US4278446A
Expired / Lapsed
US
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Very-high-velocity entrained-bed gasification of coal
Assignee: Avco Corp
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Filing: 1979-05-31
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Granted: 1981-07-14
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Expires: 1999-05-31
Abstract
Abstract A process and apparatus for gasification of carbonaceous matter, preferably coal, is disclosed. A stream of previously produced char, preferably produced from coal, or other fuel together with an oxidizer and steam is introduced into a first or combustion stage. The combustion gas produced by the combustion passes into a second or gasification stage and through a nozzle at at least sonic velocity. Pulverized carbonaceous matter, preferably coal, is introduced and dispersed in the combustion gas in the gasification stage. The temperature, velocity and velocity changes principally of the gas in the gasification stage are controlled to provide a heating rate for the particles of pulverized carbonaceous matter of at least about 10 5 degrees Kelvin per second, and to effect rapid removal of volatile components from the immediate vicinity of the particles. Upon substantial gasification of the particles in the gasification stage, the resultant product stream may be quenched, the char removed, and preferably at least a portion thereof introduced into the combustion stage.
Inventors
- 👤 Charles W. von Rosenberg, Jr.
- 👤 David B. Stickler
- 👤 Richard E. Gannon
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 01:41
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/72; C10J3/78; C10J3/82; C10J3/84; C10J3/845; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/0916; C10J2300/092; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1807; C10J2300/1846; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y10; Y10S; Y10S48/00; Y10S48/04
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
255 words
A process for the gasification of solid carbonaceous fuel comprising: (a) combusting carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a gasification stage having a nozzle through which said combustion gas and steam flow at at least sonic velocity; (d) introducing and dispersing finely-divided solid carbonaceous fuel comprising particles in said combustion gas at said nozzle; (e) selectably controlling characteristics of said flow of said combustion gas and steam containing said dispersed solid fuel to provide relative movement of said particles of said fuel with respect to said combustion gas and stream by using the inertia of said particles and a plurality of accelerations and decelerations of said combustion gas and steam, provided by at least one shock wave and expansion in said flow, said combustion gas and steam having an initial temperature and said selected flow characteristics providing sufficient relative movement to provide an average heating rate of said fuel of at least about 10 5 degrees Kelvin per second whereby said fuel is partially gasified and reduced to char and a product gas is formed; (f) withdrawing from said gasification stage a product stream comprising said char and product gas; (g) separating said char from said product stream; and (h) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.
Claim 2
Dependent Claim
255 words
A process for the gasification of solid carbonaceous fuel comprising: (a) combusting carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a gasification stage having a nozzle through which said combustion gas and steam flow at at least sonic velocity; (d) introducing and dispersing finely-divided solid carbonaceous fuel comprising particles in said combustion gas at said nozzle; (e) selectably controlling characteristics of said flow of said combustion gas and steam containing said dispersed solid fuel to provide relative movement of said particles of said fuel with respect to said combustion gas and stream by using the inertia of said particles and a plurality of accelerations and decelerations of said combustion gas and steam, provided by at least one shock wave and expansion in said flow, said combustion gas and steam having an initial temperature and said selected flow characteristics providing sufficient relative movement to provide an average heating rate of said fuel of at least about 10 5 degrees Kelvin per second whereby said fuel is partially gasified and reduced to char and a product gas is formed; (f) withdrawing from said gasification stage a product stream comprising said char and product gas; (g) separating said char from said product stream; and (h) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.
Claim 3
Dependent Claim
31 words
The process as set forth in claim 1 wherein a larger fraction of the fuel is volatilized than the volatile matter content of said fuel as defined by ASTM proximate analysis.
Claim 4
Dependent Claim
29 words
The process as set forth in claim 1 wherein said product stream drops in temperature at a rate sufficient to substantially prevent attaining equilibrium among the gas stream constituents.
Claim 5
Dependent Claim
33 words
The process as set forth in claim 3 wherein the cooled gas stream contains methane and the methane content of said cooled gas stream is larger than would be predicated by equilibrium considerations.
Claim 6
Dependent Claim
46 words
The process as set forth in claim 2 wherein said nozzle has a convergent inlet portion, a throat portion, and a divergent outlet portion; and the velocity of said products of combustion and steam increases concomitant with a decrease in temperature in said nozzle outlet portion.
Claim 7
Dependent Claim
18 words
The process as set forth in claim 5 wherein said fuel is introduced at said nozzle inlet portion.
Claim 8
Dependent Claim
18 words
The process as set forth in claim 5 wherein said fuel is introduced at said nozzle outlet portion.
Claim 9
Dependent Claim
31 words
The process as set forth in claim 1 wherein said carbonaceous matter comprises at least in part said separated char and said char is substantially completely combusted in said combustion zone.
Claim 10
Dependent Claim
28 words
The process as set forth in claim 1 wherein said products of combustion and steam are introduced into said gasification zone at a temperature above about 1900° K.
Claim 11
Dependent Claim
47 words
The process as set forth in claim 1 wherein said solid carbonaceous fuel is substantially uniformly introduced into said combustion gas and steam at said nozzle and in a direction at least substantially across the direction of flow of said combustion gas and steam through said nozzle.
Claim 12
Dependent Claim
85 words
The process as set forth in claim 10 wherein the velocity of said combustion gas and steam is controlled to provide a difference in the velocity of said combustion gas and steam and the velocity of said solid carbonaceous fuel whereby as the particles comprising said solid carbonaceous fuel flow through said gasification stage and are gasified to form said product gas, said combustion gas and steam substantially continuously rapidly carries away from said particles of solid carbonaceous fuel the products of the gasification thereof.
Claim 13
Dependent Claim
38 words
The process as set forth in claim 11 wherein a shock wave is caused to occur in said gasification stage downstream of said nozzle after substantially complete mixing of said combustion gas and steam and solid carbonaceous fuel.
Claim 14
Dependent Claim
52 words
The process as set forth in claim 12 which includes cooling the product stream withdrawn from said gasification stage to a temperature below that at which steam will substantially react with said product gas, said cooling being at a rate sufficient to substantially prevent the formation of soot in said product stream.
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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) | 1984-07-13 | 1985-01-12 | 1985-07-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-07-13 | 1989-01-12 | 1989-07-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-07-13 | 1993-01-12 | 1993-07-14 | $7700.00 | Window Closed / Lapsed |