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US4066420A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the gasification of solid fuels

Assignee: Dr C Otto and Co GmbH
•
Filing: 1977-03-04
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Granted: 1978-01-03
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Expires: 1997-03-04
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Abstract

Abstract A process for gasification of pulverized or fine-grain coal is characterized by using a portion of the combustible gas generated at a temperature between 1500° and 2200° C in a slag bath generator as a gaseous agent that is mixed with the coal and then introduced under pressure into the slag bath generator. The portion of the combustible gas to be used for this purpose undergoes processing which includes extracting dust, cooling and drying before the gas is combined with the fuel. According to a different embodiment, the combustible gas produced in the generator is used in the reduction process by feeding the gas into a reduction shaft furnace. The top gas from the shaft furnace is processed by extracting dust, cooling, drying and normalizing the acidity of the top gas before the top gas is combined with fuel for introduction as a mixture into the slag bath generator.

Inventors

  • 👤 Wilhelm Danguillier
  • 👤 Wolfgang Grams

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 03:15
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/57; C10J3/02; C10J3/20; C10J3/30; C10J3/72; C10J3/78; C10J3/82; C10J3/84; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0969; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y10; Y10S; Y10S48/00; Y10S48/02

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 115 words
A process for the gasification of pulverized or fine-grain coal which is introduced as a mixture with a gaseous agent consisting essentially of CO, H 2 and CO 2 in a slag bath generator, said process including the steps of combining said gaseous agent with said coal to form a mixture, introducing said mixture into a slag bath generator, gasifying the coal in the presence of introduced gasifying medium and of included ash in the coal in said generator at a temperature of between 1500° C and 2200° C, withdrawing liquid slag from said slag bath generator, and using a portion of the combustible gas generated by said slag bath generator as said gaseous agent.
Claim 2
Dependent Claim 115 words
A process for the gasification of pulverized or fine-grain coal which is introduced as a mixture with a gaseous agent consisting essentially of CO, H 2 and CO 2 in a slag bath generator, said process including the steps of combining said gaseous agent with said coal to form a mixture, introducing said mixture into a slag bath generator, gasifying the coal in the presence of introduced gasifying medium and of included ash in the coal in said generator at a temperature of between 1500° C and 2200° C, withdrawing liquid slag from said slag bath generator, and using a portion of the combustible gas generated by said slag bath generator as said gaseous agent.
Claim 3
Dependent Claim 62 words
The process according to claim 1 including the further steps of extracting dust from a divided portion of combustible gas withdrawn from said slag bath generator for said step of using a portion of the combustible gas, and cooling the divided portion of combustible gas withdrawn from said slag bath generator for said step of using a portion of the combustible gas.
Claim 4
Dependent Claim 29 words
The process according to claim 2 including the further step of drying the divided portion of combustible gas for said step of using a portion of the combustible gas.
Claim 5
Dependent Claim 28 words
The process according to claim 3 wherein said step of drying the divided portion of combustible gas is carried out by compressing the divided portion of combustible gas.
Claim 6
Dependent Claim 25 words
The process according to claim 1 including the further step of maintaining an elevated pressure in said slag bath generator during the step of gasifying.
Claim 7
Dependent Claim 27 words
The process according to claim 1 including the further step of maintaining a pressure of 25 atmospheres in said slag bath generator during said step of gasifying.
Claim 8
Dependent Claim 12 words
The process according to claim 1 wherein said gasifying medium includes steam.
Claim 9
Dependent Claim 12 words
The process according to claim 1 wherein said gasifying medium includes oxygen.
Claim 10
Dependent Claim 24 words
The process according to claim 1 wherein said gasifying medium has a temperature of about 300° C when fed into said slag bath generator.
Claim 11
Dependent Claim 32 words
The process according to claim 1 wherein said gasifying medium includes steam at 300° C and fed into said slag bath generator at a rate of 0.33 Kg per Kg of coal.
Claim 12
Dependent Claim 32 words
The process according to claim 1 wherein said gasifying medium includes oxygen at 300° C and fed into said slag bath generator at a rate of 1 Kg per Kg of coal.

References Cited (Backward Citations)

US1225396A Cited
US2113774A Cited
US2614915A Cited
US2687950A Cited
US2801158A Cited
US2898272A Cited
GB893057A Cited
FR1245875A Cited
US3437561A Cited
US3854896A Cited
US3957458A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-02 1981-07-04 1982-01-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-02 1985-07-04 1986-01-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-02 1989-07-04 1990-01-03 $7700.00 Window Closed / Lapsed

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