Method of continuous production of liquid and gaseous fuels from the part of organic substances in the waste
a technology of organic substances and fuels, which is applied in the production of liquid hydrocarbon mixtures, special form destructive distillation, hydrocarbon oil treatment, etc., can solve the problems of limited practical use of their availability and pri
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example 1
[0017]in the first an exemplary implementation of the method according to the invention a hermetically sealed vertically built reactor with a square base of side 1 meter and a height of 4.5 metres was used, in which the lower part contained the generator of gaseous inert medium with a device for the outlet of inorganic parts and the upper, filling part, is formed by hermetical chamber with two closures, whose volume amounted to 1 cubic meter. The middle part of the reactor was equipped in the upper part with the outlet opening for the outlet of the reaction products, which was connected to a separator of solid particles, condenser and extractor separator of particles microdroplets of hydrocarbons from the aerosol. The separator was connected to the collector of liquid parts, and the output of the media went through the condenser at a temperature of the cooling—15° C. The output from this condenser was taken out by pipe outside the workplace and was equipped with a burner for inciner...
example 2
[0021]In the second an exemplary implementation of the method according to the invention there was on the device described in example 1 processed 1426 kg of used tires. Uncrushed tires were gradually filled into the reactor through the filling chamber and an inorganic part, mainly consisting of steel wires, was extracted through a device outlet of this material. The temperature of the gaseous inert medium on entering the reaction amounted to 620° C., in the output 220° C., while the vacuum pressure was of 0.025 MPa.
[0022]The speed of flow of the gaseous inert medium in the reaction space here was 0.015 m / s and a temperature gradient amounted to 136 K / m. The gaseous inert medium, in this specific example of implementation, contained in the volume the amount of 64% of the nitrogen, 13.5% of carbon dioxide and 0.1% of carbon monoxide, with the remainder formed the superheated water steam. The amount of consumed gas of inert media was at 0.7 m3 / kg of processed waste, while it operated o...
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Abstract
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