Patent US4075079A successfully refreshed from Google Patents.
US4075079A
Expired / Lapsed
US
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Process for the production of hydrocarbons from coal
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1976-06-09
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Granted: 1978-02-21
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Expires: 1996-06-09
Abstract
Abstract Coal is liquefied by treatment with a hydrogen-donor solvent and gaseous hydrogen, a heavy bottoms product boiling primarily in excess of about 1000 DEG F. is recovered, and this bottoms product is then pyrolyzed with fresh coal to produce surprisingly high yields of liquid product. The coke formed during the pyrolysis step may be gasified to generate hydrogen for use in the liquefaction operation and additional gas which can be employed as a fuel or upgraded for other uses.
Inventors
- 👤 Robert J. Lang
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 11:34
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/002; C10B; C10B55/00; C10B55/02
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
97 words
A process for the production of liquid hydrocarbons from carbonaceous solids containing volatilizable hydrocarbons which comprises contacting said carbonaceous solids with gaseous hydrogen and a hydrogen-donor solvent under coal liquefaction conditions in a liquefaction zone; recovering liquefaction products from said liquefaction zone; separating said liquefaction products into a gaseous stream, a liquid hydrocarbon stream, and a heavy liquefaction bottoms product; pyrolyzing said liquefaction bottoms product and fresh carbonaceous solids containing volatilizable hydrocarbons in a pyrolysis unti operated at a temperature in excess of about 900° F.; and recovering gases, liquid hydrocarbons, and coke from said pyrolysis unit.
Claim 2
Dependent Claim
97 words
A process for the production of liquid hydrocarbons from carbonaceous solids containing volatilizable hydrocarbons which comprises contacting said carbonaceous solids with gaseous hydrogen and a hydrogen-donor solvent under coal liquefaction conditions in a liquefaction zone; recovering liquefaction products from said liquefaction zone; separating said liquefaction products into a gaseous stream, a liquid hydrocarbon stream, and a heavy liquefaction bottoms product; pyrolyzing said liquefaction bottoms product and fresh carbonaceous solids containing volatilizable hydrocarbons in a pyrolysis unti operated at a temperature in excess of about 900° F.; and recovering gases, liquid hydrocarbons, and coke from said pyrolysis unit.
Claim 3
Dependent Claim
18 words
A process as defined by claim 1 wherein said carbonaceous solids comprise a bituminous or lower rank coal.
Claim 4
Dependent Claim
17 words
A process as defined by claim 1 wherein said pyrolysis unit comprises a fluidized bed coking unit.
Claim 5
Dependent Claim
43 words
A process as defined by claim 1 wherein said liquefaction bottoms product and said carbonaceous solids are pyrolyzed in said pyrolysis unit in a ratio of from about 0.3 to about 3 parts by weight of carbonaceous solids per part of liquefaction bottoms.
Claim 6
Dependent Claim
23 words
A process as defined by claim 1 wherein said pyrolysis unit is operated at a temperature between about 900° and about 1400° F.
Claim 7
Dependent Claim
28 words
A process as defined by claim 1 wherein about equal parts by weight of said liquefaction bottoms product and said carbonaceous solids are pyrolized in said pyrolysis unit.
Claim 8
Dependent Claim
38 words
A process as defined in claim 1 wherein coke recovered from said pyrolysis unit is fed to a fluidized bed gasification unit operated under coal gasification conditions and a raw product gas is recovered from said gasification unit.
Claim 9
Dependent Claim
38 words
A process as defined by claim 7 wherein at least part of said raw product gas recovered from said gasification unit is treated to increase its hydrogen content and the treated gas is recycled to said liquefaction zone.
Claim 10
Dependent Claim
30 words
A process as defined by claim 7 wherein said coke recovered from said pyrolysis unit is mixed with fresh carbonaceous solids containing volatilizable hydrocarbons and fed to said gasification unit.
Claim 11
Dependent Claim
28 words
A process as defined by claim 7 wherein said coke recovered from said pyrolysis unit is fed to said gasification unit in combination with an alkaline gasification catalyst.
Claim 12
Dependent Claim
46 words
A process for the production of liquid hydrocarbons which comprises pyrolyzing a mixture of finely-divided coal and a heavy coal liquefaction bottoms product produced by the liquefaction of coal in the presence of gaseous hydrogen and a hydrogen-donor solvent and recovering gases, hydrocarbon liquids, and coke.
Claim 13
Dependent Claim
46 words
A process for the production of liquid hydrocarbons which comprises pyrolyzing a mixture of finely-divided coal and a heavy coal liquefaction bottoms product produced by the liquefaction of coal in the presence of gaseous hydrogen and a hydrogen-donor solvent and recovering gases, hydrocarbon liquids, and coke.
References Cited (Backward Citations)
US3841991A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-02-20 | 1981-08-22 | 1982-02-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-02-20 | 1985-08-22 | 1986-02-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-02-20 | 1989-08-22 | 1990-02-21 | $7700.00 | Window Closed / Lapsed |