← Back to Patent Explorer
US4166802A Expired / Lapsed US ⏱️ 0.0 years remaining

Gasification of low quality solid fuels

Assignee: Texaco Inc
•
Filing: 1978-04-20
•
Granted: 1979-09-04
•
Expires: 1998-04-20
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Low quality solid fuels are gasified by being fed to a gasifier in a concentrated water slurry, the high solids content of the slurry being possible by subjecting the solid fuel to hydrothermal treatment in the product gas quench zone.

Inventors

  • 👤 William L. Slater
  • 👤 George N. Richter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:37
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/72; C10J3/78; C10J3/82; C10J3/84; C10J3/845; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1846; Y; Y10; Y10S; Y10S48/00; Y10S48/07

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 169 words
A process for the gasification of a solid carbonaceous fuel selected from the group consisting of sub-bituminous coal and lignite which comprises forming an initial slurry of said fuel in water, containing less than 50 weight percent solids, contacting said initial slurry with hot synthesis gas comprising carbon monoxide and hydrogen in a quench zone thereby cooling said gas and heating said initial slurry to a temperature between about 400° F. and 700° F., the pressure in said quench zone being sufficiently high to keep the water in liquid phase, maintaining the slurry under said conditions of temperature and pressure for a period of time between 0.1 minute and 1 hour, subjecting the so treated fuel as a concentrated water slurry containing between about 50 and 75 wt. % solids measured on a dry basis to partial oxidation to produce additional synthesis gas comprising carbon monoxide and hydrogen and introducing said additional synthesis gas into said quench zone to heat additional initial slurry and quench said additional synthesis gas.
Claim 2
Dependent Claim 169 words
A process for the gasification of a solid carbonaceous fuel selected from the group consisting of sub-bituminous coal and lignite which comprises forming an initial slurry of said fuel in water, containing less than 50 weight percent solids, contacting said initial slurry with hot synthesis gas comprising carbon monoxide and hydrogen in a quench zone thereby cooling said gas and heating said initial slurry to a temperature between about 400° F. and 700° F., the pressure in said quench zone being sufficiently high to keep the water in liquid phase, maintaining the slurry under said conditions of temperature and pressure for a period of time between 0.1 minute and 1 hour, subjecting the so treated fuel as a concentrated water slurry containing between about 50 and 75 wt. % solids measured on a dry basis to partial oxidation to produce additional synthesis gas comprising carbon monoxide and hydrogen and introducing said additional synthesis gas into said quench zone to heat additional initial slurry and quench said additional synthesis gas.
Claim 3
Dependent Claim 23 words
The process of claim 1 in which the treated slurry is removed from the quench zone and is sent to a settling zone.
Claim 4
Dependent Claim 25 words
The process of claim 2 in which in the settling zone the slurry is separated into a clarified water layer and a concentrated slurry layer.
Claim 5
Dependent Claim 17 words
The process of claim 3 in which the clarified water is used to make additional initial slurry.
Claim 6
Dependent Claim 29 words
The process of claim 3 in which the clarified water is used to cool hot synthesis gas prior to its contact with said initial slurry in said quench zone.
Claim 7
Dependent Claim 26 words
The process of claim 1 in which the pressure in the partial oxidation zone and the quench zone is between about 500 psig and 3000 psig.
Claim 8
Dependent Claim 21 words
The process of claim 1 in which the temperature in the quench zone is between about 400° F. and 600° F.
Claim 9
Dependent Claim 19 words
The process of claim 1 in which the period of time is between about 1 minute and 15 minutes.
Claim 10
Dependent Claim 19 words
The process of claim 1 in which the slurry removed from the quench zone is concentrated by mechanical means.

References Cited (Backward Citations)

US2961310A Cited
US2987387A Cited
US3544291A Cited
US3528930A Cited
US3607156A Cited
US3764547A Cited
US3607157A Cited
US3929429A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-09-03 1983-03-05 1983-09-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-09-03 1987-03-05 1987-09-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-09-03 1991-03-05 1991-09-04 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag