Abstract: Apparatus for producing synthesis gas from a biomass feed in a closed, helical coil reactor utilizing a heat source such as a natural gas burner. The reactor includes the helical coil disposed in a reactor vessel with the heat source positioned toward a bottom of the reactor vessel. A heat shield is preferably disposed within at least an upper section of the helical coil, and the coil is placed adjacent to, but spaced from, a sidewall of the vessel so that convective heat may flow upwardly and around the individual coils of the helical coil. A lower section of the helical coil is preferably exposed to direct heat from the heat source. This lower section may exhibit a coil diameter that is greater than a coil diameter of the upper section. The biomass feed may be supplied to the helical coil from a mixing chamber including a spiraling screw valve.

Abstract: The present invention relates to an improved apparatus and method for conveying fibrous, solid and slurry materials, such as granulated wood, rice hulls, chopped cane and the like, to a pressurized vessel, wherein the material being conveyed is compacted in the feeder in a controlled manner to create a seal at the feeder exit into the pressurized vessel whereby the processing pressure in the vessel is maintained. The invention is particularly useful when used in conjunction with a biomass reactor for the production of gas selectively rich in hydrogen and carbon containing components, such as carbon monoxide, carbon dioxide and methane, which in turn, may be converted into a select end product fuel, such as methanol or ethanol or used as a feed gas for an industrial power plant, such a the biomass reactor for producing gas.

Abstract: Apparatus for producing synthesis gas from a biomass feed in a closed, helical coil reactor fired by at least a natural gas fed burner. The reactor includes the helical coil disposed concentrically in the reactor vessel with a burner positioned at the bottom of the vessel and a generally cylindrical heat shield, with the bottom end (facing the burner) being closed at the top of the vessel. The heat shield is concentrically disposed within the coil, and they are placed adjacent to, but spaced from, the sidewall of the vessel so that convective heat may flow upwardly and around the individual coils. The lower section of the coils are exposed tot he direct heat of the burner. The placement of the burner and heat shield provide respective heating zones to facilitate and control the heat supplied to the biomass for pyrolysis, reduction of char and bringing the target synthesis gas to equilibrium.