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US4344838A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal conversion catalysts

Assignee: Mobil Oil AS
•
Filing: 1981-04-20
•
Granted: 1982-08-17
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Expires: 2001-04-20
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Abstract

Abstract A solvent extraction process for coal conversion wherein coal liquids are contacted with spent petroleum hydrogenation catalyst or spent demetallizing guard chamber adsorbent.

Inventors

  • 👤 Thomas O. Mitchell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 09:25
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/006; C10G1/08; C10G1/086

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 124 words
In a solvent extraction process for coal conversion wherein coal is slurried in an organic solvent and heated to a temperature sufficient to dissolve or liquefy most of the coal, the resulting coal liquefaction product is upgraded by catalytic hydrogenation, and a process-derived recycle solvent is hydrogenated and returned to the initial dissolution stage; the improvement which comprises contacting materials selected from the group consisting of said coal liquefaction product, and said process-derived recycle solvent with a catalyst selected from the group consisting of: (1) spent hydrogenation catalyst from processes for the hydrogenation of hydrocarbons selected from the group consisting of petroleum, petroleum-derived liquids, Fischer-Tropsch liquids, and shale oils; (2) spent adsorbent from guard chambers used to demetallize said hydrocarbons; and (3) mixtures thereof.
Claim 2
Dependent Claim 124 words
In a solvent extraction process for coal conversion wherein coal is slurried in an organic solvent and heated to a temperature sufficient to dissolve or liquefy most of the coal, the resulting coal liquefaction product is upgraded by catalytic hydrogenation, and a process-derived recycle solvent is hydrogenated and returned to the initial dissolution stage; the improvement which comprises contacting materials selected from the group consisting of said coal liquefaction product, and said process-derived recycle solvent with a catalyst selected from the group consisting of: (1) spent hydrogenation catalyst from processes for the hydrogenation of hydrocarbons selected from the group consisting of petroleum, petroleum-derived liquids, Fischer-Tropsch liquids, and shale oils; (2) spent adsorbent from guard chambers used to demetallize said hydrocarbons; and (3) mixtures thereof.
Claim 3
Dependent Claim 22 words
The process of claim 1 wherein said catalyst further comprises alumina having metals, oxides, or sulfides of iron or nickel deposited thereon.
Claim 4
Dependent Claim 24 words
The process of claim 1 wherein said catalyst further comprises a crystalline aluminosilicate having metals, oxides, or sulfides of iron or nickel deposited thereon.
Claim 5
Dependent Claim 22 words
The process of claim 1 wherein said catalyst is spent hydrogenation catalyst from processes for the hydrogenation of petroleum or petroleum-derived liquids.

References Cited (Backward Citations)

US3162594A Cited
US3232861A Cited
US3488279A Cited
US3549512A Cited
US3527691A Cited
US4303497A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-08-16 1986-02-15 1986-08-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-08-16 1990-02-15 1990-08-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-08-16 1994-02-15 1994-08-17 $7700.00 Window Closed / Lapsed

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