US3963598A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Flash hydrogenation of coal
Assignee: Energy Research and Development Administration ERDA
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Filing: 1974-10-15
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Granted: 1976-06-15
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Expires: 1994-10-15
Abstract
Abstract A process for the hydrogenation of coal comprising the contacting of powdered coal with hydrogen in a rotating fluidized bed reactor. A rotating fluidized bed reactor suitable for use in this process is also disclosed. The coal residence time in the reactor is limited to less than 5 seconds while the hydrogen contact time is not in excess of 0.2 seconds.
Inventors
- 👤 Bernard Manowitz
- 👤 Meyer Steinberg
- 👤 Thomas V. Sheehan
- 👤 Warren E. Winsche
- 👤 Chad J. Raseman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 09:46
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/38; B01J8/382; B01J19/00; B01J19/28; C; C10; C10G; C10G1/00; C10G1/06; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00105; B01J2219/00108; B01J2219/19; B01J2219/194; B01J2219/1941; B01J2219/1942
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
108 words
A process for the hydrogenation of coal to maximize the production of liquid hydrocarbons, comprising contacting in a rotating fluidized bed substantially dry powdered coal having a particle size in the range of about 50-500 microns with hydrogen gas at temperatures to produce a reaction temperature between about 500° C and 800° C, at a pressure in the range of about 68 to 280 atmospheres for a coal residence time of not in excess of five seconds and hydrogen contact time not in excess of 0.2 sec to produce liquid hydrocarbons, followed by rapid cooling to a temperature sufficiently low to prevent further cracking of the liquid products.
Claim 2
Dependent Claim
108 words
A process for the hydrogenation of coal to maximize the production of liquid hydrocarbons, comprising contacting in a rotating fluidized bed substantially dry powdered coal having a particle size in the range of about 50-500 microns with hydrogen gas at temperatures to produce a reaction temperature between about 500° C and 800° C, at a pressure in the range of about 68 to 280 atmospheres for a coal residence time of not in excess of five seconds and hydrogen contact time not in excess of 0.2 sec to produce liquid hydrocarbons, followed by rapid cooling to a temperature sufficiently low to prevent further cracking of the liquid products.
Claim 3
Dependent Claim
42 words
The process of claim 1 in which said powdered coal is fluidized with said hydrogen gas and supplied to said rotating fluidized bed and excess from said fluidized bed including the reaction products, ash, char and recycle hydrogen gas are carried off.
Claim 4
Dependent Claim
60 words
The process of claim 2 in which the incoming powdered coal is fluidized with said hydrogen gas below the reaction temperature, said bed being supplied directly with hydrogen at a sufficient temperature to conduct the aforesaid reaction, said directly supplied hydrogen maintaining the overall fluidization of said bed and furnishing the majority of the heat required to heat the coal.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-15 | 1979-12-15 | 1980-06-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-15 | 1983-12-15 | 1984-06-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-15 | 1987-12-15 | 1988-06-15 | $7700.00 | Window Closed / Lapsed |