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US4222848A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal liquefaction process employing extraneous minerals

Assignee: Chevron USA Inc
•
Filing: 1978-12-15
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Granted: 1980-09-16
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Expires: 1998-12-15
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Abstract

Abstract In a coal liquefaction process which includes a recycle of a product slurry which contain recycle mineral residue and recycle of extraneous catalytic material to said liquefication zone, hydrocracking of the hydrocarbonaceous material from the mineral residue occurs and a mixture of hydrocarbon gases, dissolved liquid, normally solid dissolved coal, suspended mineral residue and suspended extraneous catalytic mineral results. A first portion of said residue slurry is recycled to the liquefication zone, a second portion is passed to separation means and the third portion goes to a hydroclone. Overflow from the hydroclone goes to the liquefaction zone to reduce the median diameter of the particles recycled.

Inventors

  • 👤 Norman L. Carr
  • 👤 Bruce K. Schmid

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 16:00
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/083; C10G1/04; C10G1/045; C10G1/086

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 259 words
A coal liquefaction process comprising passing mineral-containing feed coal, hydrogen, recycle dissolved liquid solvent, recycle normally solid dissolved coal, recycle mineral residue derived from said feed coal and a recycle extraneous catalytic mineral to a coal liquefaction zone which does not contain a fixed bed of added catalyst to dissolve hydrocarbonaceous material from mineral residue and to hydrocrack said hydrocarbonaceous material to produce a mixture comprising hydrocarbon gases, dissolved liquid, normally solid dissolved coal, suspended mineral residue and suspended extraneous catalytic mineral; passing a liquefaction zone effluent stream through vapor-liquid separator means to remove overhead hydrogen, hydrocarbon gases and naphtha from a residue slurry comprising liquid coal and normally solid dissolved coal, suspended mineral residue and suspended particles of extraneous catalytic mineral; recycling a first portion of said residue slurry to said liquefaction zone; passing a second portion of said residue slurry to a product separation means; passing a third portion of said residue slurry through hydroclone means; recovering from said hydroclone means an overflow slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue and a higher than aliquot weight proportion of suspended particles of extraneous catalytic mineral; recycling said overflow slurry to said liquefaction zone to reduce the median diameter of particles recycled to said liquefaction zone and to selectively increase the proportion of said extraneous catalytic mineral in said liquefaction zone; recovering from said hydroclone means a concentrated solids underflow slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue; and passing said underflow slurry to said product separation means.
Claim 2
Dependent Claim 259 words
A coal liquefaction process comprising passing mineral-containing feed coal, hydrogen, recycle dissolved liquid solvent, recycle normally solid dissolved coal, recycle mineral residue derived from said feed coal and a recycle extraneous catalytic mineral to a coal liquefaction zone which does not contain a fixed bed of added catalyst to dissolve hydrocarbonaceous material from mineral residue and to hydrocrack said hydrocarbonaceous material to produce a mixture comprising hydrocarbon gases, dissolved liquid, normally solid dissolved coal, suspended mineral residue and suspended extraneous catalytic mineral; passing a liquefaction zone effluent stream through vapor-liquid separator means to remove overhead hydrogen, hydrocarbon gases and naphtha from a residue slurry comprising liquid coal and normally solid dissolved coal, suspended mineral residue and suspended particles of extraneous catalytic mineral; recycling a first portion of said residue slurry to said liquefaction zone; passing a second portion of said residue slurry to a product separation means; passing a third portion of said residue slurry through hydroclone means; recovering from said hydroclone means an overflow slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue and a higher than aliquot weight proportion of suspended particles of extraneous catalytic mineral; recycling said overflow slurry to said liquefaction zone to reduce the median diameter of particles recycled to said liquefaction zone and to selectively increase the proportion of said extraneous catalytic mineral in said liquefaction zone; recovering from said hydroclone means a concentrated solids underflow slurry comprising liquid coal and normally solid dissolved coal with suspended mineral residue; and passing said underflow slurry to said product separation means.
Claim 3
Dependent Claim 21 words
The process of claim 1 wherein said extraneous catalytic mineral is derived from pyrite obtained by water washing of a coal.
Claim 4
Dependent Claim 14 words
The process of claim 1 wherein said extraneous catalytic mineral is an iron compound.
Claim 5
Dependent Claim 42 words
The process of claim 1 wherein said extraneous catalytic mineral is added to said process in the form of particles having a median particle diameter which is larger than the median diameter of the particles in said first portion of residue slurry.
Claim 6
Dependent Claim 41 words
The process of claim 1 wherein said extraneous catalytic mineral is added to said process in the form of particles having a median diameter which is smaller than the median diameter of the particles in said first portion of residue slurry.
Claim 7
Dependent Claim 43 words
The process of claim 1 wherein said extraneous catalytic mineral is added to said process in the form of particles having a median diameter which is about the same as the median diameter of the particles in said first portion of residue slurry.
Claim 8
Dependent Claim 30 words
The process of claim 1 wherein said extraneous catalytic mineral has a superior catalytic activity as compared to a similar weight of recycle mineral residue derived from the feed coal.
Claim 9
Dependent Claim 25 words
The process of claim 1 wherein said third portion of residue slurry comprises between about 10 and 75 weight percent of the total residue slurry.
Claim 10
Dependent Claim 18 words
The process of claim 1 wherein said residue slurry contains between about 5 and 40 weight percent solids.
Claim 11
Dependent Claim 18 words
The process of claim 1 wherein said overflow slurry contains between about 0.2 and 20 weight percent solids.
Claim 12
Dependent Claim 23 words
The process of claim 1 wherein the median diameter of the solids in said overflow slurry is between about 0.5 and 5 microns.
Claim 13
Dependent Claim 24 words
The process of claim 1 wherein said feed coal contains at least about 15 weight percent of inorganic mineral matter on a dry basis.
Claim 14
Dependent Claim 24 words
The process of claim 1 wherein said feed coal contains at least about 20 weight percent of inorganic mineral matter on a dry basis.
Claim 15
Dependent Claim 24 words
The process of claim 1 wherein said extraneous catalytic mineral includes a metal selected from the group comprising Group VI and Group VIII metals.

References Cited (Backward Citations)

US3540995A Cited
US3962070A Cited
US3884796A Cited
US4090943A Cited
US4102775A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-09-16 1984-03-17 1984-09-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-09-16 1988-03-17 1988-09-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-09-16 1992-03-17 1992-09-16 $7700.00 Window Closed / Lapsed

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