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US4987954A Expired / Lapsed US ⏱️ 0.0 years remaining

Fuel reactor

Assignee: Individual
•
Filing: 1990-03-13
•
Granted: 1991-01-29
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Expires: 2010-03-13
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Abstract

Abstract A fuel reactor particularly adopted for the efficient combustion of wood and wood-product fuels includes a core comprised of an inner fuel tube and an outer gas tube. Fuel is introduced into one end of the fuel tube and the combustion process is initiated. Perforations in the gas tube allow the combustion gas to progress down the fuel tube and combine with air in the gas tube. A high temperature is maintained on the gas tube to enhance the combustion process. In addition, high temperature-high pressure steam and air are introduced into the core to increase the reactivity rate of char products. The high temperature-high pressure steam is produced by a novel steam pump. The combustion gases are further processed through a gas dispersion chamber, including dispersion plates, and a gas expansion chamber. Heat is extracted from the combustion gases via a novel heat exchanger which includes a gas dispersion shelf, a radiating heat exchanger plate, a primary heat exchanger, and a condensing heat exchanger. A reheater chamber assures positive gas flow through the reactor and out a stack.

Inventors

  • 👤 Robert J. Boucher

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:25
CPC Classifications
F; F02; F02B; F02B45/00; C; C10; C10B; C10B53/00; C10B53/02; F02D; F02D19/00; F02D19/06; F02D19/0639; F02D19/0649; F02D19/0652; F04; F04F; F04F1/00; F04F1/18; F23; F23G; F23G5/00; F23G5/02; F23G5/027; F23G5/44; F23G5/46; F23G7/00; F23G7/10; F23G7/105; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y02T; Y02T10/00; Y02T10/10; Y02T10/30

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 177 words
A heat exchanger for extracting heat from a combustion gas producing core comprising: a gas dispersion shelf positioned above said core acting to distribute the combustion gas at a substantially constant density and providing a thermal barrier above the core for maintaining core temperature; a radiating heat exchanger plate positioned above said gas dispersion shelf for extracting heat therefrom; said gas dispersion shelf and said radiating heat exchanger plate being provided with flow holes with said heat exchanger plate positioned with respect to said gas dispersion shelf such that the combustion gas flows through said gas dispersion shelf holes, impinges on the lower surface of said radiating heat exchanger plate and moves laterally there across to the holes therein; and a primary heat exchanger comprising a vessel for containing the heat exchanger medium, said vessel being positioned above said radiating heat exchanger plate and including gas flow tubes extending through said vessel to allow combustion gas flow there through to thereby enhance the transfer of heat from said combustion gas to said vessel and heat exchanger medium.
Claim 2
Dependent Claim 177 words
A heat exchanger for extracting heat from a combustion gas producing core comprising: a gas dispersion shelf positioned above said core acting to distribute the combustion gas at a substantially constant density and providing a thermal barrier above the core for maintaining core temperature; a radiating heat exchanger plate positioned above said gas dispersion shelf for extracting heat therefrom; said gas dispersion shelf and said radiating heat exchanger plate being provided with flow holes with said heat exchanger plate positioned with respect to said gas dispersion shelf such that the combustion gas flows through said gas dispersion shelf holes, impinges on the lower surface of said radiating heat exchanger plate and moves laterally there across to the holes therein; and a primary heat exchanger comprising a vessel for containing the heat exchanger medium, said vessel being positioned above said radiating heat exchanger plate and including gas flow tubes extending through said vessel to allow combustion gas flow there through to thereby enhance the transfer of heat from said combustion gas to said vessel and heat exchanger medium.
Claim 3
Dependent Claim 14 words
The heat exchanger of claim 1 wherein said vessel has a generally diamond-shaped cross-section.
Claim 4
Dependent Claim 83 words
The heat exchanger of claim 1 wherein said primary heat exchanger further includes at least one heat pipe positioned between said vessel and said radiating heat exchanger plate such that combustion gases which pass through the holes in said plate flow around said heat pipe carrying the heat exchanger medium from at least two locations on said vessel to produce a flow in said heat pipe and thereby further enhance the transfer of heat from the combustion gas to said primary heat exchanger.
Claim 5
Dependent Claim 46 words
The heat exchanger of any of claims 1 through 3 further comprising: a condensing heat exchanger including a plurality of vertical pipes joined to a manifold for providing the input exchanger medium to said vessel, said vertical pipes being positioned opposite vertical faces of said core.
Claim 6
Dependent Claim 68 words
The heat exchanger of claim 4 further comprising: a housing for enclosing said core and said heat exchanger and forming a condensing chamber, said condensing chamber formed such that combustion gases which emerge from the top of the primary heat exchanger are routed around the core, past said condensing heat exchanger to the reheater chambers and up to a stack provided in the upper surface of said housing.
Claim 7
Dependent Claim 31 words
The heat exchanger of claim 5 wherein the condensing heat exchanger includes a wire mesh wall for extracting condensing fluid from the combustion gases and draining the condensate to a drain.
Claim 8
Dependent Claim 125 words
A heat exchanger for extracting heat from a central heat source and creating a self-induced draft, comprising: a primary heat exchanger positioned above said heat source and extracting heat from hot gases flowing therefrom; a condensing chamber positioned vertically downward from said primary heat exchanger and along a side of the heat source for extracting heat from, and condensing vapor in said hot gases; a reheater chamber positioned around the underside of the heat source to reheat the hot gases cooled by the condensing chamber; a stack for venting the heated gases from the reheater chamber; and an enclosure for said heat exchanger for directing gas flow from the primary heat exchanger down past the condensing chamber, into the reheater chamber and out the stack.
Claim 9
Dependent Claim 125 words
A heat exchanger for extracting heat from a central heat source and creating a self-induced draft, comprising: a primary heat exchanger positioned above said heat source and extracting heat from hot gases flowing therefrom; a condensing chamber positioned vertically downward from said primary heat exchanger and along a side of the heat source for extracting heat from, and condensing vapor in said hot gases; a reheater chamber positioned around the underside of the heat source to reheat the hot gases cooled by the condensing chamber; a stack for venting the heated gases from the reheater chamber; and an enclosure for said heat exchanger for directing gas flow from the primary heat exchanger down past the condensing chamber, into the reheater chamber and out the stack.

References Cited (Backward Citations)

US4232634A Cited
US4413590A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-01-28 1994-07-30 1995-01-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-01-28 1998-07-30 1999-01-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-01-28 2002-07-30 2003-01-29 $7700.00 Window Closed / Lapsed

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