← Back to Patent Explorer
US4250014A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal liquefaction process

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1978-08-21
•
Granted: 1981-02-10
•
Expires: 1998-08-21
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Particulate coal is contacted with a vapor phase hydrogen donor solvent to swell the coal particles and, thereafter, the swollen coal particles are subjected to coal liquefaction conditions in the presence of a liquid phase solvent.

Inventors

  • 👤 Robert B. Long
  • 👤 Martin L. Gorbaty
  • 👤 Lonnie W. Vernon

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 05:08
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/006; C10G1/04; C10G1/042; C10G1/06; C10G1/065; Y; Y10; Y10S; Y10S208/00; Y10S208/951

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 116 words
In a coal liquefaction process wherein the particulate coal is converted to a hydrocarbonaceous oil in the presence of a liquid phase solvent, in a coal liquefaction zone, at coal liquefaction conditions, the improvement which comprises: (a) contacting said particulate coal with a vapor phase hydrogen donor solvent at a temperature ranging from about 150° to about 350° C. and at a pressure ranging from about 0 to about 150 psig, for a time sufficient for said coal to sorb at least a portion of said vapor phase solvent and thereby swell, and increase in weight by at least about 3 weight percent, and (b) subsequently subjecting the resulting swollen coal to said coal liquefaction conditions.
Claim 2
Dependent Claim 116 words
In a coal liquefaction process wherein the particulate coal is converted to a hydrocarbonaceous oil in the presence of a liquid phase solvent, in a coal liquefaction zone, at coal liquefaction conditions, the improvement which comprises: (a) contacting said particulate coal with a vapor phase hydrogen donor solvent at a temperature ranging from about 150° to about 350° C. and at a pressure ranging from about 0 to about 150 psig, for a time sufficient for said coal to sorb at least a portion of said vapor phase solvent and thereby swell, and increase in weight by at least about 3 weight percent, and (b) subsequently subjecting the resulting swollen coal to said coal liquefaction conditions.
Claim 3
Dependent Claim 28 words
The process of claim 1 wherein said coal is increased in weight from about 3 to about 50 weight percent, based on the initial weight of said coal.
Claim 4
Dependent Claim 19 words
The process of claim 1 wherein said temperature of step (a) ranges from about 204 to about 350° C.
Claim 5
Dependent Claim 29 words
The process of claim 1 wherein said particulate coal is contacted with said vapor phase solvent for a period of time ranging from about 10 to about 100 minutes.
Claim 6
Dependent Claim 22 words
The process of claim 1 wherein the solvent to coal weight ratio ranges from about 0.05:1 to 1:1 in said contacting step.
Claim 7
Dependent Claim 18 words
The process of claim 1 wherein said coal liquefaction is conducted in the presence of added molecular hydrogen.
Claim 8
Dependent Claim 21 words
The process of claim 1 wherein said coal liquefaction conditions include a temperature ranging from about 371° to about 816° C.
Claim 9
Dependent Claim 21 words
The process of claim 1 wherein said coal liquefaction conditions include a pressure ranging from about 0 to about 3000 psig.
Claim 10
Dependent Claim 28 words
The process of claim 1 wherein said particulate coal in step (a) is maintained in a fluidized bed fluidized by a fluidizing agent comprising said vapor phase solvent.
Claim 11
Dependent Claim 47 words
In the process of claim 1, the improvement which comprises the additional steps of separating the effluent of said coal liquefaction zone into a vapor phase product and a solid residue, and contacting said solid residue with steam and an oxygen-containing gas to produce a hydrogen-containing gas.
Claim 12
Dependent Claim 19 words
The process of claim 1 wherein said temperature of step (a) ranges from about 204° to about 250° C.

References Cited (Backward Citations)

US2166321A Cited
US3692662A Cited
US3791957A Cited
US4019975A Cited
US3997424A Cited
US3970541A Cited
US4036730A Cited
US4036731A Cited
US4082643A Cited
US4075079A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-02-10 1984-08-11 1985-02-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-02-10 1988-08-11 1989-02-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-02-10 1992-08-11 1993-02-10 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag