NOVELTY - Making low-tar syngas from organic wastes and optionally converting to methanol/making methanol from separated carbon dioxide involves introducing raw material (1) comprising solid communal waste, sludge and/or biomass waste into double-flow one-body generator comprising inner pyrolysis zone (2), oxidation zone (5) and reduction zone (6); converting obtained coke, water and tar formed using heat content of gas flowing upwards in outer gas space by blowing oxygen into fix bed, to raw gas (9) comprising carbon dioxide; and removing and converting it to methanol (15) using hydrogen source.    USE - For preparing low-tar syngas, from organic wastes and optionally converting the syngas to methanol; and for preparing methanol from the separated carbon dioxide (claimed). The obtained syngas is suitable for the preparation of Fischer-Tropsch fuel or other carbon monoxide or hydrogen based synthesis.    ADVANTAGE - The process prepares syngas with less energy and costs by eliminating the disadvantages of prior art such as unequal retention time in the fluid-bed reactors. The process involves heat degradation of the biomass type materials, and thus water is split off. Consequently water is available in the reactor system without direct adding water. When preparing the raw material, the pre-drying composition, generates appropriate water vapor amount needed for the water gas reaction. The obtained syngas is utilized in a special process for the preparation of methanol. In the process, both from the formed syngas and from the carbon dioxide removed from the reaction mixture, methanol is produced by using an external hydrogen source. The process results in a useful carbon proportion greater than one, even if a part of the syngas would not be used for the preparation of electric energy, by which via electrolysis we can prepare pure oxygen needed for achieving the high bed temperature in the generator and also prepare hydrogen needed to adjust the carbon monoxide and hydrogen ratio. A further advantage of the system is, that at the blowing level of the generator dangerous waste hydrocarbons and water contaminated with hydrocarbons can be introduced serving as a base.    DETAILED DESCRIPTION - Preparing low-tar syngas, from organic wastes and optionally converting to methanol or preparing methanol from separated carbon dioxide involves introducing secondary raw material (1) comprising solid communal waste, sludge and/or biomass waste into a double-flow one-body generator comprising an inner pyrolysis zone (2), oxidation zone (5) and reduction zone (6); converting obtained pyrolysis coke, pyrolysis water and tar formed by the aid of the heat content of the gas flowing upwards in the outer gas space by blowing oxygen into the fix-bed, to a raw gas (9) comprising carbon dioxide, carbon monoxide and hydrogen, on the fix bed of the pyrolysis coke at 600-1200 (preferably at 1000) degrees C and optionally a liquid containing liquid hydrocarbons or a powder of high carbon content are added in order to control the temperature, and hydrohalides are removed from the obtained raw syngas on a calcium carbonate bed at 200-700 degrees C, the heat content of the raw syngas is utilized, carbon dioxide is removed by a method known per se, and carbon dioxide is converted to methanol (15) by using an external hydrogen source and optionally the obtained syngas is also converted to methanol by a method known per se.    DESCRIPTION OF DRAWING(S) - The figure shows a view of the process for producing low-tar syngas from organic wastes.    Feed of the waste mixture (1)    Pyrolysis zone (2)    Oxidation zone (5)    Reduction zone (6)    Crude syngas (9)    Pure methanol (15)