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US4057402A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal pretreatment and gasification process

Assignee: Gas Technology Institute
•
Filing: 1976-06-28
•
Granted: 1977-11-08
•
Expires: 1996-06-28
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Abstract

Abstract A process for converting a finely divided carbonaceous material, particularly coal, to a fuel gas. A finely divided or pulverized carbonaceous feed material, such as coal, is pretreated at a temperature of about 700° - 800° F in order to destroy the caking properties of a caking coal feed in a fluidized pretreatment zone, or, alternatively to dry a non-caking coal feed. The pretreated coal is passed from a pretreatment zone to a gasification zone wherein the carbonaceous feed material or coal is maintained as a fluid bed at selected conditions for converting the pretreated material to ash and a gaseous mixture. During the pretreatment of the feed material, hot off gases are formed and the hot off gases, which generally comprise steam, tars, oils, and carbonaceous fines, are passed from the pretreatment zone to the underside of the fluid bed in the gasification zone. The steam contained in the off gases is reacted with the coal in the fluidized bed in the gasification zone for converting the coal feed material to ash and the fuel gas product. The off gases also provide heat for maintaining the desired temperature conditions in the gasification zone. The tars and oils in the off gases are substantially destroyed during passage upwardly through the fluidized bed in the gasification zone. The fines in the off gases are converted by the gasification reaction in the gasification zone to form a part of the fuel gas and the ash. The fuel gas is withdrawn from the upper portion of the gasification zone and ash is withdrawn from the bottom of the gasification zone.

Inventors

  • 👤 Jitendra G. Patel
  • 👤 Frank C. Schora
  • 👤 John W. Loeding

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 21:19
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/482; C10J3/02; C10J3/20; C10J3/34; C10J3/36; C10J3/52; C10J3/523; C10J3/54; C10J3/56; C10J3/58; C10J3/60; C10J3/64; C10J3/66; C10J3/72; C10J3/721; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0956; C10J2300/0973; C10J2300/0976

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 262 words
In a process for the conversion of finely divided caking coal to a fuel gas wherein said process includes the steps of pretreating a finely divided coal feed material at a temperature of about 700°-800° F in a fluidized pretreatment zone while forming hot off gases, said pretreatment zone being in direct communication with a gasification zone, passing the pretreated coal from said pretreatment zone to said gasification zone, maintaining said pretreated coal as a fluidized bed in said gasification bed in said gasification zone at preselected conditions for converting said pretreated coal to ash and a gaseous mixture comprising fuel gas, with drawing said gas from said gasification zone, and withdrawing said ash from said gasification zone, an improvement in said process comprising the steps of adding water directly into said pretreatment zone to dissipate heat generated therein and to generate steam, passing said hot off gases from said pretreatment zone to below the upper surface of said fluidized coal bed in said gasification zone, said off gases comprising said steam, tars, oils and coal fines, passing said off gases upwardly through said fluidized bed, reacting said steam with said coal in said fluidized bed for converting said coal to said ash and said gaseous mixture, said off gases heating said gasification zone for assisting in maintaining said preselected conditions in said gasification zone, substantially destroying said tars and oils during passage through said fluidized bed in said gasification zone, and converting said fines in said off gases to a portion of said gaseous mixture and a portion of said ash.
Claim 2
Dependent Claim 262 words
In a process for the conversion of finely divided caking coal to a fuel gas wherein said process includes the steps of pretreating a finely divided coal feed material at a temperature of about 700°-800° F in a fluidized pretreatment zone while forming hot off gases, said pretreatment zone being in direct communication with a gasification zone, passing the pretreated coal from said pretreatment zone to said gasification zone, maintaining said pretreated coal as a fluidized bed in said gasification bed in said gasification zone at preselected conditions for converting said pretreated coal to ash and a gaseous mixture comprising fuel gas, with drawing said gas from said gasification zone, and withdrawing said ash from said gasification zone, an improvement in said process comprising the steps of adding water directly into said pretreatment zone to dissipate heat generated therein and to generate steam, passing said hot off gases from said pretreatment zone to below the upper surface of said fluidized coal bed in said gasification zone, said off gases comprising said steam, tars, oils and coal fines, passing said off gases upwardly through said fluidized bed, reacting said steam with said coal in said fluidized bed for converting said coal to said ash and said gaseous mixture, said off gases heating said gasification zone for assisting in maintaining said preselected conditions in said gasification zone, substantially destroying said tars and oils during passage through said fluidized bed in said gasification zone, and converting said fines in said off gases to a portion of said gaseous mixture and a portion of said ash.
Claim 3
Dependent Claim 28 words
The improved process of claim 1 wherein said pretreating step is at a temperature of 750°- 800° F and at a pressure of up to about 1000 PSIG.
Claim 4
Dependent Claim 27 words
The improved process of claim 1 wherein said steam in said off gases provides the sole source of steam for said gasification reaction in said gasification zone.
Claim 5
Dependent Claim 36 words
The improved process of claim 1 wherein water is vaporized by indirect heat exchange in said bed in said pretreatment zone to form steam, and including the step of passing said steam to said gasification zone.
Claim 6
Dependent Claim 25 words
The improved process of claim 1 wherein said water is added is part of a slurry of said coal and water to said pretreatment zone.
Claim 7
Dependent Claim 19 words
The improved process of claim 1 wherein said water is sprayed directly into the interior of said pretreatment zone.
Claim 8
Dependent Claim 31 words
The improved process of claim 1 wherein air is also added to said gasification zone for reaction with said steam and said coal to form said ash and said gaseous mixture.
Claim 9
Dependent Claim 25 words
The improved process of claim 1 wherein said temperature in said gasification zone is about 1700°-1900° F and the pressure is up to 1000° PSIG.

References Cited (Backward Citations)

US2623815A Cited
US3884649A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-11-07 1981-05-09 1981-11-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-11-07 1985-05-09 1985-11-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-11-07 1989-05-09 1989-11-08 $7700.00 Window Closed / Lapsed

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