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US4291634A Expired / Lapsed US ⏱️ 0.0 years remaining

Solid refuse disposal apparatus

Assignee: Praxair Technology Inc
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Filing: 1980-05-29
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Granted: 1981-09-29
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Expires: 2000-05-29
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Abstract

Abstract Apparatus for disposing of pelletized refuse by conversion into useful gaseous products and inert solid residue, comprising a vertical shaft and an enlarged hearth beneath the shaft, with a multiplicity of tuyeres for feeding oxygen-containing gas into the hearth.

Inventors

  • 👤 Victor E. Bergsten
  • 👤 Edward P. Eardley
  • 👤 Thomas G. Halvorson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 15:22
CPC Classifications
F; F23; F23G; F23G7/00; F23G5/00; F23G5/08; F23G5/085; C; C10; C10J; C10J3/00; C10J3/02; C10J3/06; C10J3/08; C10J3/20; C10J3/22; C10J3/72; C10J3/74; C10J3/76; F23G5/24; F27; F27B; F27B1/00; F27B1/02; F27B1/025; C10J2200/00; C10J2200/15; C10J2200/152; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/0916; C10J2300/092; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; Y; Y02; Y02P; Y02P20/00; Y02P20/141; Y02P20/145; Y10; Y10S; Y10S266/00; Y10S266/90

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 252 words
In apparatus for disposing of pelletized refuse by conversion to useful gaseous product and inert solid residue, including a vertical shaft with an upper end for pelletized refuse providing a drying zone in the top section and a thermal decomposition zone in the intermediate section thereof to form a pelletized refuse bed, a hearth beneath said shaft and in flow communication with the lower end of said shaft, means for feeding oxygen-containing gas into said hearth as a combustion zone, and a tap hole communicating with said hearth for discharging molten residue therefrom, the improvement comprising: (a) a hearth volume V (ft 3 ) which is greater than that defined by the following equation: V=7.28×10.sup.2 G.sub.r D.sub.s.sup.2 /P.sub.g where G r =pelletized refuse maximum feed rate (lb. refuse/ft 2 shaft minimum cross-sectional area/second), D s =shaft minimum equivalent diameter (ft) and P g =furnace pressure (psia). (b) an opening connection between the shaft and the hearth having minimum cross-sectional area between 0.044 and 1.0 times the shaft minimum cross-sectional area, (c) a multiplicity of tuyeres as the means for feeding oxygen-containing gas into the hearth, each positioned at circumferentially spaced locations in the upper part of the hearth adjacent to the shaft-hearth connection (b) which are less than 35% of the vertical distance from the shaft-hearth connection (b) mid-point to the hearth floor, with (d) said tuyeres inclined downwardly and away from the shaft-hearth connection (b) and directed so that said oxygen-containing gas does not impinge directly against said pelletized refuse bed.
Claim 2
Dependent Claim 252 words
In apparatus for disposing of pelletized refuse by conversion to useful gaseous product and inert solid residue, including a vertical shaft with an upper end for pelletized refuse providing a drying zone in the top section and a thermal decomposition zone in the intermediate section thereof to form a pelletized refuse bed, a hearth beneath said shaft and in flow communication with the lower end of said shaft, means for feeding oxygen-containing gas into said hearth as a combustion zone, and a tap hole communicating with said hearth for discharging molten residue therefrom, the improvement comprising: (a) a hearth volume V (ft 3 ) which is greater than that defined by the following equation: V=7.28×10.sup.2 G.sub.r D.sub.s.sup.2 /P.sub.g where G r =pelletized refuse maximum feed rate (lb. refuse/ft 2 shaft minimum cross-sectional area/second), D s =shaft minimum equivalent diameter (ft) and P g =furnace pressure (psia). (b) an opening connection between the shaft and the hearth having minimum cross-sectional area between 0.044 and 1.0 times the shaft minimum cross-sectional area, (c) a multiplicity of tuyeres as the means for feeding oxygen-containing gas into the hearth, each positioned at circumferentially spaced locations in the upper part of the hearth adjacent to the shaft-hearth connection (b) which are less than 35% of the vertical distance from the shaft-hearth connection (b) mid-point to the hearth floor, with (d) said tuyeres inclined downwardly and away from the shaft-hearth connection (b) and directed so that said oxygen-containing gas does not impinge directly against said pelletized refuse bed.
Claim 3
Dependent Claim 26 words
Apparatus according to claim 1 in which the average cross-sectional area of said hearth is between 0.7 and 3.2 times the square of the hearth height.
Claim 4
Dependent Claim 19 words
Apparatus according to claim 1 in which said tuyeres are oriented substantially tangentially to the shaft opening connection (b).
Claim 5
Dependent Claim 38 words
Apparatus according to claim 1 in which the shaft opening connection (b) minimum cross-sectional area is between 0.7 and 1.0 times the shaft minimum cross-sectional area such that said pelletized refuse bed is formed on the hearth floor.
Claim 6
Dependent Claim 51 words
Apparatus according to claim 1 in which said lower end of the shaft is sloped inwardly to form the shaft opening connection (b) with a minimum cross-sectional area between 0.075 and 0.2 times the shaft minimum cross-sectional area, such that said pelletized refuse bed is supported by said shaft opening connection.
Claim 7
Dependent Claim 22 words
Apparatus according to claim 1 wherein said tuyeres are downwardly inclined at inclination angle α of between 10 degrees and 45 degrees.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-09-28 1985-03-30 1985-09-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-09-28 1989-03-30 1989-09-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-09-28 1993-03-30 1993-09-29 $7700.00 Window Closed / Lapsed

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