Abstract: The apparatus includes a reaction chamber which in operation uses an organic fuel input, typically in the form of substantially uniform-sized pellets, to produce a tar-free fuel gas. Prior to initiating operation, the lower end of the reaction chamber is filled with a charge of charcoal, forming a charcoal bed. A portion of the charcoal bed is then ignited, typically near the top, with air from the atmosphere being drawn substantially uniformly down through the reaction chamber by a pump on the outlet line leading from the reaction chamber, creating a thin pyrolysis zone near the top of the charcoal bed. The substantially uniform-size fuel pellets are added to the top of the charcoal bed, and are pyrolized as they move down through the pyrolysis zone.

Abstract: In the method, organic, i.e. carbon-containing, material, such as straw, wood chips, sawdust, or dead bacterial waste from a sewage treatment plant, is heated in a pyrolytic reactor, thereby driving off volatiles from the organic material, including hydrogen and carbon monoxide gases, water vapor, and tars, while leaving charcoal (char) behind. The volatiles are then passed over a base material, such as hot char, which is at a temperature substantially above the pyrolizing temperature, e.g. 950.degree. C. and above, which causes a chemical reaction of the tars and volatiles, resulting in an output of a gaseous mixture consisting largely of carbon monoxide and hydrogen, characterized by an absence of tars. The apparatus includes a pyrolytic reactor in which an initial charge of charcoal is located. An inlet is provided for introduction of the organic material and an exit is provided for the resulting gases and ash products.

Abstract: The apparatus includes a pyrolytic reactor in which an initial charge of charcoal is located. An inlet is provided for introduction of the organic material and an exit is provided for the resulting gases and ash products. The reactor is arranged to permit a continuous flow of organic material volatiles, and char through the reactor, resulting in continual replenishment of organic material in the pyrolizing portion of the reactor, and replenishment of the charcoal bed portion by the char produced from the pyrolysis reaction. The reactor vessel is heated to the correct temperatures by means such as electric heating coils or hot air/flame jackets.