RU2351846C2 - Automated shaft furnace for thermal gasification of mixed composition of various solid components - Google Patents

Abstract

FIELD: heating.

SUBSTANCE: invention is related to the field of thermal processing of solid household and industrial wastes that contain flammable and incombustible materials, by means of pyrolysis and gasification of organic component in wastes by production of carbon component of wastes to prepare hydrocarbon products of pyrolysis: fuel gas and solid remains. Solid household wastes are loaded in shaft furnace, in which oxygen-containing gasifying agent is supplied in counterflow. Pyrolysis mode is arranged in shaft furnace with further gasification of pyrolysis carbon remains. Furnace also comprises statistical multi-channel power supply source and distributed-integrated control system with wide information support, which makes it possible to optimize mode of wastes recycling by means of control over flow of gasifying agent and ratio of flammable and incombustible components and oxygen content in gasifying agent.

EFFECT: provision of complete utilisation of solid wastes, increased yield of fuel gas with increased content of hydrocarbon fraction.

3 dwg

Description

The invention relates to the field of thermal processing of solid industrial and household waste containing combustible and non-combustible solid components, by pyrolysis and gasification of the organic component of the waste to produce hydrocarbon pyrolysis products: fuel gas, as well as solid lump and bulk residues, which will be widely used in ecology for utilization of various solid wastes, in particular, upon receipt of gaseous fuel for subsequent use in energy, and ash for use - in the construction industry.

A very large number of automated shaft furnaces is already known, each of which is developed depending on the field of application, the composition of the material being processed, the intended use of the products obtained, the type of fuel used or produced, the design features of the shaft furnace itself and the achieved level of scientific and technological progress at a given point in time .

1. Patents (indicating the date of publication)

SU 506628 A1, 03/03/1971;

SU 1698575 A1, 12/15/1991;

SU 1698575 A1, 12/15/1991;

SU 1836603 A3, 08.23.1993;

GB 1,104,378 A, 02/28/1968;

US 3511194, 01.24.1969;

US 5558028 A, 09.24.1996;

DE 1193860 A, 05/26/1965;

EP 0444652 A2, 09/04/1991;

RU 94021263 A1, 02.27.1996;

RU 2089786 C1, 09/10/1997.

2. Literature

1. Ksendzovsky V.R. Automation of pellet production processes. M .: Metallurgy, 1971, 216p.

2. Furnaces for the production of lime. Directory. Monastyrev A.V., Aleksandrov A.V. - M.: Metallurgy, 1979, 232s.

3. Thermal operation of shaft furnaces and units with a dense layer. Gordon Y.M. et al. M .: Metallurgy. 1989, 120s.

4. Belenky A.M. and others. Automatic control of metallurgical processes. Textbook for high schools. - M .: Metallurgy, 1989. - 25 L

5. Glinkov G.M. et al. Control and automation of metallurgical furnaces. Textbook for high schools. - M.: Metallurgy, 1989 - 20 l.

6. Krivdin V.A. and others. Thermal work and designs of furnaces of ferrous metallurgy. Textbook for high schools. - M.: Metallurgy, 1989, 462, p. 28-35.

7. Engineering environmental protection. Water purification, waste disposal. / Edited by Yu.A. Birman. M.: Publishing house "ASV", 2002, 296 S. // Section IV. Disposal of waste by thermal methods, p. 195.

8. Likhachev Yu.M. and others. Solid municipal and industrial waste management. St. Petersburg: Mendeleev Publishing House, 2005, 288 pp.

A known device system for the automation of lime kilns operating on solid fuels, published in the journal "Building Materials", 1963, No. 5, p.19-21, author Temkin L.D.

It includes a pulse system for the automatic loading of coal and limestone in a strictly specified ratio and a system for automatically controlling the firing process with stabilization of the following parameters:

- rarefaction at the outlet of the furnace;

- air flow at the inlet to the furnace;

- the position of the heating and firing zones according to the temperature difference from the sensors installed in the respective zones, or according to the temperature of the exhaust gas.

The following deviations of the parameters coming through the information channels from the respective sensors are used as alarms:

- reduction of vacuum before the suction fan;

- pressure drop after blowing the fan;

- increase in temperature of flue gases;

- emergency levels of the charge in the shaft furnace and the weakening of the cable tension of the power lift.

The disadvantages of this system include:

1. The low level of reliability due to the use of relay-contact logic circuits and control actions.

2. Great need for fuel loading.

3. The complicated management structure in start-up, scheduled and stop modes.

4. Low information security for choosing a flexible rational process control algorithm.

Known automated shaft furnace for calcining limestone with solid fuel, described in the book: Furnaces for the production of lime. Directory. Monastyrev A.V., Aleksandrov A.V. M .: Metallurgy, 1979, 232 p. (see p. 124-132, Fig. 36-40).

It includes a shaft furnace, an electrovibration feeder with a dispenser, a two-valve loading mechanism, a two-wedge roller unloading mechanism, control devices and controls. The degree of loading of the shaft furnace by its height is controlled by radioactive level alarms.

The furnace is loaded automatically, depending on the level of material in it. Upon reaching the lower level, loading is performed, and the upper - its termination.

The disadvantage of this automated shaft furnace is the inability to create a rational mode of its operation due to the low information security of the control object.

There is also known a device for implementing a method for controlling a blast furnace, comprising a blowing machine for supplying blast to the furnace, a chimney for relieving excess pressure, two pressure sensors: at the air inlet to the furnace and at the gas outlet from the furnace, corresponding controllers, actuators with butterfly valves and channel switch (see patent RU 2212014 C2, 04/05/2001).

The disadvantages of this device include:

1. The lack of sensors for monitoring the composition of the gas phase at the outlet of the furnace does not allow to optimize the mode of its operation.

2. The presence of actuators with throttle valves on the lines of air supply to the furnace and gas outlet from the furnace reduce the speed of the pressure control system and cause additional energy losses during throttling of gas flows.

Also known is a method and device for high-temperature processing of solid waste into commercial products (patent 2086850, Russia from 12.27.1995).

The device includes a vertical shaft furnace, a loading unit from above. It has means for heating and introducing air blast into the lower part of the furnace and removing gases from the upper part of the furnace during thermal gasification, an unloading unit made in the form of three slots located at different levels of the hearth. Transducers for measuring pressure pulsations of gaseous media injected into the furnace and leaving the furnace were installed using a system for monitoring and regulating technological parameters based on a microcomputer.

The disadvantages of this device are:

1. The need for coal as fuel for gasification of waste.

2. The low level of information support, which does not guarantee the rational functioning of the shaft furnace.

3. The use of only one microcomputer limits the ability to collect and process information, as well as the choice of control actions.

A device is known, presented in the article "Automation of control of shaft furnaces in a metallization shop using a dynamic expert system" (journal "Mechatronics, automation, control" 2004, No. 4, p. 44-49).

The shaft furnace consists of a lined body, loading and unloading devices and is equipped with a hot air fan, air heater, air and gas supply pipes for various purposes, a gas phase outlet pipe connected to a smoke exhaust, and the loading device is equipped with a lock gate.

The information field is provided with sensors for monitoring temperature, pressure, flow and concentration, and a microprocessor control controller is used as a control module with the development of control actions on the executive mechanisms of loading raw materials, air and gas, as well as unloading the finished product.

The device is characterized by the features of automation of shaft furnaces at the scale of the metallization shop, as the lower level of an integrated system for the automatic control of these facilities, in which a set of tasks is solved: control of the parameters of shaft furnaces, as well as the costs and parameters of material and energy flows entering and leaving; with the creation of separate control loops to stabilize the most important parameters and the presence of control channels for the mechanisms of furnaces. As a microprocessor device for generating control actions, only one microprocessor control controller is used.

The disadvantages of this device include:

1. Limited scope - the inability to use solid waste for disposal.

2. The absence at the lower level of a computer (PC) for collecting, processing, analyzing and storing incoming information from parameter sensors unjustifiably transfers the solution of some operational control tasks to the middle and upper levels of integrated automatic control systems, which requires expanding the generalized database structure and increasing computer park with its software.

3. The use of a dynamic expert system requires: preliminary accumulation of a large amount of statistical material about the control object, expert assessment of the opinions of specialists on the peculiarities of the behavior of this object in the regulated or changed modes, which are often contradictory, which is almost impossible to implement in the context of introducing new control objects with your own specific operating modes and instrumentation.

4. High sensitivity of the device to model settings, when minor errors in its adjustment, caused by inaccuracies in a priori knowledge about the characteristics of the control object, such as a shaft furnace, can cause incomplete utilization of solid waste and lead to a sharp decrease in the yield of hydrocarbon fraction in the gas phase.

The objective of the invention is to expand the scope of the shaft furnace, ensuring the completeness of solid waste disposal, increasing the yield of fuel gas with a high content of hydrocarbon fraction and more reliable operation of the facility control device.

The essence of the invention lies in the fact that an automated shaft furnace for thermal gasification of a mixed composition of various solid components includes a shaft lined casing, a loading device with a lock gate and an unloading device, a hot air fan, air heater, air and gas supply pipes, an outlet branch pipe for gas phase discharge connected to a smoke exhaust, a conical ash collector and a discharge unit, a control module in the form of a microprocessor control controller for generating control influences on the actuators for supplying solid components, gases, air and unloading the finished product, a static multi-channel power source and a personal computer, two sensors for loading solid components located in the upper part of the shaft furnace and two ash level sensors in the collector, displaced in height, thermal converters located in the shaft lined case at five points along the height of the case, in the unloading device, in the ash collector, in the nozzle for supplying hot air to the shaft furnace and in the bottom pipe of the outlet of the gas phase from the shaft furnace, pressure sensors located at the height of the shaft lined housing at three points, the sensor of rarefaction of the gas phase in the outlet pipe, flow sensors of hot air in the pipe of its supply and gas phase in the outlet pipe, oxygen concentration sensors in the air at the inlet to the air heater and carbon in the gas phase of the outlet pipe, multichannel sensors for the concentration of hydrocarbon and carbon fraction in the gas phase of the outlet pipe, and the discharge device The uru is equipped with two parallel ring electrodes with a multi-row screw shredder located below with a grate under it, and the conical ash collector is equipped with a cooling jacket, multi-blade agitator, an unloading unit with a shutter from the lower and upper gates, a vibratory flow driver with scanning frequency and amplitude, output sensors are connected in parallel to a microprocessor-based controller and a personal computer, outputs from a microprocessor-based controller Oller connected to the inputs of the static multichannel power source, which outputs are connected to inputs of the actuators drives the heater, arranged in parallel to two ring electrodes unloading device.

In order to justify the conformity of the invention with the criteria of "industrial applicability" and "scientific novelty" we give the following evidence:

1. Today in Russia annually more than 150 million m ³ or 7 billion tons of solid waste are generated containing secondary material resources of the following composition and quantity: waste paper - 20 + 40%; metal - 4 + 5%; plastics - 12 + 15%;

glass - 5-7%; textiles - 6-12% and wood - 8-14%. Currently used, i.e. only 2.0 billion tons of solid waste or only 20% of its total mass is processed.

2. To date, about 80 billion tons of solid waste has been accumulated in dumps and storages with the corresponding withdrawal of about 100 thousand hectares of land from economic turnover for these purposes. The open surfaces of landfills pose a serious environmental and sanitary hazard to humans and the environment. In addition, they are prone to spontaneous combustion and can become a hotbed of fire in the surrounding forests. Solid waste itself is still a breeding ground that promotes intensive reproduction and the secured existence of sources and carriers of infectious diseases: insects and rodents. Solid waste also causes the appearance and intensification of unpleasant odors, increases the intensity of dust emissions and the degree of pollution of groundwater and the air

3. Megacities with their high concentration of population, production, and transport attract a significant amount of material and energy resources, which in the course of use are transferred, ultimately, to the category of waste stored in landfills, often unauthorized, and landfills. The involvement of these wastes in the economic turnover of large cities can provide megacities with additional resources that contribute to their further development. This is achieved by the widespread introduction of industrial waste processing with the production of gaseous energy carriers and solid commercial products, which ensures the successful solution of many social, economic and environmental problems of the region.

4. It should be noted the significant advantages of the operation of shaft furnaces due to the following circumstances:

- increased surface of the material subjected to heat treatment. So, for example, a loaded bulk material with an average diameter of (10-15) × 10 ^-3 m has a heat and mass transfer surface of the order of 240 m ² in 1 m ³ layer with a porosity of 0.4;

- the creation of high turbulization of the gas stream is due to the specific structure of the layer, namely the alternation of narrowing and expansion of channels in the inter-musk space, which causes a multiple change in the direction of movement of the gas stream when it moves up;

- almost full use of the workspace (about 95%);

- efficient use of thermal and electric energy due to the operation of the furnace according to the countercurrent principle: the supply of calcined material and the removal of gaseous reaction products is carried out towards each other. The countercurrent movement of the calcined material and hot gases allows more efficient use of the heat of the exhaust gases for heating and faster heating of the incoming material;

- the relative simplicity of design solutions provides reliability in operation and ease of maintenance;

- guaranteed high specific productivity reaching 12 t / m ³ per day, as well as a significant duration of the shaft furnace: 10 ÷ 20 years;

- the reduction rate of recycled waste reaches 60-80% of its original volume.

5. In connection with a significant deterioration of the environmental situation, each person experiences fatal deposition of toxins and the formation of poisons - the end products of impaired metabolism. But since his health takes the leading place in the system of human values, the presence of certain diseases in a person makes him seek effective ways not only to heal him, but also to prevent their occurrence in the future, and this is inextricably linked with the creation of a rational system for industrial processing of solid waste for the purpose of their 100% disposal.

6. Today, in the world markets for project financing, environmental indicators, from the point of view of project development and implementation, are beginning to occupy key positions and, in order not to undermine the competitiveness of domestic projects, environmental requirements, no matter how stringent, should be met, since environmental dumping is not only for Russia not promising, but certainly harmful.

Solid waste must be processed as it accumulates, otherwise any unique technical development will gradually begin to turn into a source of environmental threat to the population, which is unacceptable in the modern world.

7. In iron and steel industry, shaft furnaces called blast furnaces are widely used, the level of automation of which is quite high and the principle of automation of which can be successfully used to improve the management of the shaft furnace by thermal gasification of the mixed composition of various solid components. It is also known to use shaft kilns in the production of lime (CaO) in the construction industry, where a high degree of automation is also achieved.

8. In some cases, the best regime of thermal gasification and the composition of the products obtained during its implementation can be indirectly judged by the content of residual oxygen in the outlet gas stream from the shaft furnace, which improves the reliability of its management.

9. The use of a static multi-channel power source (SMIP) makes it possible to simplify the start-up mode in the operation of a shaft furnace and to refuse to install control valves for controlling gas flows.

10. Currently, when computer technology has become widespread, traditional relay-contact systems and instrumentation can be successfully replaced by a compact, convenient and more reliable in operation distribution-integrated control system consisting of a personal computer at the top level and multi-channel microprocessor controller at the lower level. In this case, a serial personal computer (mainframe) is used as a control panel.

The principal feature of the invention is illustrated by the following graphic materials:

1. The functional diagram of an automated shaft furnace for thermal gasification of the mixed composition of various solid components, Fig.1.

2. The structural diagram of a distributed integrated control system (RISU), Fig.2.

3. The structural unit of a static multi-channel power source (SMIP), Fig.3.

Automated shaft furnace 1, designed for thermal gasification of the mixed composition of various solid components, consists of the following components (figure 1):

- shaft lined housing 2 in the form of a truncated cone;

- boot device 3;

- unloading device 4;

- collection of ash 5;

- unloading unit 6.

The shaft lined casing 2 in the upper part is equipped with an outlet pipe 7 for venting the gas phase using a smoke exhauster 8 with an engine 9.

The loading range of solid components (charge) varies in the range: 10 - minimum, 11 - maximum levels.

The loading device 3, which is a sphere 12 in the upper region and a truncated cone 13 in the lower region, is equipped with a lock gate 14, which consists of the lower 15 and the upper valves 16, which are rigidly interconnected. The upper valve 16 is suspended from the power cable 17, which through the block 18 is connected to the winch 19, rotated by the engine 20.

The unloading device 4 is equipped in the upper part with two parallel ring electrodes 21, and in the lower part with a multi-row screw chopper 22 connected through a gearbox 23 to the motor 24.

A grate 25 is located under the auger grinder. Unloading device 4 is equipped with supply pipes: 26 - hot air enriched with oxygen; 27 - a pair through the valve 28 with the engine 29.

To supply hot air to the unloading device 4, a blower fan 30 with an engine 31 is designed. Air is heated in the air heater 32.

The enrichment of air with oxygen is carried out through the valve 33 with the engine 34.

The conical ash collector 5 is equipped with a cooling jacket 35, made in the form of a tubular coil, and a multi-blade agitator 36, rotated through the gearbox 37 by the engine 38.

The unloading unit 6 is equipped with a shutter consisting of a lower 39 and an upper 40 gates moving with the help of corresponding gears 41 and 42 by means of engines 43 and 44.

To facilitate the unloading of ash, a vibratory flow inducer 45 with scanning frequency and amplitude is used.

Triangular arrows indicate material and energy flows:

- 46 - blast air;

- 47 - oxygen;

- 48 - heated air;

- 49 - steam;

- 50 - vented gas phase;

- 51 - paged ash.

The following parameters are controlled in a shaft furnace:

Temperature with the help of thermal converters along the height of the shaft furnace:

- in the shaft lined building at five points: 52, 53, 54, 55 and 56;

- in the unloading device 57;

- in the collection of ash 58;

- in the nozzle for supplying hot air 59;

- in the outlet pipe of the outlet of the gas phase from the shaft furnace 60.

Level:

- solid waste loading: minimum (mark 10) with a level sensor 61, and maximum (mark 11) with a level sensor 62;

- ash in the ash collector: the minimum value is with a level sensor 63, and the maximum value with a level sensor 64.

Pressure:

- the height of the shaft lined housing 2 by means of pressure sensors: 65, 66 and 67;

- in the supply line 26 of hot air - 68.

Underpressure:

- in the outlet pipe 7 of the outlet of the gas phase - vacuum sensor - 69.

Consumption:

- hot air supplied through the supply pipe 26 to the discharge device using the flow sensor 70;

- the gas phase in the outlet pipe 7 using the flow sensor 71.

Concentration:

- oxygen in the air supplied to the air heater 32 by means of a concentration sensor 72;

- hydrocarbon fraction (CHNu) in the outlet pipe 7 of the removal of the gas phase from the shaft furnace using a multi-channel concentration sensor 73;

- carbon (C) by means of a concentration sensor 74 and a carbon fraction and residual oxygen (CO, CO ₂ , O ₂ ) using a multi-channel concentration sensor 75 in the outlet pipe 7 of the exhaust gas phase from the shaft furnace.

Figure 2 presents the structural diagram of a distributed integrated control system (RISU), consisting of a personal computer 76 for collecting, processing and accumulating information from converters; microprocessor control controller (MRK) 77, generating a control action, and a static multi-channel power source (SMIP) 78.

Figure 3 shows the structural block SMIP 78, consisting of nine (79-87) autonomous power supplies for direct control of actuators and power systems.

The following communication channels are indicated by alphanumeric indices: X1-X23 - information signals from thermal converters and sensors; U1-U12 - control actions; Z1-Z7 - intermediate control channels coming from RTOs 77 to SMIP 78.

The work of an automated shaft furnace for thermal gasification of the mixed composition of various solid components is as follows.

In a shaft furnace regulate:

- loading level of pre-ground solid waste containing organic and inorganic components in the shaft lined casing 2 using the sensor 61 of the lower level value on channel X ₁₀ (mark 10), a signal is sent to MPC 77, from which a command is received on channel U ₁ to the inclusion of the lock gate 14 through the engine 20 to supply solid components.

As soon as their level reaches the upper mark 11, a signal is sent to channel МРК 77 from level sensor 62 through channel X ₁₁ , from which a command follows through channel U ₁ to turn off the gate lock and stop supplying solid components;

- the ash level in the ash collector 5 at the signal X ₁₃ from the upper level sensor 64 supplied to the MRK 77, from which the command is sent via channel U ₄ to the engine 44 to open the slide gate of the unloading unit 6 and through channel Z2 through an autonomous power supply 80 channel U ₃ to a vibratory flow inducer 45 to facilitate and accelerate the supply of ash from the ash collector 5 to the discharge unit 6.

When the ash level in the ash collector 5 reaches the level sensor 63 of the lowest value, a signal is sent to channel МРК 77 via channel X ₁₂ with the generation of a command through channel U ₄ to close the upper slide gate 40, and through channel U ₅ to open the lower slide gate 39 and channel U ₃ to disable the vibratory flow inducer 45;

- the temperature in the upper part of the unloading device 4 - the heating zone - according to the signal from the thermocouple 57 through channel X ₆ to MRK 77 with the issuance of the control action through channel Z ₈ through an autonomous power supply 85 through channel U ₁₁ to the electric heater 32;

- the temperature in the lower zone of the lined shaft housing 2 — the pyrolysis zone — by a signal from the thermal converter 52 through channel X ₁ to MRK 77 with the output of a control action through channel Z ₆ through an autonomous power supply 84 through channel U ₉ to two parallel ring discharge electrodes 21 devices 4;

- pressure in the lower zone of the shaft lined casing 2 by a signal from a pressure sensor 65 through channel X ₁₄ to MRK 77 with the issuing of a control action through channel Z ₇ through an autonomous power supply 85 through channel U ₁₀ to the engine 31 of the blower fan 30;

- discharge in the upper zone of the shaft lined casing 2 according to the signal from the discharge sensor 69 in the outlet pipe 7 of the gas phase outlet via channel X ₁₈ to the MPK 77 with the issuing of control action through channel Z ₉ through an autonomous power supply 87 through channel U ₁₂ to the exhaust fan engine 9 8;

- the concentration of carbon (soot) in the outlet pipe 7 of the removal of the gas phase by a signal from the carbon concentration sensor 74 through channel X ₂₃ to MRK 77 with the issuance of a control action through channel Z ₄ through an autonomous power supply 82 through channel U ₇ to the engine 29 of the valve 28 on line 27 for supplying steam to the lower part of the discharge device 4;

- the concentration of oxygen in the air supplied to the input of the blower fan 30, according to the signal from the oxygen concentration sensor 72 through channel X ₂₁ to MRK 77 with the issuance of a control action through channel Z ₅ through an autonomous power supply 83 through channel U ₈ to the motor 34 of the supply valve 33 oxygen 47 to air 46.

In an automated shaft furnace control:

- screw chopper 22, located above the grate 25 with different speed modes on command from MRK 77 through channel Z ₁ through an independent power supply 79 through channel U ₂ to the motor 24 drive auger choppers;

- agitator 36, placed in the ash collector 5, on command from MRK 77 through channel Z ₃ through an autonomous power supply 81 through channel U ₆ to engine 38.

The presence of a blower fan and smoke exhaust with adjustable drives, a heater with adjustable electric heater power in a wide range, two parallel-mounted ring electrodes with adjustable input power, oxygen enrichment of blast air and controlled steam supply, as well as a static multi-channel power source and distributed integrated control system allows choose any temperature regime of pyrolysis and ensure smooth and safe start-up mode of automation constant shaft furnace.

The technical result when using this invention consists in the complete utilization of solid waste, increasing the yield of fuel gas with an increased concentration of the hydrocarbon fraction, as well as providing more reliable operation of an automated shaft furnace.

Claims (1)

An automated shaft furnace for thermal gasification of a mixed composition of various solid components, including a shaft lined casing, a loading device with a lock gate and an unloading device, a hot air supply fan, a heater, air and gas supply pipes, a gas phase outlet pipe connected to a smoke exhaust, conical ash collector and unloading unit, a control module in the form of a microprocessor control controller for generating control actions on the executive the main mechanisms for supplying solid components, gases, air and unloading the finished product, a static multi-channel power source and a personal computer, two sensors for loading solid components located in the upper part of the shaft furnace, and two ash level sensors in the collection, offset in height, thermal converters, located in the shaft lined casing at five points along the height of the casing, in the unloading device, in the ash collector, in the nozzle for supplying hot air to the shaft furnace and in the outlet pipe for exhausting the gas phase and shaft furnace, pressure sensors located at the height of the shaft lined casing at three points, a rarefaction sensor for the gas phase in the outlet pipe, flow sensors for hot air in the pipe for its supply and gas phase in the outlet pipe, oxygen concentration sensors in the air at the inlet to the air heater and carbon in the gas phase of the outlet pipe, multi-channel sensors for the concentration of hydrocarbon and carbon fractions in the gas phase of the outlet pipe, and the discharge device along the circuit is equipped with two parallel distribution laid down ring electrodes with a multi-row screw shredder located below with a grate under it, and a conical ash collector equipped with a cooling jacket, a multi-blade agitator, an unloading unit with a shutter from the lower and upper gates, a vibration flow inducer with scanning frequency and amplitude, the sensor outputs are connected in parallel to microprocessor-based controller and personal computer, outputs from the microprocessor-based controller connected statically to the inputs multichannel power source, the outputs of which are connected to the inputs of the actuators, the heater, to two parallel ring electrodes of the discharge device.

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