RU2735307C1 - Method for vortex processing of mechanical mixtures with simultaneous enclosure of economic objects from action of moving flows of mechanical mixtures - Google Patents

Abstract

FIELD: physics.

SUBSTANCE: invention is intended for vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from action of moving flows of mechanical mixtures. Method of processing consists in the fact that the economic object is enclosed by a screen consisting of a set of vortex modules containing process lines, at least one, which include at least one process line consisting of vortex equipment process stages, not less than one, including swirlers, confusers, cyclones - confusers, overpasses, accumulators, using which processing of mechanical mixtures supplied from the supercharger is performed using a vortex effect of the confuser, performing cleaning, separation, movement and accumulation of products of processing of mechanical mixture in required concentration of included components and their separation into specific materials used in practical activities and semi-products, transportation of said materials and semi-finished products to packing points for further implementation or environmentally safe disposal. Due to use of modularity of vortex equipment, its invariance in quantity and sequence of arrangement, effective damping of head of moving flow is obtained by forming opposite, vertical, inclined flow of exhaust air from technical devices, thus deforming existing structure of head of moving main flow of mixture.

EFFECT: technical result is high efficiency of the process.

6 cl, 4 dwg

Description

All types of moving streams of mechanical mixtures formed both by natural phenomena (all types of winds) and by man-made causes (smoke flows of boiler pipes, pipes of metallurgical furnaces, exhaust gases) can be referred to the moving flows of the environment.

The vortex method of complex processing and purification of mechanical mixtures from mechanical contamination by impurities of moving streams of mechanical mixtures is used using the properties of vortex flows and separators - confusers, cyclones - confusers and is intended, by definition, to purify streams of mechanical mixtures from mechanical impurities. The proposed vortex method of complex processing and purification from mechanical pollution by impurities of moving streams of mechanical mixtures will find application in almost all sectors of the country's economy: oil, oil refining, chemical, energy, coal. The method will be an effective tool in the field of environmental protection, solutions to environmental issues.

The method can be used for the extraction of minerals from the winds of the environment, accompanying their mining or loading in an open way, for example, coal. The port city of Nakhodka is literally covered with coal dust, which accompanies the transshipment of coal from railway wagons to dry cargo ships.

A promising direction for reducing losses, reducing environmental harm is to reduce emissions and unused waste directly in the technological production process, including for the generation of electrical and / or heat energy from the captured combustion products.

In the steppe zone, wind sandstorms cause enormous damage. Environmental disasters accompany the development of quarries for mining. In world practice, as examples of the fight against natural sandstorms, dry winds, forest plantations, water barriers are best known.

The proposed present "Method for vortex processing of mechanical mixtures with the simultaneous protection of economic objects from the effect of moving streams of mechanical mixtures on them" uses the properties of the physical process first described in the invention of the authors: V.P. Kuznetsov, O.A. Sharikov, M.O. Sharikov ., patent for invention No. 2475310 publ. 02/20/2013, Bul. No. 5. "A method for separating mechanical mixtures based on the use of the properties of a vortex flow and the use of a vortex separator - confuser."

The method, in addition to the protective function, can be used for the extraction of minerals from the air masses of sandstorms, dusty winds, from the smoke streams of boiler pipes in power engineering, metallurgy, etc. Due to the modular design of the barrier screen, it is mobile, easily and quickly reconfigured depending on the direction of flow, its strength, the content of components, the state of the materials to be processed and the environment.

The task of increasing the efficiency of methods of cleaning from mechanical pollution by impurities of air flows of the environment is solved: by using the known property of vortex flows to form axial and peripheral layers; the use of a physical process - the vortex effect of the confuser: the creation on this basis, a method of complex purification of impurities from the moving air streams using the proposed separators - confusers, cyclones - confusers.

Disclosure of the invention.

The method of vortex complex processing, cleaning from mechanical impurities, with simultaneous protection of economic objects from the impact of moving streams of mechanical mixtures on them, consists of:

• in crushing the pressure of the moving mass of the mechanical mixture into jets, followed by the formation of vortex flows from them, with impurities entrained by the mass of the mixture in the course of its movement;

• in the separation of impurities of vortex flows of mechanical mixtures;

• in the development, by vortex processing, of substances, the required concentration of the composition of the components and their combination;

• in the simultaneous enrichment of the obtained semi-finished products and their division into specific materials used in practice.

• in the creation of devices with the use of which the method is implemented, and which are at the same time a fence from the moving streams of mechanical mixtures.

In the implementation of the method, devices are used, connected to one of the intake discharge cones, working jointly or independently from each other, vortex technological modules, using vortex separators (separators - confusers, cyclones - confusers), which can be grouped into batteries of various sizes and various configurations ... Each of the vortex technological modules consists of at least one intake discharge cone, one or more, combined for the purpose of complex processing of the obtained semi-finished products, technological lines of equipment, in accordance with the state of the processing object and the used production facilities. Technological lines, in turn, consist of one or more lines of equipment and separation stages. Separation stages consist of one or several devices, directly separation, the results of which are the technological redistribution of separation, as well as equipment for control of the work process and technological overpasses. Vortex separators - confusers and vortex cyclones - confusers, which use in their work the physical process - "vortex confuser effect", are used as separators directly.

In accordance with the needs in each technological line of the equipment, there is a certain amount of control and measuring equipment and control devices.

The technological process of complex processing and purification from mechanical pollution by impurities of moving air flows of the environment using the properties of vortex flows and separators - confusers, cyclones - confusers, is illustrated in Fig. 1. "Schematic diagram of the method of vortex processing of mechanical mixtures with the simultaneous protection of economic objects from the effects of moving streams of mechanical mixtures on them." The complex works as follows.

From the intake discharge cone "1", entrained by the pressure (boost), the mass of the mechanical mixture enters the swirler "3" of the separator - confuser "4" of the first stage of the first technological line. In the swirler "3" the flow swirls, the formation of peripheral and axial layers. In the process of flow movement, in the vortex tube of the swirler "3" under the influence of pressure drop forces, friction of particles against the wall of the vortex tube, mutual collisions of particles, their destruction occurs, crushing into smaller particles and groups. At the same time, there is a separation of the flow under the action of centrifugal forces into dense and light layers: the densest particles move away from the axis to the wall of the vortex tube, the particles of light components, less dense are grouped in the axial layers of the swirling flow. From the vortex tube of the swirler "3", the flow moves to the separator - confuser "4", where, after contact with the wall of the confuser, it is divided into two oppositely directed vortex flows. The less dense particles of the flow, in the composition of the axial layers, continue to move in the direction of the initial movement of the vortex flow, the denser particles of the flow, from the peripheral layer, change the direction of their axial movement, in the opposite direction, forming a counter-main, vortex flow.

The hardware part of the complex technological process is further explained in FIG. 3. "Process flow diagram of the separator - confuser" and FIG. 4. "Technological scheme of functioning of the cyclone - confuser".

FIG. 3. Description of the technological scheme of the separator - confuser.

Let us consider the physical process of the formation of a counter vortex in a confuser separator using the example of the first confuser separator of the first technological line “4”. Involved in the intake discharge cone "1", the mass of the mechanical mixture "23" enters tangentially into the swirler "3" of the first separator - confuser of the first stage of the first line. In the swirler "3", a vortex flow "24" is formed, in which the peripheral and axial layers are formed. The formed vortex flow "24" moves to the separator - confuser "4", in which the densest particles of the mixture are separated from the peripheral layers into the oncoming vortex, which is diverted through the passage "22" into the swirler "10" of the neighboring separator - confuser "11" for further processing.

The physical process of the formation of a counter vortex in the confuser separator is the main result of the vortex confuser effect. As the swirling flow moves along the axis of the separator - confuser to the smaller base, the particles of the peripheral layer, under the influence of frictional forces and viscosity, are decelerated, down to zero value of their axial translational velocity, which leads to an increase in pressure in the layer. At the same time, in front of the ring of "hindered" but rotating particles, due to ejection during the movement of particles of the axial layer, there is a decrease in pressure in the closed confuser space, zone "F", which leads to a "pressure drop", and which squeezes out the particles from the layer " retarded "particles, and centrifugal forces press them against the expanding confuser wall. Under the influence of a pressure drop, centrifugal force, the particles change their movements in the opposite direction. Thus, a counter vortex is formed in the separator - confuser, which moves along the axis of the confuser, but towards the larger one, its base and is diverted through the hole in the side wall of the separator - confuser along the "22" overpass, into the swirler "10" of the first separator - confuser the second technological line "11".

The axial layers and the remaining less dense particles of the mixture move as a vortex flow into the next separator - confuser "5", in which, in turn, under the influence of centrifugal force, new axial and peripheral layers are formed. The most dense particles are separated from the peripheral layers into the oncoming vortex of the separator - confuser of the first stage "5", which is diverted along the overpass "7" to the cyclone adjacent in motion - confuser "8". The axial layers and the remaining less dense particles of the peripheral layers of the newly formed vortex flow move into the axial hole in the smaller base of the confuser separator "5" into the overpass - accumulator "6" of the first stage redistribution (waste). FIG. 4. Technological scheme of the cyclone - confuser operation.

We will consider the technological scheme of the cyclone - confuser using the example of the first cyclone - confuser of the first technological line "8". The mass of the mixture to be processed from the separator - confuser "5" is fed through the overpass "7" at the larger base of the cyclone - confuser "8". Entering tangentially into the cyclone - confuser "8", the mixture swirls, forming axial "29" and peripheral "28" layers in the resulting vortex flow. The denser particles of the mixture, under the influence of the pressure drop and centrifugal force, move closer to the tapering wall of the cyclone - confuser, less dense to its axis. As the swirling flow moves along the axis of the cyclone - confuser to the smaller base, in the peripheral layers, under the influence of the tapering shape of the cyclone - confuser, additional compaction of the peripheral layer of the flow occurs. The particles of the peripheral layer, under the influence of frictional forces and viscosity, are decelerated, up to a zero value of the translational velocity and a simultaneous increase in pressure in the layer. An increase in pressure in the ring of "inhibited" particles of the peripheral layer with a simultaneous decrease in pressure in the confined space of the confuser, zone "F", leads to a "pressure drop", which squeezes out the particles into the space where the pressure is lower. The closed space "F" is formed in front of the loop of "hindered" particles, because in front of the inclined confuser wall, on top of the moving axial layer of less dense particles. By their motion, the axial particles create an ejection, which increases the vacuum in the inter-turn space. The buoyant force of the pressure drop is directed against the original direction of the flow, the centrifugal force presses the squeezed out particles against the expanding wall of the cyclone - confuser. The particles of the mixture squeezed out of the loop continue to move, but, already, in the opposite direction to the initial flow. Thus, a counter flow "27" is formed in the cyclone - confuser. Moving towards the side wall of the confuser, towards the larger base, the counter flow enters the hole in the wall for the overpass "13". Along the overpass "13" isolated particles are removed into the next cyclone in the first technological line - confuser "15", in which a similar process is repeated, but with the formation of a new vortex flow. The rest of the swirling flow that entered the cyclone-confuser “8” continues its movement into the axial hole in the smaller base of the cyclone-confuser, into the redistribution accumulator “9”.

Description of the technological scheme of the process in the complex.

The mass of the mechanical mixture “23”, which entered the intake discharge cone “1”, moves tangentially into the swirler “3” of the first separator - the confuser of the first stage of the first line and then, sequentially, from apparatus to apparatus, its technological processing and purification according to the described technological schemes. As a result of the sequential movement of the mixture from one separator to another separator, with its simultaneous separation, during which the particles of one component are separated from the particles of other components of the mixture, the particles of the "useful components" are separated from the "impurities", with a concomitant change in the concentrations of the components in mixtures, that is, enrichment, using the objective property of particles - density - "less dense", "denser", with the use of methods for controlling the parameters of separation, concentration, ensuring a given quality of processes - ready materials or semi-finished products are obtained.

Divided layers of the flow along the overpasses, each move according to its purpose. Axial layers, less dense particles move into the axial hole in the smaller base of the separator - confuser "4" and enter the next separator in the line along the flow direction - confuser "5". In the "5" confuser separator, further separation of the flow and separation of the densest particles are carried out with the simultaneous formation of new peripheral and axial layers. From the newly formed peripheral layer, a counter flow is formed, which moves along the "7" overpass to the adjacent one, the first cyclone is the confuser "8" of the second stage of the first ruler, and the axial layers and less dense particles move through the axial hole in the smaller base of the cyclone - confuser " 5 "into the overpass - the accumulator of redistribution (waste) of the second stage of the first line" 9 ". The counter vortex from the separator - confuser "4" moves along the overpass "22" tangentially into the swirler "10" of the separator - confuser of the first stage of the second line "11", in which, again, it swirls and under the action of centrifugal force axial and peripheral layers are formed in it ... The axial layers in the separator - confuser of the first stage of the second line "11" move into its axial hole in the smaller base, then they enter the storage for the redistribution (waste) of the first stage of the second line "12". At the same time, in the cyclone - confuser of the second stage of the first line "8", the incoming stream is divided into two streams. Formed, from the particles of the peripheral layer, the oncoming flow moves along the overpass "13" to the adjacent cyclone - the confuser of the third stage of the first line "15", in which it is divided into two streams: the oncoming flow moves along the overpass to the accumulator of conversions (waste) of the first line "16" ; the axial flow in the cyclone-confuser "15" moves to the axial hole in the smaller base, then, to the accumulator of redistribution (waste) of the third stage of the first line "14".

In the second line, the counter flow formed from the particles of the peripheral layer, in the separator - confuser "11" moves along the overpass to the adjacent cyclone - the confuser of the second stage of the second line "18", in which it is divided into flows: counter and axial. The counter flow from the cyclone - confuser "18" moves along the overpass to the accumulator of conversions (waste) "17", and the axial flow moves into the axial opening in the smaller base of the cyclone into the next cyclone - confuser of the third stage of the second line "19". In the cyclone-confuser "19" the incoming flow is again divided into an axial layer and a peripheral layer, from which a counter vortex is formed. The oncoming vortex along the overpass moves to the accumulator of redistribution (waste) of the second line "20", and the axial layer and less dense particles move into the axial hole in the smaller base of the cyclone - confuser into the accumulator of conversions (axial layers) of the third stage of the second line "21".

The configuration of the processing line of the module can be additionally completed with known technological equipment, for example, overpasses, taking into account the composition and condition of the processed mixture, production capabilities and tasks for processing the mixture.

At the end of the technological operations of the first stage of processing and according to the results of the analysis of the concentration of components in the redistribution of the mixture, which are in the technological storage tanks of the processing (waste), the subsequent, second stage of processing of the contaminated mixture continues. The volumes of redistribution (waste) of the mixture are further processed as semi-finished products, or, as finished products, in packaging, or final disposal.

In addition, due to the use of the modularity of vortex equipment, its invariance in the number and sequence of spatial arrangement, it is possible to obtain useful products, a useful weakening of the head of a moving stream, by forming counter, vertical, oblique outflows, including exhaust air from technical devices, thus deforming the existing structure of the head of the moving main flow of the mixture. Vortex tubes, devices of vortex equipment can be placed vertically, horizontally, based on the expediency, efficiency of solving the problems of processing the mixture, the tasks of fencing economic facilities.

The description uses the attribute "mechanical mixture". A well-known definition of the form of existence of matter. A mechanical mixture is formed in cases where the components are not capable of mutual dissolution in the solid state and do not form a chemical compound with each other. The formation of a mechanical mixture occurs at any ratio of components. (Great Encyclopedia of Oil and Gas). Processing (separation) of the mechanical mixture in the claimed method is carried out using the objective physical property of material particles, namely, density. Therefore, all types of mechanical mixtures in any form of existence are subject to processing in the method: gaseous, liquid, solid or free-flowing. For example, purification of water from impurities, processing of mixtures of grain materials, processing of sands of minerals, their enrichment by changing the ratio of the concentration of impurity components, dust separation, purification of boiler pipe smoke, etc.

The signs "separator - confuser", "cyclone - confuser" are well-known technological equipment that has been used for a long time and repeatedly in publications of technical literature, for example,

1. Kuznetsov V.I., Sharikov O.A. Some suggestions for a variant of the differential equation of the physical process - vortex confuser effect. // Omsk Scientific Bulletin. 2015 Series. "Devices, machines and technologies". No. 1 (137). S. 33-37.

2. Kuznetsov V.I., Sharikov O.A. New physical processes in the latest production technologies. // Scientific publication. FSBEI HE Omsk GAU, Materials of the youth forum. 2016 S. 29-34.

3. Kuznetsov V.I., Sharikov O.A. A method for the complex processing of a mechanical mixture using the properties of the vortex confuser effect. // Omsk Scientific Bulletin. 2015 Series. "Devices, machines and technologies". No. 1 (137). S. 38-41.

Description of drawings.

Description of drawings. FIG. 1 "Schematic diagram of the method of vortex processing of mechanical mixtures with the simultaneous protection of economic objects from the effects of moving streams of mechanical mixtures on them."

1 Suction discharge cone.

2 Pumped clogged mechanical mixture.

3. Swirler separator - confuser of the first stage of the second line

4. Separator - confuser of the 1st stage of the second line

5. Separator - confuser of the 2nd stage of the first line

7. Overpass from the separator - confuser of the second stage to the cyclone - confuser of the first stage of the first line;

8. Cyclone - confuser of the first stage of the first line;

9. Accumulator for redistribution (waste) of the first stage of the first line;

10 Swirler separator - confuser of the first stage of the second line;

11 Separator - confuser of the first stage of the second line;

12. Accumulator for redistribution (waste) of the first stage of the second line;

13. Overpass from cyclone - confuser of the second stage to cyclone - confuser of the third stage of the first line;

14. Accumulator for redistribution of the third stage of the first line;

15. Cyclone - confuser of the third stage of the first line;

16. Accumulator for redistribution (waste) of the second line;

17. Accumulator for redistribution (waste) of the second stage of the second line;

18 Cyclone - confuser of the second stage of the second line;

19 Cyclone is a confuser of the third stage of the second line.

20 Accumulator for redistribution (waste) of the third stage of the second line;

21. Redistribution accumulator (axial layers) of the third stage of the second line;

22. Overpass from the separator - confuser of the 1st stage of the 1st ruler to the swirler of the separator - confuser of the first stage of the second ruler;

Description of drawings. FIG. 2. "Schematic diagram of the method of vortex processing of mechanical mixtures with the simultaneous protection of economic objects from the effects of moving streams of mechanical mixtures on them." Side view.

2. Pumped clogged mechanical mixture.

12. Accumulator for redistribution (waste) of the first stage separators;

16. Accumulator of redistribution of separators of the first line lines.

22. Overpass from the separator - confuser of the 1st stage of the 1st ruler to the swirler of the separator - confuser of the first stage of the second ruler; Description of drawings.

Fig 3. "Flow diagram of the separator - confuser".

3. Swirler separator - confuser of the first stage of the first line

4. Separator - confuser of the 1st stage of the second line

5. Separator - confuser of the 2nd stage of the first line

7. Overpass from the separator - confuser of the second stage to the cyclone - confuser of the first stage of the first line.

8. Cyclone - confuser of the first stage of the first line;

9. Accumulator for redistribution (waste) of the first stage of the first line;

22. Overpass from the separator - confuser of the 1st stage of the 1st line to the swirler of the separator - confuser of the first stage of the second line

23. The mass of the mechanical mixture from the intake discharge cone;

24. Formed counter vortex flow in the swirler from the mechanical mixture received from the intake discharge cone

Description of drawings.

Fig 4. "Flow diagram of the functioning of the cyclone - confuser".

7. Overpass from the separator - confuser of the second stage to the cyclone - confuser of the first stage of the first line.

8. Cyclone - confuser of the first stage of the first line;

13. Overpass from cyclone - confuser of the second stage to cyclone - confuser of the third stage of the first line;

26. The main vortex flow in the cyclone - confuser, from the incoming flow from the separator - confuser "11" along the overpass 25.

27 Counter vortex to the main one in the cyclone - confuser;

28. Peripheral layer of the main vortex flow;

29. Axial layers of the main vortex flow.

Implementation of the method.

People have long wanted to tame wind power: windmills and sailing ships are real examples of wind power in the past. Windmills were used to grind grain in Persia as early as 200 BC. Windmills that generate electricity first appeared in the 19th century in Denmark. The predecessor of modern wind farms, power plants with a horizontal axis had a capacity of 100 kW and was built in 1931 in Yalta. It had a tower 30 meters high.

The vortex effect of the confuser allowed for the innovative use of the energy of moving streams, including winds. In the solutions of the proposed method, the moving stream is divided into jets, which move along the viaducts to the swirlers, in which the involved jets swirl, forming vortex flows. The device simultaneously: splits the moving stream into jets, deflects the pressure, its direct force, away from the head-on collision, thereby reducing the load on the “fence” and, at the same time, swirling the stream. It twists it in such a way that, further, during its advancement, already divided and twisted, it does a lot of useful things. A multistage vortex processing of the mechanical mixture in vortex flows is carried out, which is carried out along a sequential technological chain, from the swirler to the separator - confuser, then, either to the next swirler, or to the separator - confuser, or to the cyclone - confuser, until the desired product of the mixture processing is obtained. Perhaps additional equipment, including special technological equipment, for example, for generating electricity, as a source of alternative wind power or a fan.

In the process of applying the method, it is envisaged to perform two important practical tasks.

1. Economic, social objects are fenced off from the impact of moving streams of mechanical mixtures. The protective function of the method equipment will allow to save many objects of farms and enterprises from the effects of natural and man-made disasters, including possible harmful effects and destruction.

2. Processing of mechanical mixtures carried by moving streams and winds is carried out. The ability to remove any suspended particles from the stream allows you to completely abandon the use of any filtering materials in cleaning systems. Simultaneous separation and processing of the resulting semi-finished products, materials and substances, allows you to return products that, with existing technological processes, simply fly into the pipe, and often brings environmental harm. In the method, the air flow spent in the system, as an alternative source, can be used to generate electricity by this flow, including, for example, for self-sufficiency of the device.

The implementation of the method consists in the manufacture of the proposed technological scheme of equipment functioning with subsequent use in the working process. The equipment is structurally simple, it has no moving parts, parts, as such, technological to manufacture. Manufacturing is possible in every mechanical workshop. To date, a working model has been made, which was demonstrated at the exhibition "Innovation of the Year" in Omsk, May 29-30, 2019.

Information sources do not contain information about the world practice of using analogs of the proposed method or devices.

Bibliographic list.

1. Kuznetsov V.I. "Theory and calculation of the Rank effect". Scientific publication. / IN AND. Kuznetsov. - Omsk: Publishing house. OMGTU, 1994 .-- 217 p.

2. Pat. 2475310 RF, C2. Method of separation of mechanical mixtures based on the use of vortex flow properties and the use of a vortex separator - confuser / V.I. Kuznetsov, O.A. Sharikov, M.O. Sharikov; patent holders Viktor Ivanovich Kuznetsov, Oleg Alekseevich Sharikov, Marat Olegovich Sharikov. - No. 2010131618/05; declared 07/27/2010; publ. 02/20/2013, Bul. No. 5.

1. Kuznetsov V.I., Sharikov O.A. Some suggestions for a variant of the differential equation of the physical process - vortex confuser effect. // Omsk Scientific Bulletin. 2015 Series. "Devices, machines and technologies". No. 1 (137). S. 33-37.

2. Kuznetsov V.I., Sharikov O.A. New physical processes in the latest production technologies. // Scientific publication. FSBEI HE Omsk GAU, Materials of the youth forum. 2016 S. 29-34.

3. Kuznetsov V.I., Sharikov O.A. A method for the complex processing of a mechanical mixture using the properties of the vortex confuser effect. // Omsk Scientific Bulletin. 2015 Series. "Devices, machines and technologies". No. 1 (137). S. 38-41.

Claims (6)

1. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the impact of moving streams of mechanical mixtures on them, which consists in the fact that the economic object is fenced off by a screen consisting of a set of vortex modules containing technological lines, at least one, which include includes at least one technological line, consisting of technological stages of vortex equipment, at least one, including swirlers, confuser separators, confuser cyclones, overpasses, accumulators, using which mechanical mixtures received from the blower are processed using the vortex effect confuser, purification, separation, movement and accumulation of the products of processing of the mechanical mixture in the required concentration of the included components in it and their separation into specific materials and semi-finished products used in practice are carried out, transported transfer of these materials and semi-finished products to the places of packaging for further sale or environmentally friendly disposal. 2. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the impact of moving streams of mechanical mixtures on them according to claim 1, in which the used technological scheme is based on the modular principle of equipment configuration with an invariant technological arrangement in space, the quantitative ratio of the components of the technological scheme elements. 3. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the effect of moving streams of mechanical mixtures on them according to claim 1, in which the vortex modules and the applied vortex equipment are assembled in a configuration to implement a barrier function from the moving flow of mechanical mixture. 4. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the impact of moving streams of mechanical mixtures on them according to claim 1, in which the head of a flow of a moving mass of a mechanical mixture is divided into jets with the subsequent formation of vortex flows from them with impurities entrained by them in the process of its movement. 5. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the effect of moving streams of mechanical mixtures on them according to claim 1, in which the configuration of the vortex modules of the device, their direction, mutual spatial arrangement provides a constant pressure force of the moving stream, uniform distribution of pressure flow by modules. 6. A method of vortex complex processing of moving mechanical mixtures with simultaneous protection of economic objects from the effect of moving streams of mechanical mixtures on them according to claim 1, in which, due to the use of modularity of vortex equipment, its invariance in the number and sequence of arrangement, useful products are obtained, useful weakening of pressure a moving stream by forming counter, vertical, oblique outflows, including exhaust air from technical devices, while deforming the existing structure of the moving main stream of the mixture.

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