Patent US4653787A successfully refreshed from Google Patents.
US4049570A
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Method and apparatus for removing vapors and aerosols from gases produced in a gasification plant
Assignee: Dr C Otto and Co GmbH
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Filing: 1975-08-04
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Granted: 1977-09-20
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Expires: 1995-08-04
Abstract
Abstract The high temperature gasification of solid fuel or mixtures of solid and liquid fuels is carried out by a method and apparatus wherein the gasified product from a high temperature gasification chamber having a slag bath therein is fed into a first dust collector. Gases, including vapors or aerosols, are fed from the dust collector into a waste heat boiler to reduce the temperature of the gases down to about 250° C. The solids which essentially include flue coke are discharged from the dust collector into a separate heat exchanger wherein the temperature of the solids is reduced down to about 200° C. The cooled solids and the cooled gases are fed into an absorption chamber wherein for a period of 1 to 10 seconds, the aerosols are absorbed into the flue coke. The absorption chamber is connected to a second dust collector that separates the gases from the flue coke having the absorbed aerosols. The purified gases are then discharged from the second dust collector and the flue coke with the absorbed aerosols is returned to the slag bath in the gasification chamber.
Inventors
- 👤 Paul Gernhardt
- 👤 Wolfgang Grams
- 👤 Siegfried Pohl
- 👤 Wilhelm Danguillier
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 15:58
CPC Classifications
C; C10; C10K; C10K1/00; C10J; C10J3/00; C10J3/57; C10J3/72; C10J3/78; C10J3/82; C10J3/84; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0943; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0969; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1807; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/32; Y02P; Y02P20/00; Y02P20/10; Y02P20/129
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
233 words
In a process for removing vapors or aerosols from the product of high temperature gasification of solid fuel or a mixture of solid and liquid fuels wherein the fuel is fed into a gasification chamber of the type including a melting chamber therein having a slag bath at the bottom thereof, and wherein a mixture of gases and solids is discharged from the top of the gasification chamber at a temperature within the range of 800° C. to 1000° C. and slag is normally discharged from the bottom of the gasification chamber, the improvement comprising the steps of: separating said mixture after discharge from the gasification chamber into a gas phase including aerosols and into a solid phase which essentially includes flue coke, separately cooling at least down to a temperature within the range of 300° C. to 100° C. both the gases and the solids after separation thereof, combining the cooled gases and the cooled solids for a period of 1 to 10 seconds within a chamber for the absorption of aerosols by the flue coke from the gases, separating flue coke including the absorbed aerosols from the remaining gases consisting cheifly of carbon monoxide and hydrogen, discharging said remaining gases, returning the flue coke including the absorbed aerosols to said melting chamber for gasification of the flue coke, and discharging aerosols together with slag from the bottom of said gasification chamber.
Claim 2
Dependent Claim
233 words
In a process for removing vapors or aerosols from the product of high temperature gasification of solid fuel or a mixture of solid and liquid fuels wherein the fuel is fed into a gasification chamber of the type including a melting chamber therein having a slag bath at the bottom thereof, and wherein a mixture of gases and solids is discharged from the top of the gasification chamber at a temperature within the range of 800° C. to 1000° C. and slag is normally discharged from the bottom of the gasification chamber, the improvement comprising the steps of: separating said mixture after discharge from the gasification chamber into a gas phase including aerosols and into a solid phase which essentially includes flue coke, separately cooling at least down to a temperature within the range of 300° C. to 100° C. both the gases and the solids after separation thereof, combining the cooled gases and the cooled solids for a period of 1 to 10 seconds within a chamber for the absorption of aerosols by the flue coke from the gases, separating flue coke including the absorbed aerosols from the remaining gases consisting cheifly of carbon monoxide and hydrogen, discharging said remaining gases, returning the flue coke including the absorbed aerosols to said melting chamber for gasification of the flue coke, and discharging aerosols together with slag from the bottom of said gasification chamber.
Claim 3
Dependent Claim
31 words
The method according to claim 1 wherein the gases are cooled after separation from the solids to a temperature of about 250° C. before said step of combining the cooled gases.
Claim 4
Dependent Claim
31 words
The method according to claim 1 wherein the solids are cooled after separation from the gases to a temperature of about 200° C. before said step of combining the cooled gases.
Claim 5
Dependent Claim
47 words
The method according to claim 1 wherein said mixture is fed into a dust collector for said step of separating said mixture and wherein said gases after separation are fed into a waste heat boiler for said step of separately cooling both the gases and the solids.
Claim 6
Dependent Claim
39 words
The method according to claim 4 wherein the flue coke with the absorbed aerosols and the gases are fed into a dust collector for said step of separating the flue coke including the absorbed aerosols from the remaining gases.
Claim 7
Dependent Claim
29 words
The method according to claim 1 wherein the cooled gases and the cooled solids remain in a chamber during said step of combining for a period of 5 seconds.
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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) | 1980-09-19 | 1981-03-21 | 1981-09-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-19 | 1985-03-21 | 1985-09-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-19 | 1989-03-21 | 1989-09-20 | $7700.00 | Window Closed / Lapsed |