US4569194A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Integrated coal-fired gas turbine power plant
Assignee: General Electric Co
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Filing: 1984-02-10
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Granted: 1986-02-11
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Expires: 2004-02-10
Abstract
Abstract An integrated coal-fired gas turbine power plant includes a hydraulic compressor for providing pressurized air to a coal combustion system and cooling air to the gas turbine. The power plant may further include a regenerator between the compressor and the combustion system, and a gas cleanup segment between the combustion system and the gas turbine.
Inventors
- 👤 Walter B. Giles
- 👤 Norman J. Lipstein
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 13:56
CPC Classifications
F; F02; F02C; F02C3/00; F02C3/20; F02C3/205; Y; Y02; Y02E; Y02E20/00; Y02E20/16
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
168 words
An apparatus for the utilization of coal comprising: a coal combustion system including a pressurized fluidized bed gasifier; a gas cleanup segment in flow communication with said pressurized fluidized bed gasifier; an expansion turbine in flow communication with said gas cleanup segment; means for substantially isothermally producing a pressurized fluid at a temperature below about 650° F., said means being in flow communication with said coal combustion system and including a hydraulic compressor and a regenerator connected intermediate said hydraulic compressor and said coal combustion system, said regenerator being in heat exchange relationship with the exhaust of said expansion turbine, whereby said regenerator recovers heat from the exhaust of said expansion turbine for exhaust temperatures above the temperature of said pressurized fluid before said fluid passes through said regenerator; and means for supplying a flow of cooling fluid from said pressurized fluid producing means to said gas cleanup segment; said gas cleanup segment comprising an alkali scrubber system having means for circulating said flow of cooling fluid therethrough.
Claim 2
Independent Claim
168 words
An apparatus for the utilization of coal comprising: a coal combustion system including a pressurized fluidized bed gasifier; a gas cleanup segment in flow communication with said pressurized fluidized bed gasifier; an expansion turbine in flow communication with said gas cleanup segment; means for substantially isothermally producing a pressurized fluid at a temperature below about 650° F., said means being in flow communication with said coal combustion system and including a hydraulic compressor and a regenerator connected intermediate said hydraulic compressor and said coal combustion system, said regenerator being in heat exchange relationship with the exhaust of said expansion turbine, whereby said regenerator recovers heat from the exhaust of said expansion turbine for exhaust temperatures above the temperature of said pressurized fluid before said fluid passes through said regenerator; and means for supplying a flow of cooling fluid from said pressurized fluid producing means to said gas cleanup segment; said gas cleanup segment comprising an alkali scrubber system having means for circulating said flow of cooling fluid therethrough.
Claim 3
Independent Claim
189 words
An apparatus for the utilization of coal comprising: a coal combustion system including a pressurized fluidized bed gasifier; a gas cleanup segment in flow communication with said pressurized fluidized bed gasifier; an expansion turbine in flow communication with said gas cleanup segment; means for substantially isothermally producing a pressurized fluid at a temperature below about 650° F., said means being in flow communication with said coal combustion system and including a hydraulic compressor and a regenerator connected intermediate said hydraulic compressor and said coal combustion system, said regenerator being in heat exchange relationship with the exhaust of said expansion turbine, whereby said regenerator recovers heat from the exhaust of said expansion turbine for exhaust temperatures above the temperature of said pressurized fluid before said fluid passes through said regenerator; means for supplying a flow of cooling fluid from said pressurized fluid producing means to said gas cleanup segment; said gas cleanup segment comprising an alkali scrubber system having means for circulating said flow of cooling fluid therethrough; and said means for circulating cooling fluid through said alkali scrubber system being in substantially direct flow communication with said hydraulic compressor.
Claim 4
Independent Claim
189 words
An apparatus for the utilization of coal comprising: a coal combustion system including a pressurized fluidized bed gasifier; a gas cleanup segment in flow communication with said pressurized fluidized bed gasifier; an expansion turbine in flow communication with said gas cleanup segment; means for substantially isothermally producing a pressurized fluid at a temperature below about 650° F., said means being in flow communication with said coal combustion system and including a hydraulic compressor and a regenerator connected intermediate said hydraulic compressor and said coal combustion system, said regenerator being in heat exchange relationship with the exhaust of said expansion turbine, whereby said regenerator recovers heat from the exhaust of said expansion turbine for exhaust temperatures above the temperature of said pressurized fluid before said fluid passes through said regenerator; means for supplying a flow of cooling fluid from said pressurized fluid producing means to said gas cleanup segment; said gas cleanup segment comprising an alkali scrubber system having means for circulating said flow of cooling fluid therethrough; and said means for circulating cooling fluid through said alkali scrubber system being in substantially direct flow communication with said hydraulic compressor.
Claim 5
Dependent Claim
208 words
A process for the utilization of coal comprising: substantially isothermally producing compressed gas at a temperature below about 650° F., in a hydraulic compressor; passing at least a portion of the compressed gas from the hydraulic compressor through a regenerator; introducing the compressed gas that passes through the regenerator into a coal combustion system comprising a pressurized fluidized bed gasifier for inter-reaction with coal contained in said gasifier; introducing the gaseous effluent from the gasifier into an expansion turbine and expanding said effluent therein such that the turbine is driven to provide useful work; removing the expanded gaseous effluent from the turbine and passing it in heat exchange relationship with the compressed gas passing through the regenerator, whereby the regenerator recovers heat from the exhaust of the turbine for exhaust temperatures above the temperature of the compressed gas before said gas passes through the regenerator; and diverting a portion of the compressed gas to a gas cleanup segment of the coal combustion system for the purpose of cooling said segment; said step of diverting a portion of the compressed gas to the gas cleanup segment comprising diverting said portion of the compressed gas to an alkali scrubber system and circulating therethrough said diverted portion of the compressed gas.
Claim 6
Dependent Claim
208 words
A process for the utilization of coal comprising: substantially isothermally producing compressed gas at a temperature below about 650° F., in a hydraulic compressor; passing at least a portion of the compressed gas from the hydraulic compressor through a regenerator; introducing the compressed gas that passes through the regenerator into a coal combustion system comprising a pressurized fluidized bed gasifier for inter-reaction with coal contained in said gasifier; introducing the gaseous effluent from the gasifier into an expansion turbine and expanding said effluent therein such that the turbine is driven to provide useful work; removing the expanded gaseous effluent from the turbine and passing it in heat exchange relationship with the compressed gas passing through the regenerator, whereby the regenerator recovers heat from the exhaust of the turbine for exhaust temperatures above the temperature of the compressed gas before said gas passes through the regenerator; and diverting a portion of the compressed gas to a gas cleanup segment of the coal combustion system for the purpose of cooling said segment; said step of diverting a portion of the compressed gas to the gas cleanup segment comprising diverting said portion of the compressed gas to an alkali scrubber system and circulating therethrough said diverted portion of the compressed gas.
Claim 7
Dependent Claim
235 words
A process for the utilization of coal comprising: substantially isothermally producing compressed gas at a temperature below about 650° F., in a hydraulic compressor; passing at least a portion of the compressed gas from the hydraulic compressor through a regenerator; introducing the compressed gas that passes through the regenerator into a coal combustion system comprising a pressurized fluidized bed gasifier for inter-reaction with coal contained in said gasifier; introducing the gaseous effluent from the gasifier into an expansion turbine and expanding said effluent therein such that the turbine is driven to provide useful work; removing the expanded gaseous effluent from the turbine and passing it in heat exchange relationship with the compressed gas passing through the regenerator, whereby the regenerator recovers heat from the exhaust of the turbine for exhaust temperatures above the temperature of the compressed gas before said gas passes through the regenerator; diverting a portion of the compressed gas to a gas cleanup segment of the coal combustion system for the purpose of cooling said segment; said step of diverting a portion of the compressed gas to the gas cleanup segment comprising diverting said portion of the compressed gas to an alkali scrubber system and circulating therethrough said diverted portion of the compressed gas; and said step of circulating said diverted portion of the compressed gas through the alkali scrubber being carried out in substantially direct flow communication with the hydraulic compressor.
Claim 8
Dependent Claim
235 words
A process for the utilization of coal comprising: substantially isothermally producing compressed gas at a temperature below about 650° F., in a hydraulic compressor; passing at least a portion of the compressed gas from the hydraulic compressor through a regenerator; introducing the compressed gas that passes through the regenerator into a coal combustion system comprising a pressurized fluidized bed gasifier for inter-reaction with coal contained in said gasifier; introducing the gaseous effluent from the gasifier into an expansion turbine and expanding said effluent therein such that the turbine is driven to provide useful work; removing the expanded gaseous effluent from the turbine and passing it in heat exchange relationship with the compressed gas passing through the regenerator, whereby the regenerator recovers heat from the exhaust of the turbine for exhaust temperatures above the temperature of the compressed gas before said gas passes through the regenerator; diverting a portion of the compressed gas to a gas cleanup segment of the coal combustion system for the purpose of cooling said segment; said step of diverting a portion of the compressed gas to the gas cleanup segment comprising diverting said portion of the compressed gas to an alkali scrubber system and circulating therethrough said diverted portion of the compressed gas; and said step of circulating said diverted portion of the compressed gas through the alkali scrubber being carried out in substantially direct flow communication with the hydraulic compressor.
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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) | 1989-02-10 | 1989-08-12 | 1990-02-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-02-10 | 1993-08-12 | 1994-02-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-02-10 | 1997-08-12 | 1998-02-11 | $7700.00 | Window Closed / Lapsed |