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US4155313A Expired / Lapsed US ⏱️ 0.0 years remaining

Utilization of solid material containing combustible matter

Assignee: Environmental Protection Agency
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Filing: 1977-07-15
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Granted: 1979-05-22
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Expires: 1997-07-15
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Abstract

Abstract Solid particles comprising combustible matter (e.g. coal) associated with or contaminated by inert matter (e.g. ash, rock) is segregated in a segregation zone into low density/small size and high density/large size fractions. The low density/small size fractions are passed to a utilization zone for conversion of the combustible matter. The high density/large size fractions are size reduced (e.g. by grinding) and either returned to the segregation zone, or passed at least in part, directly to the utilization zone. The conversion of the combustion matter proceeds more efficiently as a result. The segregation zone may operate by fluidized size/density segregation and in the utilization zone, the combustible matter may be at least partially combusted, preferably in a fluidized bed.

Inventors

  • 👤 Gerald Moss

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 23:46
CPC Classifications
B; B03; B03B; B03B4/00; B03B4/06; C; C10; C10L; C10L9/00

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 219 words
A method for utilizing a solid particulate feedstock containing combustible matter contaminated with non-combustible or inert material comprising the steps; a. passing the feedstock into a fluidized bed segregation zone having a fluidizing gas passing upwardly therethrough whereby relatively fine particles and relatively light particles migrate upwardly and relatively dense particles and relatively coarse particles migrate downwardly through the fluidized bed, b. removing the relatively dense and the relatively coarse particles from the lower portion of the fluidized bed segregation zone, c. passing said dense and coarse particles through a comminuter zone to reduce them to a finer size, d. returning the reduced particles to the fluidized bed segregation zone, e. adjusting the rate of removal of the relatively dense and the relatively coarse particles from the fluidized bed segregation zone to maintain a predetermined particle size and density gradient in said zone, f. adjusting the rate of introduction of the feedstock to the fluidized bed segregation to maintain the upper level of the fluidized bed at a predetermined height, g. removing dust-laden gas from the upper portion of the fluidized bed segregation zone, above the surface of the fluidized bed, h. continuously withdrawing the finer particles and the lighter particles from the upper portion of the said segregation zone and passing them into a fluidized bed utilization zone.
Claim 2
Independent Claim 219 words
A method for utilizing a solid particulate feedstock containing combustible matter contaminated with non-combustible or inert material comprising the steps; a. passing the feedstock into a fluidized bed segregation zone having a fluidizing gas passing upwardly therethrough whereby relatively fine particles and relatively light particles migrate upwardly and relatively dense particles and relatively coarse particles migrate downwardly through the fluidized bed, b. removing the relatively dense and the relatively coarse particles from the lower portion of the fluidized bed segregation zone, c. passing said dense and coarse particles through a comminuter zone to reduce them to a finer size, d. returning the reduced particles to the fluidized bed segregation zone, e. adjusting the rate of removal of the relatively dense and the relatively coarse particles from the fluidized bed segregation zone to maintain a predetermined particle size and density gradient in said zone, f. adjusting the rate of introduction of the feedstock to the fluidized bed segregation to maintain the upper level of the fluidized bed at a predetermined height, g. removing dust-laden gas from the upper portion of the fluidized bed segregation zone, above the surface of the fluidized bed, h. continuously withdrawing the finer particles and the lighter particles from the upper portion of the said segregation zone and passing them into a fluidized bed utilization zone.
Claim 3
Dependent Claim 26 words
The method of claim 1 wherein the finer and the lighter particles are passed into the utilization zone employing the dust-laden gas as a conveyor gas.
Claim 4
Dependent Claim 45 words
The method of claim 2 wherein the dust-laden gas is removed from the upper portion of the fluidized bed segregation zone at a plurality of points and passed into the utilization zone with the finer and the lighter particles at a like plurality of points.
Claim 5
Dependent Claim 13 words
The method of claim 1 wherein the utilization zone is a combustion zone.
Claim 6
Dependent Claim 209 words
Apparatus for segregating combustible matter from a solid particulate feedstock containing combustible matter contaminated with non-combustible or inert material and for utilizing the segregated combustible matter comprising; a. a fluidized bed segregation zone having an upper and lower region adapted to receive a continuous feed of said feedstock, b. means for removing relatively dense particles and relatively coarse particles from the lower region of said zone, c. comminution means for comminuting the particles removed from said lower region to a relatively fine size, d. means for conveying said comminuted particles to the upper portion of the fluidized segregation zone, e. means for adjusting the rate of withdrawal of the relatively coarse particles and relatively dense particles from the lower region of said zone to maintain a predetermined finer particle size in said zone, f. means for adjusting the rate of introduction of the feedstock to the fluidized segregation zone to maintain the upper level of the fluidized bed at a predetermined height, g. means for removing dust-laden gas from the upper portion of the segregation zone, above the surface of the fluidized bed, and h. means for continuously withdrawing finer particles from the upper portion of the said segregation zone and passing them into a fluidized bed utilization zone.
Claim 7
Dependent Claim 209 words
Apparatus for segregating combustible matter from a solid particulate feedstock containing combustible matter contaminated with non-combustible or inert material and for utilizing the segregated combustible matter comprising; a. a fluidized bed segregation zone having an upper and lower region adapted to receive a continuous feed of said feedstock, b. means for removing relatively dense particles and relatively coarse particles from the lower region of said zone, c. comminution means for comminuting the particles removed from said lower region to a relatively fine size, d. means for conveying said comminuted particles to the upper portion of the fluidized segregation zone, e. means for adjusting the rate of withdrawal of the relatively coarse particles and relatively dense particles from the lower region of said zone to maintain a predetermined finer particle size in said zone, f. means for adjusting the rate of introduction of the feedstock to the fluidized segregation zone to maintain the upper level of the fluidized bed at a predetermined height, g. means for removing dust-laden gas from the upper portion of the segregation zone, above the surface of the fluidized bed, and h. means for continuously withdrawing finer particles from the upper portion of the said segregation zone and passing them into a fluidized bed utilization zone.
Claim 8
Dependent Claim 20 words
The apparatus of claim 5 comprising means employing the dust-laden gas for passing the finer particles into the utilization zone.
Claim 9
Dependent Claim 71 words
The apparatus of claim 5 wherein the upper region of the fluidized bed segregation zone is elongated horizontally and the fluidized bed utilization zone is disposed generally parallel to the said upper region, a plurality of means for removing the dust-laden gas from the upper portion of the fluidized bed segregation zone, and a like plurality of means for passing the dust laden gas and finer particles into said utilization zone.

References Cited (Backward Citations)

US1948800A Cited
US2200472A Cited
US2310894A Cited
US3078048A Cited
US3349912A Cited
US3513858A Cited
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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) 1982-05-21 1982-11-20 1983-05-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-05-21 1986-11-20 1987-05-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-05-21 1990-11-20 1991-05-22 $7700.00 Window Closed / Lapsed

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