydrocarbon feedstock gas and the amount of air fed to the gas turbine combuster, relative to the amount of hydrocarbon fed to the catalytic autothermal steam reforming stage, is greater than the maximum amount of air that enables a flame to be sustained in said combustor if that amount of hydrocarbon were to be fed directly to the combustor.
Inventors
- 👤 Warwick J. Lywood
- 👤 Jeremy C. B. Hunns
- 👤 Peter J. Davidson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 20:52
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B3/386; B; B01; B01J; B01J8/00; B01J8/02; B01J8/04; B01J8/0446; B01J8/0449; B01J8/0453; B01J8/0492; B01J8/0496; F; F02; F02B; F02B43/00; F02B43/10; F02C; F02C3/00; F02C3/20; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00026; B01J2208/00035; B01J2208/0007; B01J2208/00088; B01J2208/00106; B01J2208/00115; B01J2208/0015; B01J2208/00168; B01J2208/00212; B01J2208/00256; B01J2208/00327; B01J2208/00336; B01J2208/00353; B01J2208/00371; B01J2208/00477; B01J2208/00495; B01J2208/00504; B01J2208/0053; C01B2203/00; C01B2203/02; C01B2203/0205; C01B2203/0227; C01B2203/0233; C01B2203/0244; C01B2203/025; C01B2203/0261; C01B2203/06; C01B2203/08; C01B2203/0805; C01B2203/0811; C01B2203/0822; C01B2203/0827; C01B2203/0838; C01B2203/0844; C01B2203/0866; C01B2203/10; C01B2203/1005; C01B2203/1023; C01B2203/1041; C01B2203/1047; C01B2203/1052; C01B2203/1064; C01B2203/107; C01B2203/12; C01B2203/1205; C01B2203/1211; C01B2203/1235; C01B2203/1241; C01B2203/1276; C01B2203/14; C01B2203/142; C01B2203/143; C01B2203/148; C01B2203/16; C01B2203/1604; C01B2203/80; C01B2203/82; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02T; Y02T10/00; Y02T10/10; Y02T10/30
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
173 words
A method of operating a gas turbine wherein a compressed mixture of a fuel gas and air is combusted in a turbine combustor with the formation of a flame and the combustion products are let down through a turbine producing shaft power, wherein said fuel gas comprises the product of a stage of catalytic autothermal steam reforming of a light hydrocarbon feedstock having a boiling point at atmospheric pressure below 220° C., said catalytic autothermal steam reforming stage comprising reacting a feedstock gas containing the light hydrocarbon feedstock and steam with an amount of air insufficient to cause complete combustion and then passing the resultant hot partially combusted mixture over a catalyst that exhibits steam reforming activity, and the amount of air fed to the gas turbine combustor, relative to the amount of hydrocarbon fed to the catalytic autothermal steam reforming stage, is greater than the maximum amount of air that enables a flame to be sustained in said combustor if that amount of hydrocarbon were to be fed directly to the combustor.
Claim 2
Independent Claim
173 words
A method of operating a gas turbine wherein a compressed mixture of a fuel gas and air is combusted in a turbine combustor with the formation of a flame and the combustion products are let down through a turbine producing shaft power, wherein said fuel gas comprises the product of a stage of catalytic autothermal steam reforming of a light hydrocarbon feedstock having a boiling point at atmospheric pressure below 220° C., said catalytic autothermal steam reforming stage comprising reacting a feedstock gas containing the light hydrocarbon feedstock and steam with an amount of air insufficient to cause complete combustion and then passing the resultant hot partially combusted mixture over a catalyst that exhibits steam reforming activity, and the amount of air fed to the gas turbine combustor, relative to the amount of hydrocarbon fed to the catalytic autothermal steam reforming stage, is greater than the maximum amount of air that enables a flame to be sustained in said combustor if that amount of hydrocarbon were to be fed directly to the combustor.
Claim 3
Dependent Claim
120 words
A process according to claim 1 wherein the catalytic autothermal steam reforming stage comprises: a) feeding the feedstock gas to a mixing zone and therein mixing it with hot recycle gas to form a heated gas mixture; b) separately feeding air, and the heated gas mixture from the mixing zone, to the inlet of a combustion zone containing a combustion catalyst that also exhibits steam reforming activity, whereby partial combustion and reforming of the mixture takes place forming a hot reformed gas stream; c) recycling part of the hot reformed gas stream to the aforesaid mixing zone as said hot recycle gas; and d) feeding the remainder of the hot reformed gas to the gas turbine combustor as fuel gas.
Claim 4
Dependent Claim
27 words
A process according to claim 1 wherein the feedstock gas fed to the catalytic autothermal steam reforming stage contains hydrogen, in addition to the light hydrocarbon feedstock.
Claim 5
Dependent Claim
64 words
A process according to claim 3 wherein the feedstock gas fed to the catalytic autothermal steam reforming stage is the product of passing a heated mixture of steam and at least one hydrocarbon over a low temperature steam reforming catalyst, whereby some preliminary steam reforming of said heated gas is effected before said feedstock gas is fed to the catalytic autothermal steam reforming stage.
Claim 6
Dependent Claim
25 words
A process according to claim 4 wherein said mixture of steam and at least one hydrocarbon is preheated by heat exchange with the turbine exhaust.
Claim 7
Dependent Claim
38 words
A process according to claim 4 wherein said mixture of steam and at least one hydrocarbon that is subjected to said preliminary reforming contains at least one hydrocarbon having a boiling point at atmospheric pressure above 220° C.
Claim 8
Dependent Claim
54 words
A process according to claim 1 wherein water is heated by heat exchange with the turbine exhaust to produce a stream of hot water which is then contacted with a gas stream comprising at least one hydrocarbon so as to form a steam/hydrocarbon mixture which is used as, or to produce, the feedstock gas.
Claim 9
Dependent Claim
28 words
A process according to claim 1 wherein the feedstock gas contains 1 to 3.5 moles of steam for each gram atom of hydrocarbon carbon in said feedstock gas.
Claim 10
Dependent Claim
30 words
A process according to claim 1 wherein said product of the catalytic autothermal steam reforming stage has a hydrogen content of at least 25% by volume on a dry basis.
Claim 11
Dependent Claim
34 words
A process according to claim 1 comprising, when operating said turbine under full load conditions, at least partially bypassing said catalytic autothermal steam reforming stage whereby the fuel gas comprises the light hydrocarbon feedstock.
Claim 12
Dependent Claim
30 words
A process according to claim 1 wherein the catalytic autothermal reforming is conducted at such an elevated pressure that the reformed gas stream is at the desired turbine inlet pressure.
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US3765167A
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US3895488A
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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) | 1994-09-16 | 1995-03-18 | 1995-09-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-09-16 | 1999-03-18 | 1999-09-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-09-16 | 2003-03-18 | 2003-09-17 | $7700.00 | Window Closed / Lapsed |