US3932146A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the fluid bed gasification of agglomerating coals
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1974-07-11
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Granted: 1976-01-13
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Expires: 1994-07-11
Abstract
Abstract Feed coal particles are mixed with fine particles of devolatilized carbonaceous material having an average particle diameter less than about 25% of that of the coal and then injected into a high temperature fluidized bed gasification zone. The devolatilized material adheres to the coal particles as they soften and forms a nonsticky coating which hinders the formation of large coal agglomerates. During the gasification process the adhering particles are retained in the bed and at least partially gasified, resulting in better carbon utilization than might otherwise be obtained.
Inventors
- 👤 Edward L. Wilson
- 👤 Willard N. Mitchell
- 👤 Hermann E. VON Rosenberg
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 12:07
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/54; C10J3/48; C10J3/482; C10J3/72; C10J3/723; C10J3/78; C10J3/82; C10J3/84; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/16; C10J2300/1603; C10J2300/1606; C10J2300/18; C10J2300/1807; C10J2300/1861; C10J2300/1884; C10J2300/1892
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
111 words
In a process wherein carbonaceous solids containing volatilizable hydrocarbons which solids tend to agglomerate at elevated temperatures are fed into a high temperature fluidized bed reactor and gasified to produce a synthetic gas, the improvement which comprises mixing fine particles of devolatilized carbonaceous material having an average particle diameter less than about 25% of that of said carbonaceous solids with said carbonaceous solids in a weight ratio between about 0.1:1 and about 5:1 at a temperature below the softening point of said carbonaceous solids and introducing the resulting mixture of fine particles of devolatilized carbonaceous material and carbonaceous solids at a temperature below said softening point into said fluidized bed reactor.
Claim 2
Dependent Claim
111 words
In a process wherein carbonaceous solids containing volatilizable hydrocarbons which solids tend to agglomerate at elevated temperatures are fed into a high temperature fluidized bed reactor and gasified to produce a synthetic gas, the improvement which comprises mixing fine particles of devolatilized carbonaceous material having an average particle diameter less than about 25% of that of said carbonaceous solids with said carbonaceous solids in a weight ratio between about 0.1:1 and about 5:1 at a temperature below the softening point of said carbonaceous solids and introducing the resulting mixture of fine particles of devolatilized carbonaceous material and carbonaceous solids at a temperature below said softening point into said fluidized bed reactor.
Claim 3
Dependent Claim
17 words
A process as defined by claim 1 wherein said carbonaceous solids comprise particles of an agglomerating coal.
Claim 4
Dependent Claim
20 words
A process as defined by claim 1 wherein said fine particles of devolatilized carbonaceous material comprise particles of fluid coke.
Claim 5
Dependent Claim
27 words
A process as defined by claim 1 wherein said fine particles of devolatilized carbonaceous material are fines recovered from the gas produced in said fluidized bed reactor.
Claim 6
Dependent Claim
28 words
A process as defined by claim 1 wherein said fine particles of devolatilized carbonaceous material are produced by crushing larger char particles withdrawn from said fluidized bed reactor.
Claim 7
Dependent Claim
31 words
A process as defined by claim 1 wherein said fine particles of devolatilized carbonaceous material are mixed with said carbonaceous solids in a weight ratio between about 0.5:1 and about 3:1.
Claim 8
Dependent Claim
133 words
A process for the gasification of a bituminous coal which comprises: a. introducing at a temperature below the softening point of said coal a mixture of particles of said coal and fine char having an average particle diameter less than about 25% of that of said coal particles in a weight ratio between about 0.1:1 and about 5:1 into a fluidized bed gasification zone; b. withdrawing a product gas overhead from said fluidized bed; c. recovering fine particles of char having an average particle diameter less than about 25% of that of said coal from said product gas; and d. mixing said char particles recovered from said product gas stream with particles of coal to be fed into said fluidized bed gasification zone at a temperature below the softening point of said coal.
Claim 9
Dependent Claim
133 words
A process for the gasification of a bituminous coal which comprises: a. introducing at a temperature below the softening point of said coal a mixture of particles of said coal and fine char having an average particle diameter less than about 25% of that of said coal particles in a weight ratio between about 0.1:1 and about 5:1 into a fluidized bed gasification zone; b. withdrawing a product gas overhead from said fluidized bed; c. recovering fine particles of char having an average particle diameter less than about 25% of that of said coal from said product gas; and d. mixing said char particles recovered from said product gas stream with particles of coal to be fed into said fluidized bed gasification zone at a temperature below the softening point of said coal.
Claim 10
Dependent Claim
28 words
A process as defined by claim 7 wherein said fine particles of char are mixed with said coal in a weight ratio between about 0.5:1 and about 3:1.
Claim 11
Dependent Claim
130 words
A process as defined by claim 7 including the additional steps of: circulating a stream of solid char particles continuously between said fluidized bed gasification zone and a combustion zone; introducing an oxygen-containing gas into said combustion zone in a quantity sufficient to burn a portion of the carbon present in said char particles and raise the temperature of said char particles to a predetermined level; withdrawing flue gas overhead of said combustion zone; recovering fine particles of char having an average particle diameter less than about 25% of that of said coal from said flue gas; and mixing char particles recovered from said flue gas stream with particles of coal to be fed into said fluidized bed gasification zone at a temperature below the softening point of said coal.
Claim 12
Dependent Claim
28 words
A process as defined by claim 9 wherein at least part of said fine particles of char recovered from said flue gas is returned to said combustion zone.
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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) | 1979-01-12 | 1979-07-14 | 1980-01-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-01-12 | 1983-07-14 | 1984-01-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-01-12 | 1987-07-14 | 1988-01-13 | $7700.00 | Window Closed / Lapsed |