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US4042345A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for conversion of solid refuse to fuel gas using pelletized refuse feed

Assignee: Praxair Technology Inc
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Filing: 1976-04-12
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Granted: 1977-08-16
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Expires: 1996-04-12
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Abstract

Abstract A process for simultaneously disposing of refuse and producing a useful fuel or synthesis gas and an inert inorganic residue by feeding shredded refuse, from which ferrous metal has preferably been magnetically separated, and which has been compacted into hard pellets, into an oxygen fed pyrolizing, slagging shaft furnace.

Inventors

  • 👤 John Erling Anderson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 22:09
CPC Classifications
C; C10; C10J; C10J3/00; C10B; C10B49/00; C10B49/02; C10B53/00; C10B53/08; C10J3/02; C10J3/06; C10J3/08; C10J3/20; C10J3/30; C10J3/72; C10J3/723; C10J3/78; B; B65; B65G; B65G2201/00; B65G2201/04; C10J2300/00; C10J2300/09; C10J2300/0903; C10J2300/0906; C10J2300/0913; C10J2300/0916; C10J2300/092; C10J2300/0946; C10J2300/0953; C10J2300/0959; C10J2300/16; C10J2300/1625; C10J2300/1628; Y; Y02; Y02E; Y02E50/00; Y02E50/30

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 250 words
In a process for disposing of refuse while simultaneously producing a useful gaseous product and an inert solid residue, comprising the steps of (a) feeding refuse into the top portion of a vertical shaft furnace and forming a bed of said refuse within the furnace, (b) feeding an oxygen containing gas into the base of said furnace, (c) pyrolysing the organic portion of the refuse, (d) fluidizing the inorganic portion of the refuse, (e) discharging the gaseous products from the top of said furnace, and (f) tapping the fluidized inorganic material from the base of said furnace, the improvement comprising: feeding the refuse into the furnace in the form of pellets of compacted refuse, said pellets being of sufficient structural strength to remain coherent at least within the drying and pyrolysis zones of the furnace, in order to inhibit channeling and to provide a porous structure throughout the height of the refuse bed, said pellets having: 1. a density greater than that given by the equation: D = 2,000/(100-0.8A) where: D = the density of the pellet (lbs./ft. 3 ), and A = percent inorganics in the refuse pellet, and 2. a surface to volume ratio greater than that given by the equation: R = 15(G/H).sup.0.625 where: R = the ratio of the surface area to the volume of the pellet (ft. 2 /ft. 3 ) H = the height of the refuse bed in the furnace (ft.) G = the refuse feed rate (tons/day/ft. 2 of furnace cross-sectional area).
Claim 2
Dependent Claim 250 words
In a process for disposing of refuse while simultaneously producing a useful gaseous product and an inert solid residue, comprising the steps of (a) feeding refuse into the top portion of a vertical shaft furnace and forming a bed of said refuse within the furnace, (b) feeding an oxygen containing gas into the base of said furnace, (c) pyrolysing the organic portion of the refuse, (d) fluidizing the inorganic portion of the refuse, (e) discharging the gaseous products from the top of said furnace, and (f) tapping the fluidized inorganic material from the base of said furnace, the improvement comprising: feeding the refuse into the furnace in the form of pellets of compacted refuse, said pellets being of sufficient structural strength to remain coherent at least within the drying and pyrolysis zones of the furnace, in order to inhibit channeling and to provide a porous structure throughout the height of the refuse bed, said pellets having: 1. a density greater than that given by the equation: D = 2,000/(100-0.8A) where: D = the density of the pellet (lbs./ft. 3 ), and A = percent inorganics in the refuse pellet, and 2. a surface to volume ratio greater than that given by the equation: R = 15(G/H).sup.0.625 where: R = the ratio of the surface area to the volume of the pellet (ft. 2 /ft. 3 ) H = the height of the refuse bed in the furnace (ft.) G = the refuse feed rate (tons/day/ft. 2 of furnace cross-sectional area).
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein the refuse has been shredded prior to being compacted into pellets.
Claim 4
Dependent Claim 25 words
The process of claim 2 wherein most of the ferrous metal has been magnetically separated from the shredded refuse prior to being compacted into pellets.
Claim 5
Dependent Claim 23 words
The process of claim 1 wherein the density of said pellets is in the range of from 25 to 50 lbs./ft. 3 .
Claim 6
Dependent Claim 38 words
The process of claim 1 wherein said oxygen containing gas contains at least 40% oxygen, and wherein the weight ratio of oxygen to refuse fed to the furnace is maintained within the range of from 0.15:1 to 0.28:1.

References Cited (Backward Citations)

US749302A Cited
US3426673A Cited
US3692505A Cited
US3729298A Cited
US3926582A Cited
US3841851A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-15 1981-02-14 1981-08-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-15 1985-02-14 1985-08-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-15 1989-02-14 1989-08-16 $7700.00 Window Closed / Lapsed

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