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US4040957A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of insoluble material from coal liquefaction product by use of a diluent

Assignee: Lummus Technology LLC
•
Filing: 1976-02-20
•
Granted: 1977-08-09
•
Expires: 1996-02-20
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Abstract

Abstract Insoluble materials are separated from a coal liquefaction product having a quinoline insoluble content of greater than 15 wt. % by diluting the product with a diluent which is a solvent for the components which are quinoline soluble and benzene insoluble, with the diluent being added in an amount to provide a mixture having a quinoline insoluble content of no greater than 13 wt. %. Insoluble material is then separated by gravity settling in the presence of a promoter liquid having a 5 volume percent distillation temperature of at least 250° F and a 95 volume percent distillation temperature of at least 350° F and no greater than 750° F, with the promoter liquid having a characterization factor of at least 9.75.

Inventors

  • 👤 Morgan C. Sze
  • 👤 George J. Snell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 19:44
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/045

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 217 words
A process for separating insoluble material from a coal liquefaction product produced from a coal feed and comprised of insoluble material and carbonaceous matter dissolved in a coal liquefaction solvent, said coal liquefaction product having quinoline insolubles of at least 15 wt. %, comprising: diluting said coal liquefaction product with a liquid diluent, said liquid diluent being a solvent for the quinoline soluble and benzene insoluble components in said coal liquefaction product and a nonsolvent for quinoline insoluble components and being added in an amount to provide a mixture of coal liquefaction product and diluent having quinoline insolubles of no greater than 13 wt.%; mixing the diluted coal liquefaction product with a liquid promoter, said liquid promoter being different from said diluent and having a 5 volume percent distillation temperature of at least about 250° F. and a 95 volume percent distillation temperature of at least about 350° F. and no greater than about 750° F., said promoter liquid having a characterization factor (K) of at least 9.75, said liquid promoter having a characterization factor greater than said coal liquefaction solvent; and separating insoluble material from said diluted coal liquefaction product mixed with liquid promoter by gravity settling to thereby recover a liquid overflow essentially free of insoluble material and a liquid underflow containing the insoluble material.
Claim 2
Dependent Claim 217 words
A process for separating insoluble material from a coal liquefaction product produced from a coal feed and comprised of insoluble material and carbonaceous matter dissolved in a coal liquefaction solvent, said coal liquefaction product having quinoline insolubles of at least 15 wt. %, comprising: diluting said coal liquefaction product with a liquid diluent, said liquid diluent being a solvent for the quinoline soluble and benzene insoluble components in said coal liquefaction product and a nonsolvent for quinoline insoluble components and being added in an amount to provide a mixture of coal liquefaction product and diluent having quinoline insolubles of no greater than 13 wt.%; mixing the diluted coal liquefaction product with a liquid promoter, said liquid promoter being different from said diluent and having a 5 volume percent distillation temperature of at least about 250° F. and a 95 volume percent distillation temperature of at least about 350° F. and no greater than about 750° F., said promoter liquid having a characterization factor (K) of at least 9.75, said liquid promoter having a characterization factor greater than said coal liquefaction solvent; and separating insoluble material from said diluted coal liquefaction product mixed with liquid promoter by gravity settling to thereby recover a liquid overflow essentially free of insoluble material and a liquid underflow containing the insoluble material.
Claim 3
Dependent Claim 23 words
The process of claim 1 wherein the mixture of coal liquefaction product and diluent has quinoline insolubles of no greater than 10 wt.%.
Claim 4
Dependent Claim 13 words
The process of claim 2 wherein the diluent is a heterocyclic nitrogen compound.
Claim 5
Dependent Claim 28 words
The process of claim 2 wherein the diluent is selected from the group consisting of polynuclear aromatic and hydroaromatic compounds having at least three rings and mixtures thereof.
Claim 6
Dependent Claim 14 words
The process of claim 4 wherein the diluent is derived from the coal product.
Claim 7
Dependent Claim 11 words
The process of claim 2 wherein the diluent is a phenol.

References Cited (Backward Citations)

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US3120474A Cited
US3162594A Cited
US3519553A Cited
US3678837A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-08 1981-02-07 1981-08-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-08 1985-02-07 1985-08-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-08 1989-02-07 1989-08-09 $7700.00 Window Closed / Lapsed

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