Patent US4164397A successfully refreshed from Google Patents.
US4164397A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Fuel gas production
Assignee: Individual
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Filing: 1978-02-16
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Granted: 1979-08-14
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Expires: 1998-02-16
Abstract
Abstract A method of manufacturing fuel gas from lignocellulose material such as wood. Wood is converted to fuel gas in a descending bed reactor which encloses a descending bed of wood material. Gas produced in the reactor travels upwardly through and thence out from the top of the descending bed, with a portion of the gas being recirculated and introduced as reflow gas, together with air, to a combustion zone established at the base of the descending bed.
Inventors
- 👤 Herbert H. Hunt
- 👤 Harold S. Worcester
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 04:02
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/58; C10J3/60; C10J3/64; C10J3/66; C10J3/02; C10J3/06; C10J3/16; C10J2200/00; C10J2200/36; Y; Y10; Y10S; Y10S48/00; Y10S48/01
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
352 words
A process for making conbustible gas from lignocellulose material which comprises establishing a descending bed of such material in a descending bed reactor, newly introduced material being dropped onto the top of such bed and such newly introduced material having a moisture content within the range of 20% to 80% by weight, said descending bed having adjacent the top thereof a drying zone wherein the material is dried with the production of water vapor, and progressing downwardly from the drying zone a distillation zone where the material is converted to gaseous hydrocarbons and char, and below the distillation zone a combustion zone where the char is reacted with the production of additional gas and residual ash, channeling the ash and all of the gas as such is produced in said bed upwardly through and thence out the top of the bed with the sensible heat of such gas being transferred directly to the material in the bed, dividing gas flowing upwardly from the top of said bed into one fraction which is the gas manufactured and another fraction which is reflow gas, said reflow gas comprising the water vapor, gaseous hydrocarbons, and said additional gas produced in the combustion zone, forming a cavity within said bed in the combustion zone thereof, and contacting the material in said bed in said combustion zone with the reflow gas together with air for the support of combustion, the air and reflow gas before contacting such material initially being mixed in said cavity to produce a mixture comprising air, water vapor and gaseous hydrocarbons, the combustion zone being maintained at a temperature above about 1300° F. and below the fusion temperature of the ash of said material, said additional gas produced in said combustion zone comprising the gas combustion product produced by the exothermic reaction of char with oxygen supplied by the air and water gas produced by the endothermic reaction of char with water vapor in a water-gas reaction, the top of said bed being maintained at a temperature no higher than the boiling point of water at the pressure condition existing in the reactor.
Claim 2
Dependent Claim
352 words
A process for making conbustible gas from lignocellulose material which comprises establishing a descending bed of such material in a descending bed reactor, newly introduced material being dropped onto the top of such bed and such newly introduced material having a moisture content within the range of 20% to 80% by weight, said descending bed having adjacent the top thereof a drying zone wherein the material is dried with the production of water vapor, and progressing downwardly from the drying zone a distillation zone where the material is converted to gaseous hydrocarbons and char, and below the distillation zone a combustion zone where the char is reacted with the production of additional gas and residual ash, channeling the ash and all of the gas as such is produced in said bed upwardly through and thence out the top of the bed with the sensible heat of such gas being transferred directly to the material in the bed, dividing gas flowing upwardly from the top of said bed into one fraction which is the gas manufactured and another fraction which is reflow gas, said reflow gas comprising the water vapor, gaseous hydrocarbons, and said additional gas produced in the combustion zone, forming a cavity within said bed in the combustion zone thereof, and contacting the material in said bed in said combustion zone with the reflow gas together with air for the support of combustion, the air and reflow gas before contacting such material initially being mixed in said cavity to produce a mixture comprising air, water vapor and gaseous hydrocarbons, the combustion zone being maintained at a temperature above about 1300° F. and below the fusion temperature of the ash of said material, said additional gas produced in said combustion zone comprising the gas combustion product produced by the exothermic reaction of char with oxygen supplied by the air and water gas produced by the endothermic reaction of char with water vapor in a water-gas reaction, the top of said bed being maintained at a temperature no higher than the boiling point of water at the pressure condition existing in the reactor.
Claim 3
Dependent Claim
347 words
A process for making combustible gas from lignocellulose material which comprises establishing a descending bed of such material in a descending bed reactor, newly introduced material being dropped into the top of said bed, and such newly introduced material having a moisture content within the range of 20% to 80% by weight, said descending bed having adjacent the top of the bed a drying zone where the material is dried with the production of water vapor, and progressing downwardly from the drying zone a distillation zone where the material is converted to gaseous hydrocarbons and char, and below the distillation zone a combustion zone where the char is reacted with the production of additional gas and residual ash, channeling the ash and all of the gas as such is produced in said bed upwardly through and thence out the top of the bed with the sensible heat of such gas being transferred directly to the material in the bed, dividing gas flowing upwardly from the top of said bed into one fraction which is the gas manufactured and another fraction which is reflow gas, said reflow gas comprising the water vapor, gaseous hydrocarbons, and said additional gas produced in the combustion zone, and introducing air and reflow gas into said reactor at said combsution zone with initial combining of the air with the water vapor, gasous hydrocarbons and said additional gas in said reflow gas substantially at the time of entering the reactor and before such gas mixture contacts the material in the bed, the combustion zone being maintained at a temperature above about 1300° F. and below the fusion temeprature of the ash of said material, and the top of said bed being maintained at a temperature no higher than about the boiling point of water at the pressure condition of the reactor, said additional gas produced in said combustion zone comprising the gas combustion product produced by the exothermic reaction of char with oxygen suppled by its air and water gas produced by the endothermic reaction of char with water vapor in a water-gas reaction.
Claim 4
Dependent Claim
347 words
A process for making combustible gas from lignocellulose material which comprises establishing a descending bed of such material in a descending bed reactor, newly introduced material being dropped into the top of said bed, and such newly introduced material having a moisture content within the range of 20% to 80% by weight, said descending bed having adjacent the top of the bed a drying zone where the material is dried with the production of water vapor, and progressing downwardly from the drying zone a distillation zone where the material is converted to gaseous hydrocarbons and char, and below the distillation zone a combustion zone where the char is reacted with the production of additional gas and residual ash, channeling the ash and all of the gas as such is produced in said bed upwardly through and thence out the top of the bed with the sensible heat of such gas being transferred directly to the material in the bed, dividing gas flowing upwardly from the top of said bed into one fraction which is the gas manufactured and another fraction which is reflow gas, said reflow gas comprising the water vapor, gaseous hydrocarbons, and said additional gas produced in the combustion zone, and introducing air and reflow gas into said reactor at said combsution zone with initial combining of the air with the water vapor, gasous hydrocarbons and said additional gas in said reflow gas substantially at the time of entering the reactor and before such gas mixture contacts the material in the bed, the combustion zone being maintained at a temperature above about 1300° F. and below the fusion temeprature of the ash of said material, and the top of said bed being maintained at a temperature no higher than about the boiling point of water at the pressure condition of the reactor, said additional gas produced in said combustion zone comprising the gas combustion product produced by the exothermic reaction of char with oxygen suppled by its air and water gas produced by the endothermic reaction of char with water vapor in a water-gas reaction.
Claim 5
Dependent Claim
52 words
The process of claim 2 which comprises forming a cavity within said bed in the combustion zone thereof and the initial mixing of the air with the reflow gas including its water vapor, gaseous hydrocarbons, and said additional gas is performed in said cavity before the gas contacts material in said bed.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-08-13 | 1983-02-12 | 1983-08-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-08-13 | 1987-02-12 | 1987-08-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-08-13 | 1991-02-12 | 1991-08-14 | $7700.00 | Window Closed / Lapsed |