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US4264428A Expired / Lapsed US ⏱️ 0.0 years remaining

Conversion of coal into liquid fuels

Assignee: Mobil Oil AS
•
Filing: 1979-12-13
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Granted: 1981-04-28
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Expires: 1999-12-13
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Abstract

Abstract This invention provides an improved process for deriving liquid fuels from coal which involves the steps of (1) solubilizing coal in a FCC residual oil to form a solvated coal solution phase and an ash solids phase; (2) subject the two phase admixtureto FCC conversion conditions; (3) separating and recovering a hydrocarbon phase and a catalyst-ash solids phase in a catalyst-ash solids phase; (4) treating the catalyst-ash solids phase in a catalyst regeneration zone, and removing entrained ash solids from the flue gas effluent of the catalyst regeneration zone; and (5) fractioning the hydrocarbon phase to recover liquid fuel products.

Inventors

  • 👤 Hans-Juergen Schoennagel
  • 👤 John C. Zahner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 06:14
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; C10G1/00; C10G1/002

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 218 words
In a process for preparation of liquid fuels from coal by solvation of comminuted coal in a liquid hydrocarbon solvent derived in the process as hereinafter defined and in the presence of hydrogen, subjecting products from said solvation step to fluidized catalytic cracking with a solid cracking catalyst whereby an inactivating carbonaceous deposit is laid down on the catalyst, separating cracked hydrocarbon products from catalyst so inactivated, regenerating said separated inactivated catalyst by fluidizing the same in air to burn the said carbonaceous deposit, separating flue gas resultant from said burning, returning the so regenerated catalyst to the fluidized catalytic cracking step, fractionating said cracked hydrocarbon products to provide a bottoms fraction which is a thermally stable, highly polycyclic aromatic residual oil, transferring said residual oil to said solvation step as the liquid hydrocarbon solvent therein and separating ash derived from said coal from hydrocarbons during the said process; the improvement in separating ash from hydrocarbons which comprises subjecting said solvation products admixed with ash derived in said solvation step to fluidized catalytic cracking as aforesaid, separating the said ash admixed with inactivated catalyst from cracked hydrocarbon products, subjecting the mixture of ash and inactivated catalyst to said regeneration step, removing ash from said regeneration step with said flue gas, and separating said ash from said flue gas.
Claim 2
Dependent Claim 218 words
In a process for preparation of liquid fuels from coal by solvation of comminuted coal in a liquid hydrocarbon solvent derived in the process as hereinafter defined and in the presence of hydrogen, subjecting products from said solvation step to fluidized catalytic cracking with a solid cracking catalyst whereby an inactivating carbonaceous deposit is laid down on the catalyst, separating cracked hydrocarbon products from catalyst so inactivated, regenerating said separated inactivated catalyst by fluidizing the same in air to burn the said carbonaceous deposit, separating flue gas resultant from said burning, returning the so regenerated catalyst to the fluidized catalytic cracking step, fractionating said cracked hydrocarbon products to provide a bottoms fraction which is a thermally stable, highly polycyclic aromatic residual oil, transferring said residual oil to said solvation step as the liquid hydrocarbon solvent therein and separating ash derived from said coal from hydrocarbons during the said process; the improvement in separating ash from hydrocarbons which comprises subjecting said solvation products admixed with ash derived in said solvation step to fluidized catalytic cracking as aforesaid, separating the said ash admixed with inactivated catalyst from cracked hydrocarbon products, subjecting the mixture of ash and inactivated catalyst to said regeneration step, removing ash from said regeneration step with said flue gas, and separating said ash from said flue gas.
Claim 3
Dependent Claim 55 words
The process of claim 1 wherein a gas oil is cracked in a fluidized catalytic cracking step apart from cracking of said products from the solvation step and the products of cracking said gas oil are mixed with said cracked hydrocarbon from said cracking of said products of said solvation step for fractionation as aforesaid.

References Cited (Backward Citations)

US3974062A Cited
US4035281A Cited
US4108758A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-04-27 1984-10-27 1985-04-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-04-27 1988-10-27 1989-04-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-04-27 1992-10-27 1993-04-28 $7700.00 Window Closed / Lapsed

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