The relatively moist biomass – 60 % moisture content is introduced through a gas-tight rotary feeder at the top right in the carburetor. There, the biomass in tubes is where snails run brought to dryness. The resulting water vapor is introduced directly into the process and reacted in the hotter pipes below the formation of hydrogen and methane. So it is not necessary to pre-dry biomass with a lot of energy to make then react with energy- consuming also specially produced steam. In this respect the Hagalis steam reformer is much more energy efficient system for finger, than comparable investments. A screw, the degassed material charcoal is introduced into the multi-stage filter. There she met your second Task: cleaning the wood gas by the high surface formation. Activated carbon is also formed and characterized by a high absorption capacity. So binds the activated carbon tars and residues from the raw gas while it comes to the gas methanation by the hydrogen reacts with the carbon. The methane content is considerably increased. For electricity generation in CHP ‘s necessary and leads to a less problematic combustion . Pure hydrogen is to be obtained, the filter is assembled with other materials. The charcoal from the filter is then introduced into the combustion chamber, and completing its third Purpose: The supply of allothermic gasification process with thermal energy . Finally, just clean ash remains, which can be easily used as fertilizer. It is a novel gasification of carbonaceous biomass in the process heat is supplied from the outside. There is a steam reformer in which steam is used for drying the biomass, the steam reforming. Thus it is possible from a high- carbon- biomass synthesis gas (SNG) to produce for renewable energy. Since the inner combustion reactor, there is no process for the production of heat, and no combustion air is injected , and thus almost no nitrogen enters the gasification process . In the combustion air contains 78.1% nitrogen that would otherwise be added to the synthesis gas as a ballast so that the gas for the gas is low. Extensive measurements with a gas chromatograph have shown that with this method, a high-energy, tar-free synthesis gas SNG can be produced. The measurements before the patented filter are: H2 = 46.3 vol % CO = 21.7 % by volume CH4 = 14.2 vol % CO2 = 16.5 vol % N2 = 1.3 vol % The calorific value has reached a Wobbe index from 3.1 to 3.3 kW/m3 . In the steam reformer is a double spiral circulation reactor. The resulting purified gas is fed to the cogeneration system directly via a gas control unit and the high-efficiency gas engine then generates electricity and heat. Simultaneously represents in the gas production process heat is available for the bottom part in which the combustion and supply of the carburettor takes place with thermal energy in an air stream , is water-cooled. The heat generated there is as much as the engine exhaust and the exhaust heat from the CHP for heating and process heat available. This represents a total of the high efficiency and the superior efficiency of the system with 90 %