EA043162B1 - METHOD OF LOW-TEMPERATURE PROCESSING OF ORGANIC SOLID MUNICIPAL WASTE AND INSTALLATION FOR ITS IMPLEMENTATION - Google Patents

Description

The invention relates to the chemical, petrochemical, woodworking and thermal power industries, as well as to housing and communal services associated with the complex processing of organic solid municipal waste, rubber, polymer, pulp and paper, wood, etc.

A known method for thermolysis processing of organo-mineral products - Method for processing carbon-containing substances by means of steam thermolysis [RU patent for invention No. No. 16], containing a thermolysis reactor, means for loading crushed waste carbonaceous matter into the reactor, and a screw conveyor for unloading carbon. However, the disadvantage of this method is the difficulty in implementation due to the large number of steps of technological processes and the inability to be used for the processing of solid organic materials by thermolysis.

The closest technical solution adopted as a prototype is a patent for an invention Process and installation for the processing of rubber-containing waste, [patent RU No. temperature of 350-400°C in an environment of circulating superheated and evaporated coolant at a pressure close to atmospheric. Thermolysis products are: carbon black, synthetic oil and hydrocarbon gas. Industrial rubber waste is processed in a cylindrical thermolysis reactor with a spiral conveyor. The resulting products in the reactor are purged with air, which is the coolant.

With the essential features of the invention in terms of the method coincides with the following set of features of the prototype: thermolysis processing of organic material - industrial rubber waste at temperatures up to 400°C in a reactor with a spiral transport body.

The disadvantages of the known method include the fact that this method and installation cannot ensure high quality of the products obtained, primarily during the thermolysis processing of organic solid municipal waste - MSW (polymer-containing, pulp-and-paper, wood, etc.) having unstable physical and mechanical characteristics: dimensions, shape, density, humidity, flowability, etc.), as well as physical and chemical properties. Industrial rubber waste (after grinding - rubber crumb) is more stable in its characteristics and makes it easier to control the thermolysis process than when using various organic MSW. In addition, due to the specific features of MSW (their low initial density, often changing composition, low charge flowability, the difficulty of ensuring the tightness of the thermolysis reactor to prevent the entry of atmospheric oxygen into it from the atmosphere), all this does not allow obtaining high-quality products: carbon black, liquid carbon fuels and synthetic gas.

Devices are also known for processing household and industrial organic waste and obtaining hydrocarbons, for example, a patent for the invention Method and device for processing household and industrial organic waste [RU patent for invention No. 2392543, IPC F23G 5/027, F23G 5/20, publ. 06/20/2010 bul. No. 17] The disadvantages of the analogue is the low quality of the products obtained during the processing of bulk materials, primarily solid municipal waste, with different physical and mechanical characteristics: granulometry, shape, size, flowability, etc., which is typical for organic solid municipal waste subject to thermal processing , incl. rubber and polymer waste. Also, the impossibility of obtaining high-quality products at the installation.

The closest in technical essence to the claimed installation is the installation for waste disposal adopted as a prototype [RU patent for invention No. 2667398, IPC F 23G 5/027, publ. 09/19/2018, bul. No. 26], containing a pyrolysis (thermolysis) reactor with sluice loading and unloading devices, the internal volume of which is equipped with a continuous mixing device made in the form of a screw with scrapers cleaning it, and the exit of the pyrolysis chamber is connected to an unloading device, including a screw conveyor.

With the signs of the prototype, in terms of installation, the following set of features coincides: the presence of loading and unloading sealing devices of the thermolysis tubular reactor, inside which is located a transporting and mixing body of continuous action.

The disadvantages of the installation are the limited technological capabilities of the installation for the thermolysis processing of organic municipal waste with different physical and mechanical characteristics, which cause low product quality, due to the inability to completely seal the reactor with unstable characteristics of processed MSW: fractional composition, flowability, humidity, heterogeneity of components, their density, morphology, etc., which is typical for TCR; the complexity of providing highly efficient heat and mass transfer in a tubular reactor when using a screw conveying body in it, with physical parameters of the material changing along the length of the reactor: density, mobility, liquid phase content due to the destruction of hydrocarbons, etc.

The invention is directed to the expansion of technological capabilities in the implementation of the method

- 1 043162 thermolysis processing of organic solid waste, in particular, municipal solid waste with different physical and mechanical characteristics, using the proposed installation and improving the quality of the commercial products obtained from them.

The proposed method for low-temperature processing of organic solid municipal waste at temperatures up to 450°C allows to obtain high-quality products: carbon black, liquid carbon fuel and synthetic gas in a circulating hydrocarbon coolant medium - superheated and evaporated steam and the corresponding decomposition of organic components. The method allows the use of recyclable organic MSW of various morphological composition and physical composition: small-sized polymer, wood, pulp and paper, rubber and other waste in a loose or compacted state during thermal-humidity treatment with binders.

The problem is solved by carrying out technological preparation of bulk media, including the classification of pre-crushed small-sized materials or compacted bodies of polyfractional composition into coarse-grained and fine-grained fractions; sealing the processes of loading and unloading the compacted charge by means of forming separate material flows of various fractional compositions: dense packing of charge grains by vibration effect on them or by thermal processing of low-melting components of the compacted layer with exhaust gases, as well as the creation of controlled speed modes of movement of the heat-treated charge in a thermolysis reactor, return from zones of steam and gas release of the coolant and additional injection of the sprayed liquid phase (water) into the zone of destruction of raw materials to intensify heat and mass transfer and reduce oxidative processes. Ensuring uniform loading of the compacted raw material charge and unloading finished products in a given range of variable technological parameters from the thermolysis reactor, sealing its loading and unloading devices, stabilize the high-speed modes of movement of heat-treated materials, which ensures an increase in the quality of the products obtained. In addition, the return of the coolant from the zone of vapor-gas release to the process of heat and mass transfer and the additional introduction of the sprayed liquid phase into the zone of cooling of the raw material intensifies heat and mass transfer, which eliminates oxidative processes that lead to the ignition of an oxygen-containing medium. The method of low-temperature processing of organic MSW is carried out at temperatures up to 450°C, which makes it possible to obtain a greater yield of liquid products and a lower yield of hydrocarbon gas.

To implement the described method, an installation has been developed that contains a tubular reactor with a helical transporting body of continuous action, sealing loading and unloading devices; devices for cleaning, cooling and condensing the gas-vapor mixture in which the boot feeder-seal-gate is made in the form of a feeder inclined at an angle α=20-45° to the horizon with an internal helical working body, consisting of three parts placed, respectively, in three zones: the part of the helical working body, located in the material loading area, is made in the form of a screw with a constant pitch, the middle, cylindrical part of the device is made in the form of pairwise installed, multidirectional two-way helicoidal blades, and the conical part of the device, located in the unloading area, is made in the form of a conical the screw, while on the outer surface of the two-way helicoidal blades, along their perimeter, a perforated classifying body is fixed, located in the area of unloading fine-grained material; in the lower part of the loading device, in the unloading zone of coarse-grained and screened fine-grained material, a sealing feeder-seal-gate with arcuate blades is installed, and the unloading feeder-sealer installed at the outlet of the tubular reactor with a combined transporting body is made in the form fixed on the drive shaft a separate drive, a two-turn capturing blade located in a cylindrical housing, conjugated with the conical part.

The technical result from the implementation of the method of low-temperature processing of organic solid municipal waste, carried out using the proposed installation, is to provide a highly efficient process for processing organic MSW with different physical and mechanical characteristics and physico-chemical properties, obtaining commercial products from waste (carbon black, liquid hydrocarbon fuel and synthetic gas) while eliminating the emission of pollutants into the atmosphere, which keeps the environment clean. In addition, the quality of products obtained as a result of its implementation increases.

The alleged invention is illustrated in the drawings, where in Fig. 1 shows a general diagram of a thermolysis plant for the processing of organic solid municipal waste;

in fig. 2 - loading feeder-compacter-shutter of the installation;

in fig. 3 is a diagram of the arrangement of two-way helicoidal blades of a boot feeder in a cylindrical housing, section A-A in FIG. 2;

in fig. 4 - sealing pendulum elements of the unloading body;

in fig. 5 - sealing drum feeder with arcuate blades;

- 2 043162 in Fig. 6 - unloading feeder compactor;

in fig. 7 is a section B-B in FIG. 6.

The installation contains a receiving hopper with a built-in boot feeder-seal gate 1 (Fig. 1). Tubular reactor for thermolysis of organic municipal waste 2. Inside the tubular reactor for thermolysis of organic municipal waste there is a helical transporting working body of continuous action 3, kinematically connected with a gear motor 4. Helical transporting working body of continuous action 3 is made of three parts: in the zone of supply and heating of compacted raw materials - in the form of a tape screw feeder 5, in the zone of destruction of the intermediate viscous-liquid product - in the form of a segment-spiral transporting body 6, and in the cooling zone of the final product - in the form of a cantilevered spiral 7. The reactor has a heating jacket 8, including a fitting flue gas outlet 9. Gas-liquid burner 10 and chimney 11. Vapor-gas mixture cleaning filter 12, gas-vapor mixture cooling and condensation column 13 (Fig. 1). The column contains a fitting for the selection of light hydrocarbon fuel 14, a fitting for the selection of technical water 15, a fitting for the selection of dark hydrocarbon fuel 16, a condenser 17, a heat exchanger 18, a fitting for the outlet of hydrocarbon gas 19. includes a two-turn capturing blade 22, a conical body 23, with a sealing screw device 24 installed in it. The conical body 23 is associated with a cylindrical body of the unloading part 25 with a smaller diameter, where the unloading single-thread helical blades 26 are located, kinematically connected with the motor-reducer 27. The thermolysis tubular reactor has an industrial water inlet fitting 28 supplied by a pump 29, a steam extraction fitting 30, and a steam supply fitting 31 (Fig. 1).

In FIG. 2 shows the loading feeder-compacter-gate of organic solid municipal waste of the installation for implementing the method for low-temperature processing of organic solid municipal waste. Boot feeder-compacter-gate 1 includes a belt feeder 32, a receiving hopper 33 with an auger 34 located inside (with a constant pitch), inclined at an angle a=20z-45° to the horizon. On the drive shaft of the screw 35, in the cylindrical part 36 of the body of the boot feeder-seal-shutter fixed, installed in pairs, multidirectional, two-way helicoidal blades 37, 38, with an opening angle φι=φ ₂ =90°, rotated relative to each other at an angle ξι= 70-120°, (Fig. 3). The surface of the blades is made of rods 39, the working side of which, from the cylindrical surface, is covered with solid plates 40 with a height of th _pl \u003d (0.15 + -0.3) g _{in l} , where r _{in l} is the radius of the helical blades (Fig. 2, 3 ). On the outer surface of the blades 37, 38, along their perimeter, a perforated classifying body 41 is fixed, located in the zone of unloading fine-grained material (Fig. 2).

In the unloading case of fine-grained material 42, a conveying plate 43 is hinged inside (at point 0), which ensures directional unloading of the material through the sealing pendulum elements 44 (Fig. 2, 4).

In the conical part 45 of the housing 42, there is a compacting screw 46 with a decreasing pitch towards the material unloading (Fig. 2). In the lower part of the unloading cylindrical pipe of coarse-grained material 47 and the unloading body of fine-grained material 42, a sealing feeder-gate 48 with arcuate plates 49 is installed, at the ends of which elastic plates 50 are fixed (Fig. 2, 5), inclined in the direction opposite to the movement of the material. At the same time, the supply rotor with the blades of the sealing drum feeder-seal is displaced relative to the center of the feeder down, along the central axis of the fine-grained material loading pipe 51, by the eccentricity value e=(0.05e-0.1)K _{l p} , where R _lp is the radius of the blades feeder. In the loading pipe of fine-grained material 51 and the unloading cylindrical pipe of coarse-grained material 47, guide elastic plates 52 and 53 are fixed, and on the side of the feeder-gate 48, in the area of unloading fine-grained material, a spring-loaded and connected to a vibrator (not shown in Fig.) is fixed. arcuate plate 54.

The unloading feeder-seal 21 (Fig. 1, 6), installed behind the helical transporting working body of continuous action 7 of the tubular thermolysis reactor 2, is made in the form of a two-turn capturing blade 22 mounted on a drive shaft from a separate drive, installed in a cylindrical housing 20, coupled , with a conical body 23, with a sealing screw device 24 installed in it. The taper of the body 23 is

K = ^=0.2-0.35 where D, d are the larger and smaller diameters of the conical body, respectively, 1 is the length of the body. The conical body, on a smaller diameter d, is associated with a cylindrical body of the unloading part 25, where the unloading single-thread helical blades 26 are located, with the opening angle of the helical surface Ψι=Ψ ₂ =Ψ ₃ =Ψ ₄ =180° and rotated relative to each other by an angle ξ ₂ =90-140° in the direction of movement of the material (Fig. 7).

Tubular reactor thermolysis of organic municipal waste, loading and unloading feeders operate as follows.

-3043162

The original organic solid municipal waste in a pre-crushed (or pre-compacted-compressed) state, in the form of separate conglomerates of a polyfractional composition, is loaded by a belt feeder 32 into a receiving hopper 33 and using a screw feeder 34 installed in it with a constant pitch on a drive shaft 35 and inclined at an angle α=20+45°, are fed into the cylindrical part 36 of the body of the feeder-seal-shutter, Fig. 2. The given angle α=20+45° is determined by the flowability of the processed material and the values of the coefficients of internal friction of its components or conglomerates. With the help of pairs of installed multidirectional two-way helicoidal blades 37, 38, with an opening angle φ1=φ ₂ =90° and rotated relative to each other at an angle ξι=70-120°, internal recycling is provided (moving material of polyfractional composition) between two differently directed helicoidal blades , for example 37 and 38, along the inner side surface of the perforated classifying body 41, fixed along the outer contour of these blades. The execution of the blades from the rods 39, on the working surface of which are fixed, from the cylindrical surface of the housing, solid plates 40, provides a greater intensity of classifying and mixing effects when moving the material. The height of the plate is H _pl \u003d (0.15 + 0.3) g _in _ _l , where g _in . _l is the radius of the helical blades, which ensures a reliable grip of the material in the given range and its movement in the working space.

The opening angle of the helical surfaces φι=φ ₂ =φ3=φ4=90°, provides complete overlap of the cross section of the mesh body (360°) when the blades rotate relative to each other at an angle ξ1=70-90° (Fig. 3). The range of changing angles ξ1 allows you to change the speed of movement of classified materials along the mesh surface, depending on the size, humidity, flowability, granulometry, and other indicators of processed materials.

Fine-grained material, after classification, enters the discharge zone through the fine-grained material unloading body 42, and coarse-grained material is compacted in the conical body 45 of the device using a cone-shaped compacting screw 46 with a decreasing step towards unloading. Through the unloading cylindrical pipe of coarse-grained material 47, compacted coarse-grained material, together with fine-grained material from the unloading body of fine-grained material 42, enters the sealed feeder-gate 48 with arcuate blades 49, (Fig. 2, 5). At the ends of the blades, removable elastic plates 50 are fixed, inclined in the direction opposite to the movement of the material, which eliminates jamming of the blades in the body and reduces their wear. To ensure the directed movement of coarse-grained and fine-grained materials, elastic plates 52 and 53, respectively, are installed in the zone of their further compaction. To prevent hanging of materials, rotating arcuate blades act on these plates, shaking the material located on them. To improve the conditions for compaction of materials moving along the plates 52 and 53 (Fig. 5), the rational use of the working space of the sealed feeder-gate 48, its rotor with blades is shifted relative to the center of the feeder down along the central axis of the fine-grained material loading pipe 51. The selected eccentricity range ensures the implementation the above conditions. In addition, directing the flow of compacted fine-grained material with a minimum layer porosity from the fine-grained material discharge body 42 into the narrowing space, between the elastic plate 52 and the spring-loaded vibrating arcuate plate 54, provides a sufficiently high sealing of the drum feeder-gate 48, and thus minimizes the ingress of air oxygen. into a tubular thermolysis reactor.

The method of thermolysis processing of organic solid municipal waste is implemented as follows.

Organic municipal solid waste with different physical and mechanical characteristics (shape, size, density, humidity, flowability, etc.) in a pre-crushed state in the form of small-sized materials or compacted bodies of a polyfractional composition are fed into the feeder-compacter-gate 1, after which enter the tubular reactor for thermolysis of organic municipal waste 2. The movement of raw materials in the reactor occurs with the help of a helical transporting working body of continuous action 3, rotated by a motor reducer 4. thermal degradation reaction. As a result of this reaction, a gas-vapor mixture and solid carbon products are formed. The gas-vapor mixture, having passed through the gas-vapor mixture purification filter 12 and the heat exchanger 18, enters the gas-vapor mixture cooling and condensation column 13. With the help of the condenser 17, liquid hydrocarbons in the vapor state are condensed. Light hydrocarbon fuel is taken from the light hydrocarbon fuel selection nozzle 14 and sent to the gas-liquid burner 10, hydrocarbon gas is also sent there, taken from the hydrocarbon gas outlet nozzle 19. Burner heat is supplied to the heating jacket 8. Flue gases are removed from the heating jacket 8 through the outlet fitting flue gases 9 into the chimney 11. Industrial water is partially supplied through the technical water inlet fitting 28 using a pump 29, into the cooling zone of the final product, and partially taken from

- 4 043162 fittings for the selection of technical water 15 into a storage tank and further use for internal plant needs. The steam generated during the cooling of the final product is removed through the steam extraction nozzle 30 and is directed to the destruction zone of the intermediate viscous-liquid product through the steam supply nozzle 31 to intensify the process. Dark hydrocarbon fuel is collected from the dark hydrocarbon fuel selection nozzle 16 into a storage tank and further sale to the consumer. The cantilevered spiral 7 provides movable transportation of the solid product - carbon black into the cylindrical body 20 of the unloading feeder-sealer 21. Further, the solid product is advanced by a two-turn capturing helical blade 22, which ensures the product is injected into the conical body 23 with a helical sealing blade 24. This ensures sealing unloading compactor feeder. To stabilize the process of unloading the compacted end product in the cylindrical body of the unloading part 25 coupled with the conical sealing device, unloading single-thread helical blades 26 are installed on the drive shaft.

At the first stage, in the zone of compacted feedstock supply, a belt screw feeder (Fig. 1) is used, installed in the tubular reactor vessel - axially (eccentrically) - with the drive shaft axis shifted to the lower semicircle. The developed working surface of the screw feeder belt, which increases in the direction of material movement, its pitch, as well as the volume of space under the feeder, in comparison with the screw conveying body of the prototype, eliminates clogging of the interturn space of the feeder with compacted material, ensures its accelerated removal to the destruction zone, and the increased space under the feeder (due to its eccentric location in the reactor vessel) increases the intensity of thermal heating and steam removal from moistened raw materials.

At the second stage - in the zone of destruction of organic solid municipal waste (Fig. 1), taking into account the decreasing volume of the material and its viscous-liquid state, respectively, increased adhesion with the working surface of the helical transporting working body of continuous action, the latter is made in the form of a segmented-spiral transport organ.

The step-by-step fastening of the reinforcing segments to the turns of the helix ensures the elastic-rigid state of the feeder, prevents sticking of its turns by the adhesive material, and also provides sufficient reliability from the impact of deformation loads during the transformation of the material.

The use of a continuous helical transporting body in the form of a cantilevered spiral 7 (Fig. 1) at the third stage of the thermolysis treatment of organic MSW, in the cooling zone, ensures the mobile transportation of the solid product - carbon black to the unloading feeder compactor (Fig. 6).

The use of the specified combined combination of transporting organs: tape, segment-spiral and spiral (cantilever mounted) in a tubular reactor for thermolysis of organic municipal waste takes into account the real conditions for processing organic MSW: changing density and volume of the heat-treated material along the length of the reactor, increased steam removal at the first stage and intensive the destruction of hydrocarbon raw materials - on the second, significant dynamic loads during the transportation of the material in the first two stages and their reduction in the last stage of cooling the porous product, etc.

The proposed technological and technical solutions help to increase the efficiency of the thermolysis method at each stage of organic MSW processing, prevent the formation of plugs from compacted material, and, consequently, the creation of high pressure zones along the length of the reactor, which ultimately stabilizes the process of heat treatment of raw materials with different physical properties. -mechanical characteristics, increases the productivity of the tubular thermolysis reactor and the method as a whole, and also improves the quality of the resulting commercial products.

Taking into account the reduced volume of the finished product compared to the initial volume of raw materials, in the cylindrical (transitional part between the tubular thermolysis reactor and the unloading feeder sealer) a two-turn capturing helical blade 22 is installed, which ensures that the product is injected into the conical housing 23 with the helical sealing blade 24. This ensures sealing the unloading compactor feeder. To ensure the possibility of varying the degree of compaction of the product, respectively, the sealing of the device, it is necessary to observe the specified taper

K = =0.2-0.35, where D, d - respectively, the larger and smaller diameter of the conical body, 1 - the length of the body (Fig. 1).

To stabilize the process of unloading the compacted final product in the cylindrical body of the unloading part 25 coupled with the conical sealing device, unloading single-thread helical blades 26 are installed on the drive shaft with an opening angle of the helical surface Ψ ₁ =Ψ ₂ =Ψ ₃ =Ψ ₄ =180° (Fig. 7 ).

To ensure additional sealing of the unloading device and uniform unloading

- 5 043162 marketable products blades are rotated relative to each other, in the direction of movement of the material, at an angle ξ ₂ =90-140°. The specified range of angles ξ ₂ provides (Fig. 7) additional sealing of the node and uniform unloading of the material compacted in the conical gate.

The proposed method and installation for thermolysis processing of organic solid municipal waste provides a low-temperature and highly efficient method for processing organic MSW with different physical and mechanical characteristics and physical and chemical properties, obtaining commercial products from waste (carbon black, liquid hydrocarbon fuel and synthetic gas), with the exception of emission of pollutants into the atmosphere.

Thus, the problem of the invention is solved.

Claims (6)

1. Installation for the implementation of the method of low-temperature processing of organic solid municipal waste by thermolysis, containing a tubular reactor with a helical transport body of continuous action and with sealing loading and unloading devices; device for cleaning, cooling and condensing the gas-vapor mixture, characterized in that the boot feeder-seal-gate is made in the form of a feeder, with an axis of inclination to the horizon at an angle of α=20-45°, equipped with a helical transporting body of combined action, consisting of three parts : the first part is a helical conveying body located under the receiving hopper at the place of material loading, made in the form of a screw with a constant pitch, the second part - in the form of pairs of oppositely directed two-way helicoidal blades installed in a cylindrical housing with an opening angle of Ψ1=Ψ2=90° helical surface, rotated relative to each other at an angle ξ1=70-120°, the third part of the conveying body - in the form of a cone-shaped auger with a step decreasing towards unloading; located in front of the discharge nozzle and housed in a conical body; at the same time, on the outer surface of the two-way helicoidal blades, along the perimeter, a perforated classifying body is fixed for unloading fine-grained material in the lower part of the loading device, and in the lower part of the unloading cylindrical pipe of coarse-grained material and the unloading body of fine-grained material, a sealing feeder-gate with arcuate blades is installed, the rotor of which displaced relative to the center of the feeder down, along the central axis of the feed pipe of fine-grained material by the value of the eccentricity e=(0.05+0.1)R _Λ . _n , where R _l . _n is the radius of the feeder blades; in addition, on the side of the housing of the feeder-gate with arcuate plates, from the side of the fine-grained material loading nozzle, a spring-loaded arcuate plate connected to the vibrator is fixed; and an unloading feeder-seal installed at the outlet of the tubular reactor, equipped with a coolant inlet pipe into the initial part of the reactor to intensify heat and mass transfer and a coolant outlet pipe from the final part of the reactor and with a combined transporting body, driven by a motor reducer with an adjustable speed of the output shaft, respectively, speed of movement of the heat-treated charge, is made in the form of a two-turn capturing blade fixed on the drive shaft from a separate drive, located in a cylindrical housing, conjugated with its conical part and installed inside the conical part of the body of the sealing screw device in such a way that the smaller diameter helical blade of the latter is associated with unloading single-thread helical blades of constant diameter, located in a smaller diameter cylindrical body of the unloading feeder-compactor; while the helical blades of constant diameter are rotated relative to each other at an angle ξ2=90-140° in the direction of movement of the material, and the opening angle of their helical surface is Ψ1=Ψ2=Ψ ₃ =180°. 2. A method for low-temperature processing of organic solid municipal waste by thermolysis in a tubular reactor with a helical transport body at temperatures up to 400-450 ° C in a circulating coolant medium and the corresponding decomposition of organic components into carbon black, liquid hydrocarbon fuel and synthetic hydrocarbon gas, characterized in that that the thermolysis of organic solid municipal waste includes the stepwise implementation of technological processes for the preparation of bulk media, which consists in classifying pre-crushed small-sized materials or compacted bodies of polyfractional composition into coarse-grained and fine-grained fractions while ensuring the sealing of the processes of loading and unloading the compacted charge, as well as in creating controlled speed modes of movement heat-treated charge in a thermolysis reactor and return of the coolant from the final part of the reactor to the initial one in the form of steam to intensify heat and mass transfer, reduce oxidative processes, and complete the process; introducing water into the final part of the reactor, which contributes to the cooling of carbon black, the opening of its pores and the desorption of hydrocarbons. 3. The method according to claim 2, characterized in that for the intensification of heat and mass transfer processes, water vapor is introduced through a fitting installed between the heating jackets of a tubular reactor in its cylindrical housing. - 6 043162 4. The method according to claim 2, characterized in that for the use of a heterogeneous, moistened and low-flowing mass of processed waste in a crushed state, in the cylindrical part of the housing of the loading device, after the screw feeder, on its shaft, two-way helicoidal helical blades unidirectional towards the unloading are installed with solid working surface, rotated relative to each other, in the direction of material movement, at an angle β=90°, facilitating the transportation of material in a compacted state. 5. The method according to claim 2, characterized in that the adjustment of the speed modes of movement of the heat-treated charge is carried out, based on the technological modes, by changing the speed of rotation of the output shaft of the motor-reducer connected to the helical transporting working body of continuous action of the thermolysis reactor, located in the tubular housing axially relative to the central axis in the lower semicircle and represented by a combined mover, consisting of three parts of equal length and made in the first part in the form of a belt screw feeder with a step increasing in the direction of unloading, in the second part - in the form of a segmented spiral transporting body, and in the third part - in the form of a cantilevered spiral. 6. The method according to claim 2, characterized in that water is used to open the pores of carbon black, desorb hydrocarbons from it and exclude the formation of coke.