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US 4,164,397 AGranted
Fuel gas production
OwnerHerbert H. Hunt, Harold S. Worcesterinventors
Life of this patent
Estimating the term…
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.
Claims3
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.degree. 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.
4 more elements
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.degree. 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.
2 more elements
Dependencies are inferred from the claim text.