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公开(公告)号：US10260002B2
公开(公告)日：2019-04-16
申请号：US15319177
申请日：2015-08-06
Applicant: ALPAJAR GROUP s.r.o.
Inventor： Alois Vasicek
Abstract: The device for the continuous processing of used or otherwise degraded tires consists of a reactor (1) for the thermal decomposition of these waste tires into the organic decomposition products in the form of low molecular hydrocarbons, and residual inorganic waste shares. In the upper part of the reactor (1) there is created a filling chamber (2) with a pair of filling closures (3) for filling its internal space by the waste tires and in the bottom part of the reactor (1) there is formed the output chamber (8) of the residual inorganic shares with a pair of output closures (9), while in the lower part of the reactor (1) there are arranged the nozzles (5) for generating of a mild gaseous inert medium by oxidation of unreacted residues of organic matter from the processed tires. In the upper part of the inner space of the reactor (1) under the filling chamber (2) is then created at least one output opening (11) of this inert gas media, which, together with the therein dispersed organic decomposed products in the form of aerosol, is led through the separator (12) of solid particles and a cooler (17) into a separator (10) of liquid particles from the cooled aerosol which is equipped with the first end output (21) of the liquid particles into the tank (22) and, second, between-operating output (23) of the gaseous particles, which are led to the direct energy use by combustion in thermal machines or in a convenient implementation they are driven Into the freezing chamber (24) for the separation of gases with a condensing temperature above the temperature in this chamber. From freezing chamber (24) there is ended up the second end output (25) of one part in it non-condensed gases and the third end output (26) of the remaining part in it non-condensed gases.
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2.发明申请公开(公告)号：US20170174997A1
公开(公告)日：2017-06-22
申请号：US15325360
申请日：2015-07-09
Applicant: ALPAJAR GROUP s.r.o.
Inventor： Alois Vasicek
CPC classification number: C10B49/02 , C10B53/00 , C10B53/02 , C10B53/07 , C10G1/02 , C10G1/10 , C10G2300/1003 , Y02E50/14 , Y02P20/143
Abstract: Method of continuous production of liquid and gaseous fuels from the part of organic substances in the waste, in particular in the industrial, agricultural and municipal waste, including their mixtures, consists in thermic decomposition of these wastes into fuels—usable low-molecular hydrocarbons, as well as other residual inorganic or other parts intended for recycling or to any landfill, where the treated waste with a content of organic substances, especially in the form of paper, plastics, rubber, including non-crushed used tires, wooden elements, sawdust, rests of meals and fats, and their packaging, in a hermetically sealed reaction space with non-access of air thermically decomposes by the heated gaseous inert medium. By the influence of the electrostatic charge, resulting from the decomposition of organic, in particular polymeric substances, pass from them decomposed low-molecular substances in the form of hydrocarbons altogether in the mixture with gaseous inert medium as the carrier gas in the aerosol, which is then further conducted to its cooling, precipitation and the mutual separation in it contained gaseous, and liquid low-molecular hydrocarbons. After the decomposition of all of the parts of organic substances from the hermetically closed reaction space, all the residual inorganic or other parts of the processed waste are gradually being removed.
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公开(公告)号：US20170166817A1
公开(公告)日：2017-06-15
申请号：US15319177
申请日：2015-08-06
Applicant: ALPAJAR GROUP s.r.o.
Inventor： Alois Vasicek
Abstract: The device for the continuous processing of used or otherwise degraded tyres consists of a reactor (1) for the thermal decomposition of these waste tyres into the organic decomposition products in the form of low molecular hydrocarbons, and residual inorganic waste shares. In the upper part of the reactor (1) there is created a filling chamber (2) with a pair of filling closures (3) for filling its internal space by the waste tyres and in the bottom part of the reactor (1) there is formed the output chamber (8) of the residual inorganic shares with a pair of output closures (9), while in the lower part of the reactor (1) there are arranged the nozzles (5) for generating of a mild gaseous inert medium by oxidation of unreacted residues of organic matter from the processed tyres. In the upper part of the inner space of the reactor (1) under the filling chamber (2) is then created at least one output opening (11) of this inert gas media, which, together with the therein dispersed organic decomposed products in the form of aerosol, is led through the separator (12) of solid particles and a cooler (17) into a separator (10) of liquid particles from the cooled aerosol which is equipped with the first end output (21) of the liquid particles into the tank (22) and, second, between-operating output (23) of the gaseous particles, which are led to the direct energy use by combustion in thermal machines or in a convenient implementation they are driven Into the freezing chamber (24) for the separation of gases with a condensing temperature above the temperature in this chamber. From freezing chamber (24) there is ended up the second end output (25) of one part in it non-condensed gases and the third end output (26) of the remaining part in it non-condensed gases.
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