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US4078914A Expired / Lapsed US ⏱️ 0.0 years remaining

Gasification of coal and refuse in a vertical shaft furnace

Assignee: Individual
•
Filing: 1975-07-31
•
Granted: 1978-03-14
•
Expires: 1995-07-31
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Abstract

Abstract The combustion of refuse, including all types of trash and garbage, in the presence of coal and/or coke and a fluxing agent in a vertical shaft furnace provides for the clean combustion of the refuse, the recovery of metallic wastes and the enhanced production of a gaseous fuel. By blending the refuse with the coal and/or coke and fluxing agent in a coal reaction, a fairly even distribution of the refuse will be achieved to prevent the compaction of the refuse and clogging of the furnace and to provide a more uniform controllable combustion temperature within the furnace thereby prolonging the life of the furnace lining. By using a conventional blast furnace, iron ore and/or scrap metal can also be added to the feed stock for the production of pig iron and the steam generated as a result of the high moisture content of the refuse can be utilized to react with the nascent pig iron within the furnace for the production of hydrogen to enrich the blast furnace gas to provide a high quality fuel gas. The refuse can be added directly to the furnace or be subjected to a preheating operation to reduce the moisture content and volume of the refuse. The steam generated in the pretreatment can be directed into the furnace to cause an enrichment of the furnace effluent gas or be utilized directly for heating or power generation.

Inventors

  • 👤 Louis Gold

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 08:10
CPC Classifications
C; C10; C10J; C10J3/00; C01; C01B; C01B3/00; C01B3/02; C01B3/06; C01B3/061; C01B3/08; C01B3/10; C10J2300/00; C10J2300/09; C10J2300/0983; C10J2300/0996; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/36

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 146 words
A method for the clean combustion of sulfur-bearing coal comprising, introducing a mixture consisting essentially of municipal refuse, said coal and limestone into a substantially closed vertical shaft furnance, burning said coal in the presence of the limestone, decomposing and melting the limestone to provide a slagging action for the removal of ash and sulfur-bearing compounds resulting from said burning, introducing an unheated air blast into the furnace through a plurality of circumferentially spaced tuyeres to define a combustion zone within the furnance adjacent the level of the tuyeres, converting the carbon dioxide produced by the burning of the coal in the combustion zone to carbon monoxide as it passes upwardly through the coal and limestone burden, removing the slag from the bottom of the furnace and removing the gaseous effluent from the top of the furnace which is comprised substantially of nitrogen and carbon monoxide.
Claim 2
Independent Claim 146 words
A method for the clean combustion of sulfur-bearing coal comprising, introducing a mixture consisting essentially of municipal refuse, said coal and limestone into a substantially closed vertical shaft furnance, burning said coal in the presence of the limestone, decomposing and melting the limestone to provide a slagging action for the removal of ash and sulfur-bearing compounds resulting from said burning, introducing an unheated air blast into the furnace through a plurality of circumferentially spaced tuyeres to define a combustion zone within the furnance adjacent the level of the tuyeres, converting the carbon dioxide produced by the burning of the coal in the combustion zone to carbon monoxide as it passes upwardly through the coal and limestone burden, removing the slag from the bottom of the furnace and removing the gaseous effluent from the top of the furnace which is comprised substantially of nitrogen and carbon monoxide.
Claim 3
Dependent Claim 23 words
The process as set forth in claim 1 wherein the temperature of the combustion zone is maintained between 1200° C. and 1500° C.
Claim 4
Dependent Claim 50 words
The process as set forth in claim 1 wherein said refuse is subjected to a preheating in a separate vessel external of said vertical shaft furnace at a temperature between 800° C. and 1000° C. to produce steam and compacting the residue prior to introduction into the vertical shaft furnace.

References Cited (Backward Citations)

GB226500A Cited
US3830636A Cited
US3850588A Cited
US3729298A Cited
US3909446A Cited
GB1396205A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-03-13 1981-09-12 1982-03-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-03-13 1985-09-12 1986-03-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-03-13 1989-09-12 1990-03-14 $7700.00 Window Closed / Lapsed

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