US4018663A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Coal liquefaction process
Assignee: Energy Research and Development Administration ERDA
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Filing: 1976-01-05
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Granted: 1977-04-19
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Expires: 1996-01-05
Abstract
Abstract An improved coal liquefaction process is provided which enables conversion of a coal-oil slurry to a synthetic crude refinable to produce larger yields of gasoline and diesel oil. The process is characterized by a two-step operation applied to the slurry prior to catalytic desulfurization and hydrogenation in which the slurry undergoes partial hydrogenation to crack and hydrogenate asphaltenes and the partially hydrogenated slurry is filtered to remove minerals prior to subsequent catalytic hydrogenation.
Inventors
- 👤 Clarence Karr, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 11:37
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/002; F; F02; F02B; F02B3/00; F02B3/06
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
103 words
An improved liquefaction process comprising passing a liquid coal slurry containing suspended materials under a pressure of hydrogen of 1000-2000 psig and at a temperature in the range 400° to 450° C. through a first reactor containing a charge of porous inert inorganic nominally non-catalytic material having a sufficiently high pore size and surface area so as to promote at least partial hydrogenation of asphaltenes, passing the partially hydrogenated hydrogen-pressurized slurry to a second reactor to contact a charge of hydrogenation catalyst at a temperature in the range 350° to 400° C. and removing a liquid fuel from said second reactor as product.
Claim 2
Dependent Claim
103 words
An improved liquefaction process comprising passing a liquid coal slurry containing suspended materials under a pressure of hydrogen of 1000-2000 psig and at a temperature in the range 400° to 450° C. through a first reactor containing a charge of porous inert inorganic nominally non-catalytic material having a sufficiently high pore size and surface area so as to promote at least partial hydrogenation of asphaltenes, passing the partially hydrogenated hydrogen-pressurized slurry to a second reactor to contact a charge of hydrogenation catalyst at a temperature in the range 350° to 400° C. and removing a liquid fuel from said second reactor as product.
Claim 3
Dependent Claim
23 words
The process of claim 1 in which the partially hydrogenated coal slurry issuing from the first reactor is treated to remove mineral residues.
Claim 4
Dependent Claim
41 words
The method according to claim 1 in which the inorganic material charge in the first reactor is a material selected from the group consisting of alpha alumina, silica, and similar chemically inert solids, with high surface area and large pore size.
Claim 5
Dependent Claim
28 words
The process of claim 1 in which a portion of the liquid product issuing from the second reactor is recycled back to the said first or second reactor.
Claim 6
Dependent Claim
17 words
The method according to claim 1 in which the second reactor contains a desulfurization and denitrogenization catalyst.
Claim 7
Dependent Claim
37 words
The method according to claim 1 in which the porous inert nominally non-catalytic material has a pore size in the range 0.05 to 0.5 microns and a surface area in the range 1-5 square meters per gram.
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) | 1980-04-18 | 1980-10-18 | 1981-04-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-04-18 | 1984-10-18 | 1985-04-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-04-18 | 1988-10-18 | 1989-04-19 | $7700.00 | Window Closed / Lapsed |