NOVELTY - Raw material and fuel from wastes are treated in monotubular reactor, with descending flow. The materials are then introduced into the reactor gasification area. Gasification residue is discharged in powdery form or subjected to vitrification. Syngas obtained by gasification is sent for cleaning and multi-stage separation is performed to obtain hydrogen and carbon dioxide with purity higher than 99%.    USE - The method is useful for production of pure syngas e.g. hydrogen and carbon dioxide.    ADVANTAGE - Hydrogen and carbon molecules of high purity are obtained by effectively utilizing industrial and municipal wastes which are not recyclable. The process is economical, safe and avoids atmospheric pollution. The differential pressure system prevent atmospheric air from entering the reactor and also prevents the syngas inside the reactor from coming out and spreading into the atmosphere. The method is performed in a short time. The gasification area of the reactor provides fast gasification with maximum performance. The method allows a double possibility of discharge.    DETAILED DESCRIPTION - Liquid, muddy or solid raw materials, either produced for the purpose or from industrial processes, in which they are not recyclable, fuels from wastes or biomass, are treated in the feeding section of a vertically oriented monotubular reactor, having descending flow with differential pressure system. The materials are subsequently introduced into a gasification area of the reactor without entraining external air and with the raw material size inversely related to the thickness. Raw material in the gasification area undergoes gasification in reducing atmosphere, at a working temperature regulated by a changeable thermal profile obtained through a series of torches located along the gasification area, each coupled at 180 degrees C from the other.    Physical-chemical characteristics of the feed raw material ranges between 350-1200 degrees C, respectively in the upper and lower ends of the gasification area. The gasification residue, in powdery form is collected at the reactor bottom in a discharge area which either functions as a final oxidation chamber or as an oxidation chamber and melter with subsequent vitrification of the residue through cooling in water.    Syngas obtained by the gasification process is sent for cleaning and a multi-stage separation treatment is performed to obtain hydrogen and carbon dioxide with purity higher than 99%.    An INDEPENDENT CLAIM is included for a reactor for carrying out fast thermal gasification of raw materials.    DESCRIPTION OF DRAWING(S) - The figure shows the production process of pure syngas.