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US4400181A
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Method for using fast fluidized bed dry bottom coal gasification
Assignee: United States Department of Energy
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Filing: 1982-01-28
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Granted: 1983-08-23
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Expires: 2002-01-28
Abstract
Abstract Carbonaceous solid material such as coal is gasified in a fast fluidized bed gasification system utilizing dual fluidized beds of hot char. The coal in particulate form is introduced along with oxygen-containing gas and steam into the fast fluidized bed gasification zone of a gasifier assembly wherein the upward superficial gas velocity exceeds about 5.0 ft/sec and temperature is 1500 DEG -1850 DEG F. The resulting effluent gas and substantial char are passed through a primary cyclone separator, from which char solids are returned to the fluidized bed. Gas from the primary cyclone separator is passed to a secondary cyclone separator, from which remaining fine char solids are returned through an injection nozzle together with additional steam and oxygen-containing gas to an oxidation zone located at the bottom of the gasifier, wherein the upward gas velocity ranges from about 3-15 ft/sec and is maintained at 1600 DEG -200 DEG F. temperature. This gasification arrangement provides for increased utilization of the secondary char material to produce higher overall carbon conversion and product yields in the process.
Inventors
- 👤 George J. Snell
- 👤 Paul H. Kydd
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 15:39
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/54; C10J3/56; C10J3/72; C10J3/74; C10J3/78; C10J2200/00; C10J2200/15; C10J2200/152; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0943; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1861; C10J2300/1884; C10J2300/1892
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
208 words
A process for gasifying particulate hydrocarbon feed materials to produce a fuel gas product, having low-to-medium heating value, comprising: (a) introducing the hydrocarbon feed material with steam and oxygen into a gasification zone containing a fast fluidized bed of char particles for gasification therein, said zone being maintained at temperature of 1500°-1850° F., at pressure exceeding about 30 psig, and at upward superficial gas velocity exceeding about 5 ft/sec to heat and gasify the feed and produce a gaseous material; (b) withdrawing said gaseous material along with char particles from the upper portion of the gasification zone and passing the materials to a primary gas-solids separation step for char solids removal; (c) withdrawing a first gas stream from said primary gas-solids separation step and returning particulate char solids to the gasification zone; (d) passing said first gas stream to a secondary gas-solids separation step and removing fine char solids therefrom; (e) returning the fine particulate char solids from the secondary gas-solids separation step to the lower end of a fluidized bed oxidation zone located immediately below the fast fluidized bed gasification zone; said oxidation zone having temperature maintained within the range of 1600°-2000° F.; and (f) withdrawing a fuel gas product stream from the secondary gas-solids separation step.
Claim 2
Dependent Claim
208 words
A process for gasifying particulate hydrocarbon feed materials to produce a fuel gas product, having low-to-medium heating value, comprising: (a) introducing the hydrocarbon feed material with steam and oxygen into a gasification zone containing a fast fluidized bed of char particles for gasification therein, said zone being maintained at temperature of 1500°-1850° F., at pressure exceeding about 30 psig, and at upward superficial gas velocity exceeding about 5 ft/sec to heat and gasify the feed and produce a gaseous material; (b) withdrawing said gaseous material along with char particles from the upper portion of the gasification zone and passing the materials to a primary gas-solids separation step for char solids removal; (c) withdrawing a first gas stream from said primary gas-solids separation step and returning particulate char solids to the gasification zone; (d) passing said first gas stream to a secondary gas-solids separation step and removing fine char solids therefrom; (e) returning the fine particulate char solids from the secondary gas-solids separation step to the lower end of a fluidized bed oxidation zone located immediately below the fast fluidized bed gasification zone; said oxidation zone having temperature maintained within the range of 1600°-2000° F.; and (f) withdrawing a fuel gas product stream from the secondary gas-solids separation step.
Claim 3
Dependent Claim
36 words
The process of claim 1, wherein the feed stream is introduced into the gasification zone through a shrouded injection nozzle, and the velocity in the solids injection nozzle is between about 6 and about 100 ft/sec.
Claim 4
Dependent Claim
26 words
The process of claim 1, wherein the feed is coal and the weight ratio of gasification zone char to coal is between about 20 and 30.
Claim 5
Dependent Claim
31 words
The process of claim 1, wherein the fine char solids from the secondary cyclone separator are returned to the oxidation zone through a gas shrouded nozzle together with an oxygen-containing gas.
Claim 6
Dependent Claim
31 words
The process of claim 1, wherein the gasification zone temperature is within the range of 1600°-1800° F., the pressure is 50-750 psig, and the upward superficial gas velocity is 6-20 ft/sec.
Claim 7
Dependent Claim
20 words
The process of claim 1, wherein the temperature of the oxidation zone is maintained within the range of 1650°-1950° F.
Claim 8
Dependent Claim
26 words
The process of claim 1, wherein the feed material is anthracite coal having particle size within the range of 0.040-0.004 inch (18-140 mesh U.S. Sieve Series).
Claim 9
Dependent Claim
47 words
The process of claim 4, wherein the secondary char solids are injected into the oxidation zone at a velocity within the range of 3-10 ft/sec and the shroud gas has exit velocity within the range of 20-80 ft/sec to provide a grinding effect on the char solids.
Claim 10
Dependent Claim
20 words
The process of claim 1, wherein the coarse ash particles are withdrawn from the lower portion of the oxidation zone.
Claim 11
Dependent Claim
219 words
A process for gasifying coal to produce a fuel gas product, having low-to-medium heating value, comprising: (a) introducing coal feed into a gasification zone containing a fast fluidized bed of char particles for gasification therein, said zone being maintained at 1500°-1850° F. temperature range, at pressure exceeding about 30 psig and at upward superficial gas velocity exceeding about 5 ft/sec, and a weight ratio of char to coal feed maintained between about 20 to 30 to heat and gasify the coal and produce a gaseous material; (b) withdrawing said gas and substantial char from the upper portion of the fast fluidized bed gasification zone and passing the materials to a primary gas-solids separation step for char solids removal; (c) withdrawing a first gas stream from said primary solids separation step and returning particulate char solids to the gasification zone; (d) passing said first gas stream to a secondary gas-solids separation step and removing a fine char solids therefrom; (e) returning the fine particulate char solids from the secondary gas-solids separation step through a gas shrouded nozzle into the lower end of a fluidized bed oxidation zone maintained at temperature within the range of 1600°-2000° F. and located immediately below the fast fluidized bed gasification zone; and (f) withdrawing a fuel gas product stream from the secondary gas-solids separation step.
Claim 12
Dependent Claim
219 words
A process for gasifying coal to produce a fuel gas product, having low-to-medium heating value, comprising: (a) introducing coal feed into a gasification zone containing a fast fluidized bed of char particles for gasification therein, said zone being maintained at 1500°-1850° F. temperature range, at pressure exceeding about 30 psig and at upward superficial gas velocity exceeding about 5 ft/sec, and a weight ratio of char to coal feed maintained between about 20 to 30 to heat and gasify the coal and produce a gaseous material; (b) withdrawing said gas and substantial char from the upper portion of the fast fluidized bed gasification zone and passing the materials to a primary gas-solids separation step for char solids removal; (c) withdrawing a first gas stream from said primary solids separation step and returning particulate char solids to the gasification zone; (d) passing said first gas stream to a secondary gas-solids separation step and removing a fine char solids therefrom; (e) returning the fine particulate char solids from the secondary gas-solids separation step through a gas shrouded nozzle into the lower end of a fluidized bed oxidation zone maintained at temperature within the range of 1600°-2000° F. and located immediately below the fast fluidized bed gasification zone; and (f) withdrawing a fuel gas product stream from the secondary gas-solids separation step.
Claim 13
Dependent Claim
19 words
The process of claim 10, wherein the percentage conversion of carbon in the coal exceeds about 50 W %.
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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) | 1986-08-22 | 1987-02-21 | 1987-08-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-08-22 | 1991-02-21 | 1991-08-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-08-22 | 1995-02-21 | 1995-08-23 | $7700.00 | Window Closed / Lapsed |