← Back to Patent Explorer
US4687570A Expired / Lapsed US ⏱️ 0.0 years remaining

Direct use of methane in coal liquefaction

Assignee: United States Department of Energy
•
Filing: 1985-06-19
•
Granted: 1987-08-18
•
Expires: 2005-06-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract This invention relates to a process for converting solid carbonaceous material, such as coal, to liquid and gaseous hydrocarbons utilizing methane, generally at a residence time of about 20-120 minutes at a temperature of 250°-750° C., preferably 350°-450° C., pressurized up to 6000 psi, and preferably in the 1000-2500 psi range, preferably directly utilizing methane 50-100% by volume in a mix of methane and hydrogen. A hydrogen donor solvent or liquid vehicle such as tetralin, tetrahydroquinoline, piperidine, and pyrolidine may be used in a slurry mix where the solvent feed is 0-100% by weight of the coal or carbonaceous feed. Carbonaceous feed material can either be natural, such as coal, wood, oil shale, petroleum, tar sands, etc., or man-made residual oils, tars, and heavy hydrocarbon residues from other processing systems.

Inventors

  • 👤 Muthu S. Sundaram
  • 👤 Meyer Steinberg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 12:36
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/06; C10G1/065; C10G1/02; Y; Y10; Y10S; Y10S208/00; Y10S208/951

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 65 words
A process for the liquefaction of carbonaceous materials to produce predominantly liquid hydrocarbons comprising heating said materials in a liquefaction reactor to a temperature in the range of 250° C. to 750° C., under pressure up to 6000 psi of a gas containing methane in the initial gas feed at 50-100% by volume for a residence time in the liquefaction reactor of about 20-120 minutes.
Claim 2
Dependent Claim 65 words
A process for the liquefaction of carbonaceous materials to produce predominantly liquid hydrocarbons comprising heating said materials in a liquefaction reactor to a temperature in the range of 250° C. to 750° C., under pressure up to 6000 psi of a gas containing methane in the initial gas feed at 50-100% by volume for a residence time in the liquefaction reactor of about 20-120 minutes.
Claim 3
Dependent Claim 15 words
The process according to claim 1 wherein the liquefaction is carried out at 400°-450 C.
Claim 4
Dependent Claim 13 words
The process according to claim 1 wherein the gas employed is natural gas.
Claim 5
Dependent Claim 13 words
The process of claim 3 wherein hydrogen is added to the natural gas.
Claim 6
Dependent Claim 43 words
The process according to claim 1 wherein the solid carbonaceous feed material is selected from a member of a group consisting of natural raw materials, such as coal, wood, oil shale, petroleum, tar sands, and man-made residual oils, tars, and heavy hydrocarbon residues.
Claim 7
Dependent Claim 13 words
The process according to claim 5 wherein the solid carbonaceous material is coal.
Claim 8
Dependent Claim 28 words
The process according to claim 1 wherein the carbonaceous material is slurried with a donor solvent selected from the group consisting of hydroaromatic solvents and hydrogenated anthracene oil.
Claim 9
Dependent Claim 25 words
The process according to claim 7 wherein the hydroaromatic solvent employed is selected from the group consisting of tetralin, tetrahydroquinoline, piperidine, indoline, perhydropyrene, and pyrolidine.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-08-17 1991-02-16 1991-08-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-08-17 1995-02-16 1995-08-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-08-17 1999-02-16 1999-08-18 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag