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US4081358A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the liquefaction of coal and separation of solids from the liquid product

Assignee: Honeywell UOP LLC
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Filing: 1976-12-29
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Granted: 1978-03-28
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Expires: 1996-12-29
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Abstract

Abstract Production of a low mineral content fuel by a coal liquefaction process utilizing a hydrogenated coal solvent having been hydrogenated to remove at least about 80% of the asphaltenes which yields as the primary product a mixture of liquid and solids, a part of which is suspended in the liquid. The suspended solids are effectively removed with minimum loss of desired product by means of a light aromatic solvent in combination with a hydrogenated coal solvent having been hydrogenated to remove at least about 80% of the asphaltenes with a weight ratio of unreacted coal oil solvent to light aromatic solvent of from about 0.1 to about 1000.

Inventors

  • 👤 Gim Tan
  • 👤 John G. Gatsis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 16:49
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/045; C10G1/002; C10G1/006

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 272 words
A process for producing hydrocarbonaceous liquid products from coal which comprises the steps of: (a) contacting the coal, at a temperature of from about 150° C. to about 450° C. and a pressure of from about 10 to about 300 atmospheres with a hydrogenated coal oil solvent having been hydrogenated to remove at least about 80% of the asphaltenes and hydrogen; (b) separating gas from the resultant mixture to provide a liquid phase comprising coal extract, a partially spent coal oil solvent and finely divided solid particles; (c) supplying said liquid phase, including substantially all of said partially spent coal oil solvent, to a pre-mix zone and therein commingling the same with from about 10 weight percent to about 1000 weight percent of a light aromatic solvent selected from the group consisting of benzene, toluene and xylene at a temperature of from about 10° C. to about 150° C., a pressure of from about atmospheric to about 25 atmospheres and a weight ratio of unreacted coal oil solvent to light aromatic solvent of from about 0.1 to about 1000; (d) introducing the mixture from the pre-mix zone to a separation zone and therein separating a solid ash from the admixed liquids; (e) thereafter removing said light aromatic solvent from said admixed liquids in a solvent recovery zone; (f) removing an ash-free hydrocarbon stream from said solvent recovery zone and hydrogenating at least a portion thereof to form a hydrogenated coal oil with at least 80% of the asphaltenes removed therefrom; and (g) supplying at least a portion of said hydrogenated coal oil to step (a) as said asphaltene-free hydrogenated coal oil solvent.
Claim 2
Dependent Claim 272 words
A process for producing hydrocarbonaceous liquid products from coal which comprises the steps of: (a) contacting the coal, at a temperature of from about 150° C. to about 450° C. and a pressure of from about 10 to about 300 atmospheres with a hydrogenated coal oil solvent having been hydrogenated to remove at least about 80% of the asphaltenes and hydrogen; (b) separating gas from the resultant mixture to provide a liquid phase comprising coal extract, a partially spent coal oil solvent and finely divided solid particles; (c) supplying said liquid phase, including substantially all of said partially spent coal oil solvent, to a pre-mix zone and therein commingling the same with from about 10 weight percent to about 1000 weight percent of a light aromatic solvent selected from the group consisting of benzene, toluene and xylene at a temperature of from about 10° C. to about 150° C., a pressure of from about atmospheric to about 25 atmospheres and a weight ratio of unreacted coal oil solvent to light aromatic solvent of from about 0.1 to about 1000; (d) introducing the mixture from the pre-mix zone to a separation zone and therein separating a solid ash from the admixed liquids; (e) thereafter removing said light aromatic solvent from said admixed liquids in a solvent recovery zone; (f) removing an ash-free hydrocarbon stream from said solvent recovery zone and hydrogenating at least a portion thereof to form a hydrogenated coal oil with at least 80% of the asphaltenes removed therefrom; and (g) supplying at least a portion of said hydrogenated coal oil to step (a) as said asphaltene-free hydrogenated coal oil solvent.
Claim 3
Dependent Claim 24 words
The process of claim 1 further characterized in that the light aromatic solvent from said solvent recovery zone is introduced to said pre-mix zone.
Claim 4
Dependent Claim 15 words
The process of claim 1 further characterized in that said light aromatic solvent is benzene.
Claim 5
Dependent Claim 15 words
The process of claim 1 further characterized in that said light aromatic solvent is toluene.
Claim 6
Dependent Claim 15 words
The process of claim 1 further characterized in that said light aromatic solvent is xylene.

References Cited (Backward Citations)

US2476999A Cited
US3505203A Cited
US3598718A Cited
US3607716A Cited
US3607718A Cited
US3997425A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-03-27 1981-09-26 1982-03-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-03-27 1985-09-26 1986-03-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-03-27 1989-09-26 1990-03-28 $7700.00 Window Closed / Lapsed

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