US4741290A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the combustion of carbonaceous materials in a circulating fluidized bed, and fluidized bed furnace installation for performing the process
Assignee: Hitachi Zosen Inova Steinmueller GmbH
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Filing: 1987-07-28
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Granted: 1988-05-03
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Expires: 2007-07-28
Abstract
Abstract In a process and a fluidized bed furnace installation for performing the process for the combustion of carbonaceous materials in a fluidized bed reactor with an atmospheric or pressurized, circulating fluidized bed, wherein solids are circulated in a circulation system consisting of a fluidized bed reactor, at least one separator, and at least one return line, and wherein solids are withdrawn from the circulation system, and wherein the stack gases are discharged downstream of the separator, and wherein combustion heat is removed at least by way of heating surfaces of the fluidized bed reactor and by way of stack-gas-exposed heating surfaces downstream of the separator, the invention provides that a partial stream of solids withdrawn from the circulation system is admixed to the stack gases or waste gases, exiting from the separator, upstream of the heating surfaces for the removal of heat from the stack gases.
Inventors
- 👤 Ernst Krieger
- 👤 Karl Ihne
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 19:58
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/02; F22; F22B; F22B31/00; F22B31/0007; F22B31/0084
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
132 words
Process for the combustion of carbonaceous materials in a fluidized bed reactor with an atmospheric or pressurized, circulating fluidized bed wherein solids are circulated in a circulation system consisting of the fluidized bed reactor, at least one separator, and at least one return line, and solids are withdrawn from the circulation system, and wherein the flue gases are discharged downstream of the separator, and wherein combustion heat is removed at least by way of heating surfaces of the fluidized bed reactor and by way of stack-gas-exposed heating surfaces downstream of the separator, characterized in that a partial stream of solids withdrawn from the circulation system is admixed to the stack gases or waste gases, exiting from the separator, upstream of the heating surfaces for the removal of heat from the stack gases.
Claim 2
Dependent Claim
132 words
Process for the combustion of carbonaceous materials in a fluidized bed reactor with an atmospheric or pressurized, circulating fluidized bed wherein solids are circulated in a circulation system consisting of the fluidized bed reactor, at least one separator, and at least one return line, and solids are withdrawn from the circulation system, and wherein the flue gases are discharged downstream of the separator, and wherein combustion heat is removed at least by way of heating surfaces of the fluidized bed reactor and by way of stack-gas-exposed heating surfaces downstream of the separator, characterized in that a partial stream of solids withdrawn from the circulation system is admixed to the stack gases or waste gases, exiting from the separator, upstream of the heating surfaces for the removal of heat from the stack gases.
Claim 3
Dependent Claim
43 words
Process according to claim 1, characterized in that the partial stream of solids is withdrawn together with waste gas from the circulation system between the fluidized bed reactor and the separator, and is readmixed to the treated gas stream downstream of the separator.
Claim 4
Dependent Claim
34 words
Process according to claim 1, characterized in that the partial stream of solids introduced into the stack gas is separated from the stack gas after its cooling and recycled into the fluidized bed reactor.
Claim 5
Dependent Claim
105 words
Fluidized bed furnace installation, especially steam generator, with a circulation system at least consisting of a fluidized bed reactor with at least one heating surface, a separator arranged downstream thereof, and a return line from the separator to the fluidized bed reactor, and with a waste heat disposal unit connected downstream of the separator on the waste gas side, characterized in that a device (10) is provided for withdrawing a partial stream of solids from the circulation system (3, 4, 5, 6) and a device is furthermore provided for admixing the partial stream of solids into the stack gases (7) exiting from the separator (5).
Claim 6
Dependent Claim
105 words
Fluidized bed furnace installation, especially steam generator, with a circulation system at least consisting of a fluidized bed reactor with at least one heating surface, a separator arranged downstream thereof, and a return line from the separator to the fluidized bed reactor, and with a waste heat disposal unit connected downstream of the separator on the waste gas side, characterized in that a device (10) is provided for withdrawing a partial stream of solids from the circulation system (3, 4, 5, 6) and a device is furthermore provided for admixing the partial stream of solids into the stack gases (7) exiting from the separator (5).
Claim 7
Dependent Claim
26 words
Fluidized bed furnace installation according to claim 4, characterized in that the separator (5) is associated with a bypass conduit (10) on the stack gas side.
Claim 8
Dependent Claim
57 words
Fluidized bed furnace installation according to claim 4, characterized in that the waste heat disposal unit consists of a stack gas flue (8) with heating surfaces (9) and of an air preheater (15) optionally connected downstream thereof, and the solids can be introduced upstream of the stack gas flue (8) and/or upstream of the air preheater (15).
Claim 9
Dependent Claim
45 words
Apparatus according to claim 4, characterized in that a separator (13; 13') is arranged downstream of the waste heat disposal unit, this separator being connected on the solids side with the fluidized bed reactor (1) and on the gas side with a dust filter (16).
References Cited (Backward Citations)
DE2539546A1
Cited
US4111158A
Cited
US4471723A
Cited
US4522154A
Cited
EP0158033A2
Cited
US4665865A
Cited
US4682567A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-05-03 | 1991-11-02 | 1992-05-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-05-03 | 1995-11-02 | 1996-05-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-05-03 | 1999-11-02 | 2000-05-03 | $7700.00 | Window Closed / Lapsed |