TECHNOLOGY FOCUS - BIOTECHNOLOGY - Preferred Process: In the procedure (I), the cooking process is carried out in a vacuum at 250-400 degrees C in the oven. One third of the smoke gas (present outside of the oven) is burned under the addition of oxygen and less addition of one or more materials of propane, butane and alcohol at above 1200 degrees C. Two third of the collected gases are conducted through an iron-cesium-catalyst, which absorbs the cyanide compounds and eliminates nitrogen and carbon dioxide. The gases emerging, after burning process, is oxidized by the Lavoisier-procedure and the remaining gases with portions of nitrogen and carbon dioxide are obtained. The GRP-pieces, after the cooking process, are mechanically reduced to granulates, preferably by shredding, where the granulates exhibit a particle size of 6 to 10 mm (diameter), preferably a diameter of 6 to 7 mm. The granulates are subjected to a fermentation process in a reactor under the addition of water, a fat containing nutrient, preferably glycerin and bacterial strains. The granulates, bacteria in the substrate and the nutrient in the reactor are mechanically pressed with circulating pumps by baffle plate that is arranged on the upper part of the reactor, to collect metabolic gases of the bacteria, like hydrogen and nitrogen, and optionally nutrient is provided to the substrate to prevent over acidification. The residence time of the existing suspension in the reactor amounts to 45 to 75 days, preferably 60 days at approximately 40 degrees C, preferably 38 degrees C, so an adaptation of the bacterial strains at this conditions of the reactors is achieved. The procedure for fermentation is an aerobic procedure. In the procedure (II), Archaebacteria of the family Methanobacterium, Methanosarcina, Methanospirillum, Methanococcus and Methanosaeta are added to the suspension. The methane gas is generated from the granulates of the suspension, which consists of hydrocarbon compounds. Nitrogen is fed into the anaerobic reactor for the displacement of the atmospheric oxygen. The anaerobic-reactor is: equipped with glass fiber lattice to absorb residues, which are break down by the bacterial splitting of the plastic granulate and to provide the Archaebacteria adhesion possibility; and kept in motion when the suspension using the circulating pumps. The mesh size of the lattice fabric corresponding to the granulate size amounts to 5 mm x 5 mm to 10 mm x 10 mm and the flow velocity of the suspension is 0.175 cm3/h. The mud settled at the bottom of the reactor is analyzed continuously for portions of hydrocarbon and the substrate is fed again until no hydrocarbons are detectable. In the procedure (III), the basin is surrounded with plate glass, which permits the light in the angle of 30 to 45 degrees into the basin. The water-/mud mixture is inoculated with green alga of the species Cladophora vulgaris and Cladophora rivularis. The water-/mud mixture is kept in slow, but constant motion by a bottom agitator of the basin, preferably with a flow velocity of maximum 0.002 cm3/hour. A part of the biomass with adhering solid material is dried and is burned with methane gas to cinder, where the biomass serves as additional fuel and the other part of the biomass serves as a basis for the further growth of algae. The cinder production is initiated by combustion of waste carbon dioxide to accelerate the growth of algae in the basin. The waste heat emerging during the cinder burning is used for hot water circulations for keeping a moderate temperature of the basin and the reactors and electricity is generated, in which a part of the methane gas is burned in an Otto-engine, which runs a generator. The substrate is inoculated with the algae as well as protozoa and metazoa of the family Viridiplantae, Trebouxiophyceae and Mesostigma and with small aquatic plants, like Volvox aureus and Cladophora linnaei. The spiral towers are built around the translucent double chamber plates, which are occupied with filter foils. The double chamber plates serve as the thermal separation of the spiral towers. The filter foil allows the light passage at a wavelength from 360 to 720 nanometers. The suspension is introduced through a slow running hose pumps with a flow movement of 1.5 m per 24 hour. The carbon dioxide gas in the suspension is combusted directly under the hose pumps. The formation of the biomass with the algae and aquatic plant is influenced by factor 7, where for optimizing at this entry point, additionally nutrient (e.g. calcium- and phosphorus compounds) can be provided in the suspension. In the procedure (IV), photosynthetically produced oxygen is obtained, in which a tube piece of same diameter is used intermittently from 2 to 3 m of the tube stretch, in which plastic baffle is located. The tube pieces are closed at an exhaust device, which delivers the oxygen either to the surrounding or collected in the corresponding containers. The produced biomass is decreased after approximately 8 to 10 days in the upper end of spiral tower and can be easily centrifuged, where the substrate occurring at the same time is fed in the spiral towers as liquid phase, at the same time the biomass can be feed directly either as fertilizer, fodder or as sources of energy in the anaerobic reactor for the production of methane gas. In the procedure (IV), for optimizing the binding, a LED-guard post with LED's, which produces the wavelength of 360 to 720 nanometers, is positioned centrically within the spiral tower and emitting light in all sides, where e.g. the electric stream is used. Preferred Components: The bacterial strains are Clostridium, Micrococcus, Pseudomonas and Ruminicola Bacter. EXAMPLE - No suitable example given.