RU2784299C1 - Waste disposal plant - Google Patents

Abstract

FIELD: industrial and domestic waste disposal.

SUBSTANCE: invention relates to equipment for the disposal of industrial and domestic waste. The waste disposal plant contains a thermoreactor with a grate, an afterburner, a vortex chamber, a heat exchanger, a receiver rigidly connected in series relative to each other. The thermoreactor, afterburner, vortex chamber, heat exchanger, receiver are rigidly fixed relative to the rigid frame. The outlet of the thermoreactor is made in its under-grate zone, communicated with the inlet of the afterburner, the outlet of which is in communication with the inlet of the vortex chamber, the outlet of which is in communication with the inlet of the heat exchanger, the outlet of the heat exchanger is in communication with the inlet of the receiver, the first outlet of which is in communication with the under-grate zone of the thermoreactor, the second outlet of the receiver is in communication with zone of the fluidized bed of the thermoreactor, located above the grate. The thermoreactor in the upper part is configured to communicate with the waste loading device. In the under-grate zone of the thermoreactor, the destruction of combustion gases is ensured at a temperature of 1400 ± 50°C and at a pressure of 0.02 - 0.08 MPa. The receiver and the afterburner are located between the thermoreactor and the vortex chamber. The plant is equipped with a pyrolysis gas smoke exhauster, connected on the one hand by means of a pyrolysis gas collector with the over-grate zone of the thermoreactor, and on the other hand with an afterburner.

EFFECT: increasing productivity and simplifying the design of a waste disposal plant while ensuring the environmental friendliness of the recycling process, reducing the overall dimensions of the plant, expanding its functionality, ensuring the disposal of industrial and domestic waste with the proper quality.

9 cl, 2 tbl, 2 dwg

Description

The invention relates to equipment for the disposal of industrial and domestic waste, including combustible low-calorie waste.

From RF patent No. 2502017 for the invention, a waste incineration plant is known, consisting of a bunker block, a solid waste incineration block in a drum-type rotary kiln, a smoke purification block, a water treatment and heat recovery block, an ash recycling block, which contains a melting reactor lined from the inside; plasma torch; ash bin with ash input mechanism; a system for draining the melt and granulating slag, a power source, a flue gas cleaning system, while the melting reactor of the ash recycling unit has a metal water-cooled casing, the ash recycling unit contains an air compressor and a water pump for cooling the plasma torch electrodes and the reactor casing, the flue gas cleaning system of the recycling unit ash contains an afterburner, a vortex scrubber (centrifugal bubbling apparatus) with an alkaline solution, a bag filter for cleaning from solid impurities and an ash residue (secondary ash) receiver.

From the patent of the Russian Federation No. 2502018 for the invention, an integrated district heating plant for environmentally friendly processing of municipal solid waste with the production of thermal energy and building materials is known, which contains 2 workshops: a waste incineration workshop (MSC) and a heating workshop, and the waste incineration workshop consists of a bunker unit, an incineration unit MSW in a drum-type rotary kiln, a smoke cleaning unit, a water treatment and heat recovery unit, an ash utilization unit that contains a melting reactor lined from the inside, a plasma torch, an ash bin with an ash input mechanism, a melt drain and slag granulation system, a power supply, a flue gas cleaning system , while the melting reactor of the ash utilization unit has a metal water-cooled casing, the ash utilization unit contains an air compressor and a water pump for cooling the electrodes of the plasma torch and the casing of the melting reactor, the flue gas cleaning system of the ash utilization unit contains an afterburner, a vortex scrubber (centrifuge but-bubbling apparatus) with an alkaline solution, a bag filter for cleaning from solid impurities and a receiver for ash residue (secondary ash).

The disadvantage of the known technical solutions is their complexity, due to the complexity of the composition of the equipment, as well as the implementation of the process in two stages with the need to use a system of high-temperature afterburning of slag using a plasma torch. Also, a disadvantage of the known solutions is their non-environmental friendliness, due to the possibility of restoring complex molecules of hazardous substances behind the chimney after thermal heating.

The technical solution according to the patent of the Russian Federation No. 2502018 was chosen as the closest analogue.

The technical problem solved by the invention is the creation of a simple, high-performance plant that provides environmentally friendly disposal of industrial and domestic waste, a reduction in the overall dimensions of the plant, and an expansion of the arsenal of means for waste disposal.

The technical result achieved by the invention is to increase productivity and simplify the design of the installation for waste disposal while ensuring the environmental friendliness of the recycling process, reducing the overall dimensions of the installation, expanding its functionality, ensuring the disposal of industrial and domestic waste with proper quality.

The claimed technical result is achieved due to the fact that in a waste disposal plant containing a thermoreactor with a grate, an afterburner chamber, a vortex chamber, a heat exchanger, a receiver, rigidly connected in series relative to each other, according to the invention , a thermoreactor, an afterburner chamber, a vortex chamber, a heat exchanger, a receiver rigidly fixed relative to the rigid frame, the outlet of the thermoreactor, made in its under-grate zone, is in communication with the inlet of the afterburner, the outlet of which is in communication with the inlet of the vortex chamber, the outlet of which is in communication with the inlet of the heat exchanger, the outlet of the heat exchanger is in communication with the inlet of the receiver, the first outlet of which is in communication with the under-grate zone of the thermoreactor, the second outlet of the receiver is in communication with the zone of the fluidized bed of the thermoreactor, located above the grate, the thermoreactor in the upper part is configured to communicate with the waste loading device, in the under-grate zone of the thermoreactor, destruction of combustion gases is provided at a temperature of 1400± 50 ° C and at a pressure of 0.02 - 0.08 MPa, the dimensions of the vortex chamber are given from the ratio V = (3-5) x X, where V is the volume of the vortex chamber, m ³ , X is the flow rate of hot gas through the vortex chamber, m ³ /s, the receiver and the afterburner are located between the thermoreactor and the vortex chamber, the installation is equipped with a pyrolysis gas smoke exhauster, communicated on the one hand by means of a pyrolysis gas collector with the over-grate zone of the thermoreactor, and on the other hand with the afterburner.

The receiver and the afterburner are located between the thermoreactor and the vortex chamber one above the other.

The plant is equipped with a scrubber equipped with a gas outlet for venting gas to the atmosphere, while the heat exchanger is equipped with a second outlet, which is connected to the scrubber inlet through a flue gas exhauster.

The scrubber is rigidly fixed relative to the frame.

The thermoreactor, afterburner, vortex chamber, heat exchanger, and receiver are interconnected by means of pipelines or sections of pipelines.

The scrubber and the heat exchanger are interconnected by means of a pipeline or pipeline section.

The receiver is made with a third output communicated through an air duct with an external consumer of thermal energy.

The unit is equipped with a fan rigidly fixed relative to the frame and designed for external cooling of the air flow from the thermoreactor to the receiver.

The fan is installed above the heat exchanger.

The claimed utility model is illustrated by drawings.

In FIG. 1 shows a block diagram of the proposed installation for the disposal of combustible waste.

In FIG. 2 shows the claimed installation.

Positions on figures:

1 - thermoreactor;

2 - chamber (furnace) afterburning;

3 - vortex chamber (furnace);

4 - heat exchanger;

5 - scrubber;

6 - receiver;

7 - the first output of the receiver;

8 - the second output of the receiver;

9 - the third output of the receiver;

10 - grate;

11 - frame;

12 - scrubber chimney (scrubber gas outlet);

13 - under-grate zone of the thermoreactor;

14 - fluidized bed zone of the reactor;

15 - fan;

16 - smoke exhauster of flue gases;

17 - smoke exhauster of pyrolysis gases;

18 - collector of pyrolysis gases.

Implementation of the invention

The inventive installation for waste disposal contains a thermoreactor 1 with a grate 10, an afterburner chamber (furnace) 2, a vortex chamber (furnace) 3, a heat exchanger 4, a scrubber 5, a receiver 6, rigidly connected in series relative to each other. The thermoreactor 1, afterburner chamber (furnace) 2, vortex chamber (furnace) 3, heat exchanger 4, scrubber 5 and receiver 6 are rigidly fixed relative to the rigid frame 11. The outlet of the thermoreactor 1, made in its under-grate zone, communicates with the inlet of the chamber (furnace) 2 afterburning, the output of which is connected to the input of the vortex chamber (furnace) 3, the output of which is connected to the input of the heat exchanger 4, the first output of which is connected to the input of the scrubber 5 through a flue gas exhauster 16; the scrubber 5 is equipped with a gas outlet (chimney) 12 for venting gas to the atmosphere; the second outlet of the heat exchanger 4 is in communication with the inlet of the receiver 6, the first outlet of which is in communication with the under-grate zone 13 of the thermoreactor 1, the second outlet of the receiver is in communication with the zone 14 of the fluidized bed of the thermoreactor 1, located above the grate 10, the third outlet 10 of the receiver 6 is connected through an air duct with an external consumer thermal energy. The thermoreactor 1 in the upper part is configured to communicate with the waste loading device (not shown in the figure), in the grate zone 13 of the thermoreactor 1, the destruction of combustion gases is provided at a temperature of 1400±50°C and at a pressure of 0.02-0.08 MPa, the receiver 6 and the afterburner 2 are placed between the thermoreactor 1 and the vortex chamber 3, while the receiver 6 is located above the afterburner 2. Thermoreactor 1, afterburner chamber 2, vortex chamber 3, heat exchanger 4, scrubber 5 and receiver 6 are interconnected by means of pipelines or pipe sections based on the convenience of their placement on the frame 11 and on the basis of ensuring the minimum necessary and sufficient distance between them. The minimum necessary and sufficient distance between the structural elements of the installation is determined taking into account the exclusion of external heat exchange between them and the possibility of dismantling each structural element of the installation during operation, for example, for repair, replacement of equipment. The dimensions of the vortex chamber are given from the ratio V = (3-5) x X, where V is the volume of the vortex chamber, m ³ , X is the flow rate of hot gas through the vortex chamber, m ³ /s. Such dimensions of the vortex chamber 3 are due to the fact that the so-called “quenching” (holding) of hot gases from the thermoreactor 1 must be ensured in this chamber. no more than 0.6 s. This range of exposure will be provided subject to the above ratio between the volume of the vortex chamber 3 and the flow through it of hot gases. The unit is equipped with: a fan 15 designed for external cooling of the air flow from the thermoreactor 1 to the receiver 6; smoke exhauster 16 (scrubber flue), which organizes the movement of flue gases from the thermoreactor 1 to the chimney 12; smoke exhauster 17 pyrolysis gases 17 for pumping pyrolysis gases from the upper part of the thermoreactor 1 to the afterburner chamber 2 for this smoke 17 pyrolysis gases are connected on the one hand through the collector of pyrolysis gases with the above-grate zone of the thermoreactor 1, and on the other hand - with the afterburner chamber 2. Receiver 6 is made with a third outlet 9, communicated through an air duct with an external consumer of thermal energy. Fan 15 is rigidly fixed relative to the frame and installed above the heat exchanger.

The installation works as follows. In the upper part of the reactor 1, through a loading device, for example, a belt conveyor, solid household and/or industrial wastes are received, which are accepted without sorting both from special vehicles and from general purpose trucks. Large-sized metal inclusions are separated from the waste at the receiving stage. Then the waste uniformly enters the zone 14 of the fluidized bed in the area of the grate 10 of the thermoreactor 1 with a temperature of 900 _-200 °C. To ensure high efficiency of neutralization, the waste incineration process is carried out in two stages. At the first stage, thermal destruction is carried out in the thermoreactor 1, and at the second stage, afterburning of flue gases is carried out in the afterburning chamber 2 due to the supply of pyrolysis gases from the upper part of the thermoreactor. This raises the flue gas temperature to 1400°C. Next, thermal hardening is performed: flue gases are held for at least 3 seconds in the vortex chamber 3 with a temperature of up to 1400 ° C and are rapidly cooled in the heat exchanger 4 in no more than 0.6 seconds. Thus organized "thermal hardening" of flue gases. As a result, complex molecules destroyed during thermal destruction are not restored. Then the flue gases enter the smoke cleaning unit, for example, scrubber 5. The flue gases are extracted by a smoke exhauster. Part of the thermal energy from the cooling system of the units, for example, the reactor 1, the afterburner 2, the heat exchanger 4 enters the receiver 6, where the gas-dynamic parameters are equalized. Further, an already uniform flow of hot air with a temperature of up to 800 ° C enters through gas ducts (representing pipelines or sections of pipelines) 7 and 8 to organize the combustion process in the reactor 1 in the zone 14 of the fluidized bed and in the grate zone 13.

The supply of hot air from the cooling system to the thermoreactor 1 through the receiver 6 allows:

- significantly improve the combustion process (oxidizer - heated air from the flue gas cooling system, fuel - waste heated by light radiation and convective heat transfer in the upper grate part of the reactor);

- to produce heat recovery, which, in turn, increases the thermal efficiency of the destructor (proposed installation) as a heat engine.

At the same time, the supply of hot air from the receiver 6 to the above-grate zone 14 of the thermoreactor (fluidized bed zone) and to the under-grate zone 13 makes it possible to most effectively maintain the combustion process in the thermoreactor 1 in its entirety.

Part of the hot air from the cooling system can be supplied to an external consumer of thermal energy through the air duct 9. As an external consumer of thermal energy, for example, a boiler room, a heating system for industrial or residential premises, technological heat consumers can serve.

The scrubber is designed to remove flue gases that have cooled down after the heat exchanger 4 from a temperature of 1400°C to a temperature of 90°C.

In the receiver 6, all air flows are collected from the cooling system of the equipment: thermoreactor 1, heat exchanger (economizer) 4, vortex chamber 3, afterburner chamber 2 and directly the outer casing of the receiver 6. The average temperature of the air flow from the thermoreactor 1 to the receiver 6 can be controlled by the air flow from the fan 15 and, as a rule, ranges from 600°C to 800°C.

The amount of heat Q generated during the operation of the proposed installation can be determined by the formula:

Q \u003d with _rg x m _g x (t ₂ -t ₁ ) \ _u003d with rp x m _in x (t ₃ -t ₄ ),

where:

с _r is the specific heat capacity of flue gases,

c _r - specific heat capacity of air,

m _g is the mass of flue gases (flow rate through the smoke exhauster 16);

m _in - air mass (air flow through fan 15);

t ₁ - flue gas temperature under the grate 10,

t ₂ is the flue gas temperature in the chimney 12 (after cooling in the heat exchanger 4);

t ₃ - air temperature at the outlet of the receiver 6,

t ₄ - outdoor air temperature (at the inlet to the fan 15).

The cooling system in the proposed installation is formed by a vortex chamber 3, a heat exchanger 4, a scrubber 5, a receiver 6.

From this formula it can be seen that the maximum air temperature from the cooling system of the equipment of the waste disposal plant t ₃ is slightly less than the maximum flue gas temperature t ₁ . This allows you to significantly increase the thermal efficiency (COP) of the entire installation as a heat engine. The efficiency can be up to 90%.

Due to its compactness, taking into account the placement of all structural components of the unit on a rigid frame, the entire unit can be placed in a standard shipping container. At the same time, due to the use of an external casing (container wall) that closes the thermal equipment of the installation from the outside, the issue of ensuring the requirements for safe work for maintenance personnel (from burns) is removed. the temperature on the outer surface of the equipment and pipelines (gas ducts, air ducts) does not exceed 30°C.

Due to the uniform distribution of the oxidant (air from the cooling system through the receiver 6) and fuel (waste) in the fluidized bed 12 of the thermoreactor 1, a favorable stoichiometric ratio and conditions for a stable combustion process are organized. Heat energy recovery is carried out by partially directing heated air into the thermoreactor 1 from the receiver 6 through outlets 7 and 8. To organize combustion using an automatic control system, it is important to have a stable oxidizing gas (air). The presence of the receiver 6 allows you to align the thermal gas-air flows to uniform aligned parameters for temperature, pressure, flow rate (flow rate). Receiver 6 allows the use of thermal energy for auxiliary systems of the installation. For example, air extraction for drying economizer collectors from moisture condensate, etc.

Thus, due to the receiver 6 and its connection with zones 13 and 14 of the thermoreactor 1, the gas-dynamic properties of the fuel (oxidizer plus fuel) are increased due to the preheating of the oxidizer and fuel. Fuel (waste) is heated in the upper grate part 14 of the thermoreactor 1 due to convective heat transfer and light radiation from the fluidized bed zone.

The combustion process is organized in the zone of the fluidized bed 14 and in the chamber 2 afterburning. Receiver 6 is an actuator that directly distributes hot air from the flue gas cooling system to organize the combustion process in thermoreactor 1: the fluidized bed zone 14 in the area of the grate 10, and the combustion of flue gases in the afterburner chamber 2. In this case, part of the air is supplied to an external consumer of thermal energy or heat is discharged into the atmosphere.

Technical parameters of the gas-dynamic path during operation of the plant: temperature under the grate 10 - 1400±50°C; flue gas temperature in scrubber 5 – 80±10°C; pressure throughout the gas-dynamic path (flue gases) is 800±100 Pa; the degree of air compression in the duct from the receiver 6 is about 1.039; the capacity of the plant under consideration is up to 5 t/h for municipal solid waste; the required air flow for stoichiometric combustion is 12896 m ³ /hour or 4.31 kg/sec, while the heat released per kilogram of fuel is 9.318 MJ/kg; the total capacity of the installation with a productivity of 5 t / h, a stoichiometric ratio during combustion and a specific heat of combustion of 9.318 MJ / kg is 12.94 MW (46590 MJ per hour).

These parameters indicate the high quality of the proposed installation (destructor) from the point of view of a heat engine: high efficiency (efficiency) - about 85% (and this is when recycling waste, and not when burning hydrocarbon fuels such as natural gas), the stoichiometric ratio of oxidizing agent - fuel (for our case 1:1.1). At the same time, the proposed installation is a compact and easy-to-maintain heat engine.

After exposure (hardening) of hot gases in the vortex chamber 3 and their subsequent rapid cooling in the heat exchanger 4, the substances contained in the hot gases pass into the atomic state, i.e. non-recoverable state. Therefore, the periodic partial discharge of flue gases from the scrubber 5 through the duct 12 does not lead to environmental pollution. For the same reasons, there is no environmental pollution at the third outlet of the receiver 6. Harmless hot air enters the possible consumer of thermal energy. All substances in the outgoing gases are contained in an atomic, non-recoverable state, which is safe for the environment. The intensification of the movement of hot air in the installation is provided by smoke exhausters 16 and 17.

Table 1 provides information on the content of municipal solid waste in Moscow and the Moscow region.

Table 1 MSW components % by weight Carbon, C ^p _I Hydrogen, H ^p _I Oxygen, O ^p _I Nitrogen, N ^p _I Sulfur, S ^p _I Ash, Λ ^R _I Humidity, W ^p _I Food waste 32 3.84 0.576 2.56 0.304 0.048 1.44 23.04 Paper and cardboard 27 7.479 0.999 7.101 0.0432 0.0378 4.05 6.75 Polymers eight 4.408 0.608 1.4 0.072 0.024 0.848 0.64 Glass 5 - - - - - 5 - Black metals 3 - - - - - 3 - Non-ferrous metals 0.5 - - - - - 0.5 - Textile 5 2.02 0.245 1.16 0.17 0.005 0.4 one Wood 3 1.215 0.144 1.014 0.003 - 0.024 0.6 Bones one 0.65 0.05 0.126 0.002 0.0067 0.116 0.05 Leather and rubber 3 1.95 0.15 0.378 0.006 0.0201 0.348 0.15 Stones and small construction debris 0.5 - - - - - 0.5 - hazardous waste 0.5 - - - - - 0.5 - Other eight 3.76 0.424 2.216 0.008 0.016 0.936 0.64 construction waste 3.5 - - - - - 3.5 - Total values 100 25.322 3.196 15.955 0.608 0.158 21.162 32.87

The calculation of combustion of municipal solid waste in the reactor is carried out according to the source "Methodological guidelines for calculating emissions of pollutants into the atmosphere from low-capacity installations for the thermal processing of municipal solid waste and industrial waste" (Moscow, Research Institute of Natural Gases and Gas Technologies - VNIIGAZ LLC) , 1999, UDC 502.55.(203).

In the process of utilization of the given wastes, the composition of which is given in the table, the heat release per 1 kg of fuel was 8.316-9.318 MJ/kg. The air consumption was 2.579 m ³ /kg.

The productivity of the installation was up to 5 t/h, while the required air flow was 12896 m ³ /h, the air density at n.o. amounted to 1.2041 kg/m ³ , the mass air flow required for complete combustion of fuel at a stoichiometric ratio with alpha=1 amounted to 4.31 kg/sec.

On the basis of the claimed invention, a serial model of the waste disposal plant KMUO TsKM.90.00.00.000 was created, the technical characteristics of which are given in table 2:

table 2 No. Name of indicator Indicator value one Working mode Constant,
with periodic maintenance 2 Degree of destruction (processing), %, not less than 99 3 Thermal power, kW/h, not less than 10,000 four Overall dimensions of KMUO from 9 twenty-foot containers, mm
(width Length height) 4800 x12000 x10200 5 Constructive weight, kg, no more 42 000 6 Network settings rated voltage, V 220/380 frequency Hz 50-60 7 Efficiency, %, not less 65 eight Working pressure in the reactor, MPa (kgf/cm ² ) - nominal 0.002(0.02) - maximum 0.005(0.05) 9 Time to enter the operating mode, minutes, no more 60 ten Time of continuous operation before overhaul, hour, not less 40 000 eleven Maximum power consumption, kW 130 12 Installed power, kW 90 13 Service personnel, people/shift 2 fourteen Maximum flue gas temperature), С°. 1300 fifteen The degree of danger of recyclable waste 2-5 grades
GOST 12.1.007 16 Waste types Industrial and household waste 17 The highest permissible moisture content of raw materials, % 100 eighteen Waste pre-sorting requirements 1. Removal of metals and debris
2. Creation of a homogeneous mass using a shredder 19 Generated electrical energy, kWh 500 to 1000 twenty Transfer of thermal energy (coolant water: Т=115°С, Р= 5 bar), MW per hour Up to 8

Placing all units of the installation on a rigid frame, which has dimensions that allow it to be placed in a standard shipping container, allows you to quickly organize the disposal of a significant amount of waste by ensuring the simultaneous operation of several installations (modules). Which significantly expands the functionality of the proposed installation (due to the variability in the number of installations - modules required to ensure the disposal of waste of any volume).

Simplification of the design and reduction of the overall dimensions of the installation is ensured by reducing the number of functional units compared to the closest analogue, due to the compact placement of the receiver and the afterburner.

The increase in productivity is ensured by ensuring an effective heat balance in the installation by supplying air from the receiver outlet to the above-grate and under-grate zones of the thermoreactor. The performance increase compared to the closest analogue is 8-12%.

Claims (13)

1. Installation for waste disposal, containing a thermoreactor with a grate, an afterburner chamber, a vortex chamber, a heat exchanger, a receiver rigidly connected in series relative to each other, characterized in that the thermoreactor, afterburner chamber, vortex chamber, heat exchanger, receiver are rigidly fixed relative to a rigid frame, the outlet of the thermoreactor, made in its under-grate zone, is in communication with the inlet of the afterburner, the outlet of which is in communication with the inlet of the vortex chamber, the outlet of which is in communication with the inlet of the heat exchanger, the outlet of the heat exchanger is in communication with the inlet of the receiver, the first outlet of which is in communication with the under-grate zone of the thermoreactor, the second outlet of the receiver is in communication with the zone of the fluidized bed of the thermoreactor located above the grate, the thermoreactor in the upper part is made with the possibility of communication with the waste loading device, in the under-grate zone of the thermoreactor, the destruction of combustion gases is provided at a temperature of 1400 ± 50°C and at a pressure of 0.02 - 0.08 MPa , dimensions of the vortex chamber The values are given from the relation: V = (3-5) x X, where V is the volume of the vortex chamber, m ³ , X - hot gas flow through the vortex chamber, m ³ / s, the receiver and the afterburner are located between the thermoreactor and the vortex chamber, the plant is equipped with a pyrolysis gas smoke exhauster connected on the one hand by means of a pyrolysis gas collector with the over-grate zone of the thermoreactor, and on the other hand with the afterburner. 2. Installation according to claim. 1, characterized in that the receiver and the afterburner are placed between the thermoreactor and the vortex chamber one above the other. 3. The installation according to claim 1, characterized in that it is equipped with a scrubber equipped with a gas outlet for venting gas to the atmosphere, while the heat exchanger is equipped with a second outlet, which is connected to the scrubber inlet through a flue gas exhauster. 4. Installation according to claim 3, characterized in that the scrubber is rigidly fixed relative to the frame. 5. Installation according to claim 1, characterized in that the thermoreactor, afterburner, swirl chamber, heat exchanger, and receiver are interconnected by means of pipelines or pipeline segments. 6. Installation according to claim. 3, characterized in that the scrubber and the heat exchanger are interconnected by means of a pipeline or pipeline section. 7. Installation according to claim. 1, characterized in that the receiver is made with a third outlet, communicated through an air duct with an external consumer of thermal energy. 8. Installation according to claim 1, characterized in that it is equipped with a fan rigidly fixed relative to the frame and designed for external cooling of the air flow from the thermoreactor to the receiver. 9. Installation according to claim 8, characterized in that the fan is installed above the heat exchanger.

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