TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The process involves converting the fed waste to syngas comprising carbon monoxide, carbon dioxide and hydrogen at a bed temperature of 1000 degrees C, by injecting oxygen at a pressure of 0.9-2 bar and water vapor derived from drying and pyrolysis in the reactor space. The process involves applying a temperature of 650 degrees C in the reactor removing hydrohalides; injecting hydrocarbon containing liquid wastes into the reactor space of the generator for controlling temperature; injecting powdered wastes of high carbon content into the pyrolysis reactor space of the generator for controlling temperature; ensuring the electric energy needed for the operation of the system by utilizing a part of the purified gases in the gas motor; isolating the carbon dioxide content of the raw syngas by an absorption desorption process, storing it in liquid state and converting it to methanol by adding hydrogen; and carrying out the methanol synthesis in a catalytic reactor at a pressure of 15-75 bar and at 100-260 degrees C. EXAMPLE - A waste flow comprising 10% of sludge (30% of dry material), 70% of organic communal waste and 20% of harvest loss of forest felling site was fed to a low gas inverter generator having an upper filling hole, the bed temperature of which was 1000 degrees C. Into the upper level of the hot layer oxygen of a purity obtained by the electrolysis of water, amounting to 30 m/m% of the raw material flow was introduced. The volume of the generator was 50, the ratio of height and outer diameter was 4:1. The diameter of the inner pyrolysis zone was 75% of the outer diameter. The hydrochloric acid vapors were bound by transferring same from the exhaust gases through a calcium-carbonate-filled column by inner feeding, where after the water vapors were condensed by air cooling. Due to the small size a lux mass was applied for the removal of hydrosulfide. The purified crude gas was washed with potassium hydrogen carbonate solution at a pressure of 50 bar in a column filled with Raschig rings, and it was then reacted after drop separation by passing it through tubes of a temperature of 150 degrees C thermostated with an oilbath, filled with a catalyst having an inner diameter of 5 mm. The reaction product was condensed by cooling. The catalyst was a mixture of potassium methyl carbonate applied on an alumina carrier and transitory metal-methyl carbonates. The obtained methanol was 35% of the weight of the charged material, its water content amounts to less than 1%. The uncondensed gases were burnt.