TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: In the method: the irradiation step is performed in the presence of cellulose or cellulose derivative, carbon compound, and/or water; step (c) is performed in the presence of a hydrocarbon or a mixture of hydrocarbons; step (d) is performed in the presence of a hydrocarbon or a mixture of hydrocarbons, and/or an oxidizing agent; and/or step (e) is performed in the presence of an organic acid solution of 5-40%, and/or a solid metal, and/or an iron sulfate solution of 5-50%. The method, further comprises: separating the coal, asphalt, liquid hydrocarbon, organic acids and/or methane and hydrogen obtained in steps (b), (c), (d), (e) and (f), respectively from the residual materials in gaseous state; precipitating inorganic substances comprising sulfur, chlorine, phosphor, bromine and/or boron and heavy metals during steps (b), (c), (d) and/or step (e), using alkali-reagents which are added to the reaction mixture; and performing thermal reduction of water between step (e) and (f). Preferred Components: The waste material comprises at least 50% of organic material, plant leaves and branches, fruit peel, husk and shells of cereals and oilseeds, food leftovers, spurge, Jatropha curcasplant and/or sugar cane bagasse, vegetable refuse comprising tobacco, cotton, sawdust or shaving, and/or all waste from the timber industry, and/or all other organic waste from agro-industrial waste, pruning waste, weeds and/or all types of vegetable rests, solid waste of animal origin comprising bones, manure, solid waste from the meat industry and/or any other type of waste of animal origin, plastic, paper, rubber, tires, natural and synthetic fabric, latex, diapers and/or disposable towels. EXAMPLE - Municipal solid waste residues (comprised of paper, cardboard, newspapers, magazines, cardboard packaging, paper containers (38 kg), organic remains (72 g), textiles, clothing, apparel and home decorative items (12 kg), waste from street cleaning, parks, playgrounds and beaches (34 kg), dead pets and furniture (8 kg), wood in the form of furniture and boxes (6 kg), and plastics (30 kg)) (200 kg) was loaded into the RMO apparatus. Then the implementation of the photon radiation was monitored using meters measuring the internal temperature of the material. Gasification was initiated at a pressure of 1-15 bar, showing a peripheral temperature of 207.5 degrees C of the material, this temperature was increased by applying infrared photon radiation at a rate of 10.4 degrees C/minute on average for the first hour of the process and the increase was more rapid initially (21 degrees C/minute for the first 12 minutes). The internal pressure of the system was also increased slowly with increasing temperature. The process preceded simultaneously in all reaction vessels of the RMO apparatus. An internal pressure of 1.034 bar was registered. As the first product a gaseous mixture of a combustible gas was produced (comprised of carbon monoxide 48%, water vapor 23% and air 29%), during the first 10 minutes, was used as feedback to the burners in a mixture of one volume part of gas poor in methane and three volume parts of gas rich in methane gas. 8 minutes after the start of the process, precipitation of discharged acid from reaction vessel (e) was observed. After 16 minutes the start of the process the first discharge of liquid hydrocarbon in reaction vessel (d) was observed. The discharge rate of liquid hydrocarbon also gradually increased. 53 minutes after the start of the process discharge of fluid asphalt from reaction vessel (b) was initiated. Meanwhile discharge of acid and liquid hydrocarbon reached and maintained at peak level. At this time, the organic starting material has a uniform temperature of 835 degrees C. The pressure inside the system reached its maximum value in this process of 1.077 bar. From this moment the external application of energy for the process was slowed down. The discharge of asphalt production still increased while the discharge of other products gradually reduced. The discharge of gas was reduced to a minimum while discharge of the other products continued. The pressure inside the system was recorded its lowest value in this process of 1.029 bar. At the bottom of the reaction vessel of phase (b) water vapor at a rate of 1 m 3/minute for 10-15 minutes was introduced while the burner was stopped to let the heat of the waste generate gases e.g. hydrogen and carbon dioxide. This speeded up the discharge of asphalt, acids and liquid hydrocarbons of organic material, which was then charred and the temperature was gradually reduced from the 835-400 degrees C. The discharge was obtained from the three precipitators. The discharged gas was at this moment determined to be hydrogen and carbon dioxide and high amounts of methane. The process ended when a temperature of 400 degrees C was registered. At this point the injection of water vapor was stopped. The vessel containing the coal was extracted and this vessel was cooled for 4 hours before discharge. At this time the RMO apparatus is available for the start of a new process by introducing a new vessel loaded with a new organic matter.