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US4303496A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal liquefaction process

Assignee: Mobil Oil AS
•
Filing: 1980-08-14
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Granted: 1981-12-01
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Expires: 2000-08-14
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Abstract

Abstract The invention is directed to undertaking the liquefaction of coal in the presence of lignin.

Inventors

  • 👤 Leslie R. Rudnick

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 19:58
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/042; C10G1/06; C10G1/065; C10G1/08; C10G1/083

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 114 words
A process for the liquefaction of coal comprising admixing the coal to be subjected to liquefaction with lignin wherein the amount of lignin ranges from about 0.01 to about 1% based on the weight of the coal; introducing the mixture of coal and lignin to a dissolver wherein said mixture is subjected to elevated temperature and elevated pressure for a period of time ranging from 0.5 to 180 minutes wherein said elevated temperature ranges from about 600° F. to about 1000° F. and wherein said elevated pressure ranges from about 50 to about 3000 psig; and separating light hydrocarbon fractions from a mixture of ash, undissolved coal, deashed coal and high quality coal extracts.
Claim 2
Dependent Claim 114 words
A process for the liquefaction of coal comprising admixing the coal to be subjected to liquefaction with lignin wherein the amount of lignin ranges from about 0.01 to about 1% based on the weight of the coal; introducing the mixture of coal and lignin to a dissolver wherein said mixture is subjected to elevated temperature and elevated pressure for a period of time ranging from 0.5 to 180 minutes wherein said elevated temperature ranges from about 600° F. to about 1000° F. and wherein said elevated pressure ranges from about 50 to about 3000 psig; and separating light hydrocarbon fractions from a mixture of ash, undissolved coal, deashed coal and high quality coal extracts.
Claim 3
Dependent Claim 21 words
The process of claim 1, wherein said mixture is subjected to elevated temperature and elevated pressure in the presence of hydrogen.
Claim 4
Dependent Claim 19 words
The process of claim 1, wherein the mixture contains a source of phenanthrene, dihydrophenanthrene, tetralins, hydropyrenes or mixtures thereof.
Claim 5
Dependent Claim 27 words
The process of claim 1, wherein the mixture contains a high quality coal extract, obtained by recycling at least a portion of the high quality coal extracts.
Claim 6
Dependent Claim 23 words
The process of claim 1, wherein the mixture consists essentially of said coal and said lignin and is free of a liquefaction catalyst.
Claim 7
Dependent Claim 17 words
The process of claim 1, wherein a liquefaction catalyst is added to the mixture in the dissolver.
Claim 8
Dependent Claim 11 words
The process of claim 6, wherein said catalyst is cobalt molybdate.
Claim 9
Dependent Claim 15 words
The process of claim 1, wherein the light hydrocarbon fractions are recycled into the dissolver.

References Cited (Backward Citations)

GB173907A Cited
US2591496A Cited
US4247384A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-11-30 1985-06-01 1985-12-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-11-30 1989-06-01 1989-12-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-11-30 1993-06-01 1993-12-01 $7700.00 Window Closed / Lapsed

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