H13 MULTI-MODE VORTEX PYROLYSIS REACTOR. Figure 1. Figure 1а LEGEND. I. RDF (refuse derived fuel),

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1 MULTI-MODE VORTEX PYROLYSIS REACTOR Figure 1 2 LEGEND I. RDF (refuse derived fuel), 1 7b V SRF (solid recovered fuel), Biomass. Air. Steam IV. ННО (oxyhydrogen) - gas V. Steam-gas mixture VI. Solid residue I 6 IV 5 7a 8a 8b 3 10 IV Body of the pyrolysis reactor 2. Exit of the pyrolysis steam-gas mixture 3. Vibrating grate 4. Slide valve at the exit of the reactor 5. Entrance for RDF, SRF, Biomass 6. Slide valve at the entrance of the reactor 7а, 7б. Steam-air nozzle 8а, 8б. Burners for ННО - gas 9. Recirculation pipe 10. Steam-gas injector 11. Steam nozzle 12. Steam-air nozzle 12 4 VI 5 Figure 1а I

2 MULTI-MODE VORTEX PYROLYSIS REACTOR I. Purpose pyrolysis of RDF, SRF and waste biomass, with each one of the said fuel - alone or mixed in different proportions.. Working mode:.1. Fast pyrolysis for predominantly production of bio oils - (55-60) % from the mass of the raw material. They are chemically stable, with low acidity рн (4,0 % - 5,0%) and high calorific over 35 MJ/kg..2. Gasification, with main purpose - obtaining a maximum quantity synthesis gas with high calorific value (16 18) MJ/m Mixed mode - to produce the maximum quantity of combustible vapors and gases over 85% and minimum quantity solid residue.. Technical parameters:.1. Pyrolysis initiating agents: superheated steam, HHO gas, air (only for the initial restart and absolute necessity).2. Terms of pyrolysis: in moving vortex bed with medium intensity - in the middle and the top parts of the reactor and in a vibration-bubbling bed and fixed bed in the bottom part of the equipment.3. Consummation of RDF, SRF and/or biomass - ( ) kg/h. The raw material might be with humidity up to 50%. Prior being fed into the facility it is crushed..4. Thermal efficiency of the reactor: (91 93)%..5. Processes of: fuel supply, pyrolysis/gasification, evacuation of the solid residue, production of HHO-gas, superheated steam and etc. are managed by digital, automated management system.

3 MODULE FOR PRODUCTION OF HOT FUME GASES Figure 2 V V I V 7 IV IX V V 4 VI VI 9 LEGEND I. RDF, SRF, Biomass. Air. Steam IV. ННО - gas V. Steam-gas mixture VI. Solid residue V. Water V. Hot fume gases IX. Hot fume gases + steam 1. Pyrolysis reactor 2. Shredder 3. Screw conveyor 4. HHO gas generator 5. High pressure fan 6. Steam-air injector 7. Vortex insinerator 8. Steam generator with steam superheater 9. Container for solid residue

4 MODULE FOR PRODUCTION OF HOT FUME GASES.4. Automated system for control of the processes pyrolysis and burning.. Technical parameters:.1. Quantity of processed RDF, SRF and/or biomass: ( ) kg/h. I. Purpose neutralization of RDF, SRF and/or waste biomass and utilization of their energy potential trough pyrolysis and burning of the received steam-gas mixture till receiving hot and environment friendly gases. The equipment can replace burners at natural gas, fuel oil, naphtha and etc. at the entrance of the existing boilers which are working at fossil fuels or waste wood.. Module components:.1. Vortex pyrolysis reactor for pyrolysis of waste fuel up to burning of the produced steam and gas. The reactor is equipped with: Crusher for the fuel Screw feeder Generator for HHO-gas.2. Vortex incinerator for burning of the pyrolysis steam-gas mixture up to hot fume gases. It is integrated with steam generator with a superheater. It produces the necessary for the module working, superheated water steam..3. Steam-air injector with a fan for high pressure. It is used for downloading the pyrolysis steam and gases from the reactor and passed them with high speed, tangentially to the cylindrical wall of the incinerator. The injector is also used to deposit the necessary quantity air for the complete burning on the steam-gas mixture..2. Heat energy carried by the hot flue gases at the exit on the module: ( ) KWh..3. Thermal efficiency about 90%.4. Temperature of the flue gases at the exit of the incinerator: C..5. Flow of the flue gases at the exit average 7200 m 3 /h..6. Burning process in the incinerator vortex with a combustion time over 4 sec. and working temperature up to С. IV. Profit of realization on the established by the Module for the production of hot flue gases, heat energy not less than 50 EURO per tonne of fuel from waste. V. Deadline for return on investment up to 2,5 years.

5 COGENERATION UNIT Figure 3 V 14 V I V 13 V 2 IV V 5 6 IX X VI VI X X X 7 V X Електричество Ф1 Ф2 Ф3 XI LEGEND I. RDF, SRF, Biomass. Hot air. Superheated steam IV. ННО - gas V. Steam-gas mixture VI. Solid residue V. Cold water V. Hot fume gases IX. Hot fume gases + steam X. Hot water XI. Cold air X. Ash 1. Pyrolysis reactor 2. HHO gas generator 3. High pressure fan 4. Steam-air injector 5. Vortex insinerator 6. Gas-air heat exchanger 7. Heat exchanger air-air 8. Hot air turbine 9. Compressor 10. Electric generator 11. Heat exchanger fume gases-water 12. Filter for fine purification and chemical treatment 13. Draft fan 14. Chimney

6 COGENERATION UNIT I. Purpose neutralization of RDF, SRF and/or waste biomass and using of their energy potential for common production of heat energy and electricity.. Components of cogeneration unit:.1. Module for the production of hot flue gases by pyrolysis of RDF, SRF and/or biomass and burning the received steam and gases in vortex incinerator..2. Gas-air heat exchanger. In there the hot flue gases with temperature С, heat the air. The temperature of the air at the entrance of the gas-air heat exchanger is about С, and at the exit it is within С С..3. Turbo-shaft, gas-turbine engine, which works as a Turbine with hot air. The compressor of the engine sucks and compresses cold atmospheric air. The compressed air is fed into a heat exchanger air-air, where it is heated further. From there it enters into the described gas-air heat exchanger, where its temperature is increased further. After that it enters in the engine s turbine. There it gives its energy on the rotating turbine wheels. The wheels are engaged with the compressor and the electro-generator. After the turbine the hot air is with temperature about C..4. Exchanger air air. It is used as economizer - for utilization of the energy on the hot air after the turbine. The temperature of that air is about С at the entrance and it drops to about С at the exit. This air after that joined to the module for hot flue gases, where it is passed into the pyrolysis reactor and the vortex incinerator..5. Three-phase generator. It is powered by the turbine with hot air. It produces electricity that can be sold on the market at preferential prices, as electricity produced from waste..6. Heat exchanger flue gases-water. In it the flue gases that have leaved the gas-air exchanger, attached their energy as they heat water up to temperature 98 0 С. In this kind, the heat energy can be stored and transported more-easily. It can be sold at the market at preferential prices as well..7. Filter for fine cleaning and chemical treatment on the cooled flue gases. After the last heat exchanger the flue gases are with temperature about С. The movement of the flue gases trough the vortex incinerator, heat exchangers and the filter is forcedly, under the influence of centrifugal fan. After the fan trough the chimney the gases are released into the atmosphere..8. The processes of the pyrolysis, incinerator burning of the pyrolysis steam and gases, co-production of heat energy and electricity and cleansing the emited in the atmosphere fumes are managed automatically.. Technical parameters:.1. Quantity of the processed RDF, SRF and/or biomass: ( ) kg/h..2. Energy produced by the cogeneration unit:.2.1. Electricity 150 KWh;.2.2. Heat energy 550 KWh Total efficiency: (88-90)%. IV. The profit from the realization on the produced by the cogeneration unit energy not less than 65 EURO/ton revised fuel. V. Deadline for return on investment up to 3 years.

7 CHG 5000 Industrial oxy-hydrogen generator of hydrogen-oxygen mixture /Brown gas/ The Brown gas is already called HHO - gas, oxy-hydrogen gas and etc. It s been patented by our compatriot Ilia Valkov - Yull Brown in 1971 year. The gas is created by electrolysis of the water. It is not the classic found in 1800 year, electrical decomposition of the water into hydrogen and oxygen. In it the result is a mixture of hydrogen and oxygen, as these two chemical elements are in a molecular species Н 2 and О 2. In the production of Brown gas is obtained a gas mixture in which the majority of the hydrogen and oxygen are in atomic form H and O. It gives the gas different and very interesting for the science and the industry properties. At the burning of the Brown gas is releasing energy which is 3.8 times greater than those released at the combustion of molecular hydrogen in oxygen environment. It is developing temperatures over С. With them comes transmutation of chemical elements, as in some reactions is releasing additional energy. The hydrogen and oxygen atoms in the gas are in the form of ions (they hold electrical charge). This provides them with high reactive abilities. At the burning of the Brown gas is obtaining overheated water steam. It is an active component in many thermo-chemical processes. That s why in the presence of "HHO - gas", the burning and the pyrolysis of various hydrocarbons, occur under significantly higher efficiency, than in ordinary conditions. Himera 13 Ltd. holds patents on a number of technical solutions in the production of "HHO - gas". Our Brown gas generators create gas with high pressures and flow, and a large share of atomic hydrogen and oxygen. Their control is a microprocessor. They have been successfully tested in different applications: For cutting of metals - ferrous and non-ferrous metals with thickness up to 100 mm, as it has reached a temperature at which the Tungsten is evaporated. Cutting, soldering and vitrification of different ceramics, including refractory ones with a high content of Corundum and limited temperature over С. As an addition at burning of different fuels - gasoline, diesel, natural gas, biomass, etc. It is registered increasing of the efficiency of the combustion process up to 30% and sharply reducing the emitted in this - nitrogen oxides, dioxins and furans and polyaromatic hydrocarbons. The Brown gas produced by our generators is used as a working medium for the production and transmission of heat and the pyrolysis and gasification of a wide range of carbon-containing materials. The results obtained by fast pyrolysis bio-oils are chemically stable, high calorific (36 38) MJ/kg., low acidity - рн (4,0-5,0)% and share of the weight of the processed raw material (55 65)%. In the gasification is generating a gas with calorific reaching 18 MJ/m3 and share up to 90%.

8 CHG 5000 Industrial oxy-hydrogen generator of hydrogen-oxygen mixture /Brown gas/ OXY-HYDROGEN GENERATOR CHG500 SPECIFICATIONS Flow 84 L/min. Maximum capacity 5000 L/h at temperature 7000 С. Maximum capacity 9500 L/h at temperature 3600 С. Water Consumption max 2,7 L/h. Power 3 х 380V +10%, -15%. Maximum input power 27 KW. Full computer control of the processes and the protections Ability to connect into a battery of generators by CANOpen interface Automatic water refilling. Ability to autonomous operation without refilling 20 h at maximum load. Complete visualization of the operating parameters and the status of protections.