TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The conductive carrier is constituted by a molten metal such as tin, bismuth, zinc, lead and aluminum and/or their alloys with catalytic metals constituted by iron, nickel, chromium, manganese, cobalt and titanium, and by concentrated irradiation devices such as microwaves, radio frequency and/or power laser suitable for reconverting the oxides formed in the metals. The catalysts used for the production of multi-wall carbon nanotubes are metallo-organic compounds such as ferrocene and inter-metallic compounds obtained from lanthanum, neodymium and nickel carbonates. The additives and/or catalysts used for torrefaction comprise calcium oxide, calcium carbonate, potassium hydroxide, dolomite, peridot, zinc oxide, manganese oxide, copper oxide, iron (III)-oxide, magnesium oxide and/or magnesium carbonate, oxides or hydroxides of alkaline and/or alkaline-earth metal and/or 1-6C alcoholates of alkaline and/or alkaline-earth metal. The catalysts for the syngas production are filling bodies with high surface and based on nickel, chromium, manganese, iron, cobalt, titanium and/or their alloys. The biomass is subjected to pyrogasification to produce syngas to be used as energetic or bio-energetic vector in a cogeneration and combined heat and power group and/or to be converted into bio-liquid in the modules for converting gas to liquids by Fischer-Tropsch process for the conversion of the carbonaceous matrix. The carbonaceous matrix is extracted from oils and/or essences and/or active principles and/or biogenic intermediates such as cellulose and lignin form plants and/or hydrocarbons and organic pollutants.    TECHNOLOGY FOCUS - INSTRUMENTATION AND TESTING - Preferred Components: The basic module includes chambers with a concentrated irradiation device such as ultrasounds, microwaves, radio frequency, electromagnetic and/or power laser. An opening is made in the stationary head for allowing the passage of a liquid making the conductive carrier from inside of the reactor towards a hollow space defined between the casing and the reactor. The head fixed to the reactor has a friction member passing leak-proof through an end flange of the casing, and a heat-exchanger or a cathode extending within the reactor that is inserted within the friction member. The portion of the casing close to the head fixed to the body of the rotating reactor is provided with interfaces suitable for allowing the exit of the converted matrices. A thermo-stating fluid produced by the combustion of a fraction of the matrix or products derived from the matrix flows into the chamber, which is contiguous to a part of the external wall of the casing, where the plant is energetically auto-sustained. The basic modules have same or different application configuration, are operating in different conditions and interconnected in series or in parallel, include a further module, and arranged within a container. The controlled feeding module is provided with a unit for drying and mixing the solid matrices and a unit for expelling the matrices. The expulsion unit comprises an Archimedean screw with variable pitch, or a pusher device provided of a driving mechanism such as a rod/crank mechanism, a piston or a pinion/rack mechanism. The basic module is suitable as a thermochemical conversion reactor for performing processes of torrefaction or flexible pyrolysis in hyper-dynamic and catalytic conditions by internal members with the addition of additives and/or catalysts at a temperature of 850-900 degrees C and gasifying at 600-1200 degrees C and suitable as a fuel cell. The further basic module is: arranged downstream of the first basic module; suitable for conducting a sub-stoichiometric oxidation process of the matrix converted in the first basic module, where vapors and gases produced by the basic modules are fed to a third basic module; and suitable for producing multi-wall carbon nanotubes by doublestage catalytic conversion of syngas at a temperature of 750-900 degrees C using catalysts. The modules convert the vapors and gases in hyper-dynamic and catalytic conditions with auto-cleaning of the catalytic fluid bed in the presence of metal spheres. The further module is also suitable for biochemically converting carbonaceous matrices produced in the first and second basic modules with contemporaneous production of primary algae biomass to be re-converted in the modules that constitute a closed loop and bring about a global emission balance, which is low or nil, using a tube photo-bioreactor for integrally reconverting gaseous emissions such as carbon dioxide, nitrogen oxide, solid particulate and micronutrients with electro-biostimulation and targeted inoculation of micronutrients with chelating agents in the units placed in the container. The anode is constituted by the molten metal and the cathode is a tube bundle of ceramics material such as yttria stabilized zirconia (YSZ) with the surface layer of nickel (Ni) alloy such as Ni-YSZ, within which hot air is blown. The physical decontamination, depolarization, dehalogenation and detoxification of halogenated compounds such as polychlorinated biphenyls and further halogenated persistent organic pollutants and corrosive acid and sulfurated compounds is effected in a temperature of 80-100 degrees C under vacuum and with the help of reactive and/or adsorbing particle supports such as silicates or alumino-silicates with a size of 0.1-5 mm and weight ratio of 50-70%.