RU2435031C1 - Benefication device of above-ore waters of technogenic deposits - Google Patents

Abstract

FIELD: mining. ^ SUBSTANCE: device includes platform with distribution assemblies, which has the possibility of submersion and floating, control unit and scavenging header, which are connected by means of hoses to distribution assemblies of the platform consisting of several hydraulically insulated parts made in the form of hollow communicating vessels. At that, each of the platform parts consists of a set of cells formed with frame pipes and their connections. ^ EFFECT: increasing development efficiency of water-flooded technogenic sites and reducing the dates. ^ 7 cl, 12 dwg

Description

The invention relates to the mining and mining industry, in particular to the development of irrigated technogenic objects (tailing dumps) as a result of the enrichment of above-water waters at the site of their occurrence.

At the present stage of development of the mining industry, there is an increasing need for the use of technogenic mineral deposits containing such industrially important components as uranium (U), gold (Au), rhenium (Re), molybdenum (Mo), scandium (Sc) , tungsten (W), yttrium (Y), rare earth (RZ), lithium (Li), tungsten (V), also copper (Cu), nickel (Ni), zinc (Zn), cobalt (Co), manganese (Mn ) and etc.

A device for the development and enrichment of ore mass (GRM), containing dredge and storage capacity. When transporting the pulp to the aerator unit, it is saturated with reagents and partially aerated, and from the aerator unit, the pulp is unloaded by gravity into a dredging pit where the flotation process is carried out. The foam product from the surface of the dragee pit is removed by a foam trough. From the foam trough, the foam concentrate is forcibly pumped to the flotation concentrate tank. The flotation concentrate is brought directly to the dredge to the required condition or sent to a metallurgical plant for subsequent enrichment (RU 2262987 C1 (Usmanova N.F. et al.), B03D 1/00, B03B 7/00, 02/11/2004). The specified device provides the development and enrichment of timing of irrigated deposits, but does not allow enrichment of above-water in the place of occurrence.

Closest to the proposed design is a device for cleaning the water area from hydrocarbon contaminants, containing a watercraft, with an underwater farm made of articulated parts, and generators of working agents for supplying superheated steam and supercooled gas to the aqueous medium into its surface layer. The underwater farm contains nozzles arranged in cascades in height and in plan for introducing these working agents into the aquatic environment of the water area. The farm is equipped with side boards and floats and is made of modular units interconnected by hinges (RU 2068055 C1 (A.I. Plugin), ЕOВВ 15/10, В63В 35/32, 03/29/1993).

The specified device does not have the possibility of immersion and ascent and, accordingly, does not allow mixing to enrich the above-water of technogenic deposits.

The objective of the invention is to increase the efficiency of the development of irrigated anthropogenic objects and reduce the time of mining by creating a device for enriching the above-water of technogenic deposits, in particular, providing full contact of the entire sludge component in the entire tailings with the solvent at the site of useful components (PC), by mixing aqueous component, timing and solvent.

Another objective of the invention is to simplify the management of the leaching process, its repeated use, low cost of the components of the device, the simplicity and speed of installation and dismantling. Device management involves a minimum energy consumption compared to the process of borehole underground leaching (SST), the minimum time for mining facilities of any area, obtaining the maximum economic effect regardless of the increasing area of the facility, adapting the device to any area of the facility and chemical and technological regulations.

The proposed invention is aimed at saturating the domestic market of Russia with valuable, strategic and radioactive metals in a short time, as well as at ensuring employment of the population of the regions adjacent to such facilities.

The problem is solved in that the device for enriching the above-water of technogenic deposits contains a platform with distribution units, configured for immersion and ascent, a control unit and a pumping manifold connected by hoses to the distribution nodes of the platform, consisting of several parts hydraulically isolated from each other, made in the form of hollow communicating vessels, and each part of the platform consists of a set of cells formed from frame tubes and nodes of their connection.

Mostly the platform consists of four parts.

Preferably, the frame pipes are blind and / or hollow, intact and / or perforated, the connection units of the frame pipes are made in the form of fittings with bends equipped with compression couplings, and some of the fittings are equipped with bends-supports.

Mostly the distribution nodes are located in the center of each part of the platform and consist of four combs, each of which is equipped with ten branches, for connecting additional hoses connected under the platform to the nodes of the frame pipe connection.

Advantageously, the control unit includes a compressor, a pump, shut-off, control valves and a distributor connected to the hoses using quick-release fittings.

Advantageously, the hoses connecting the control unit to the pumping manifold are located under the platform.

Mostly bends-supports are equipped with conical adapters with holes.

The platform can be made in the form of a square 50 × 50 m in size with the possibility of immersion, ascent, capture and discharge of timing of sludge into the upper layers of above-sea water. The platform is controlled on the coastal part of the facility using a control unit connected to the platform by hoses that can be connected into a braid.

Using the platform, an easily-leachable suspension is created, consisting of timing of sludge and above-sea water. The solvent for leaching the timing of the sludge comes from the pumping collector, passing along the entire perimeter of the object, through the braid of hoses into the body of the platform and is evenly distributed over the entire area and volume of the processing facility due to the cellular structure of the platform. The power supply to the control unit comes from the central diesel power station (DES). As indicated above, the platform may consist of four hydraulically isolated parts made in the form of hollow communicating vessels.

Hydraulic isolation of the hollow parts of the platform is ensured by partial perforation of the edge pipes of each part, as well as blind compression couplings connecting the edge frame perforated pipes of each part of the platform. The inner sides of the edge parts of the platform are combined into a central crosspiece, also consisting of perforated polyethylene (PE) pipes and blind fittings. In addition, the corner connecting parts of the entire platform, double-outlet squares and adjacent frame pipes adjacent to them are not perforated and are continuous hollow and hydraulically insulated.

Each part of the platform contains: hollow frame pipes, whole and perforated, supply hoses - central and auxiliary, bends-supports connected to frame pipes by shaped fittings through outlet openings, solvent and air distribution units are located in the center of each part of the device, each distribution unit consists of four distributors connected by shaped fittings, ten auxiliary supply hoses of the same length are connected to each distributor, the other ends of which are connected to the frame through the inlet pipes. All elements of each part of the device are hydraulically connected. Wire-frame pipes, auxiliary supply hoses connected to central solvent and air distribution units, support bends connected perpendicularly to wire-frame hoses are connected by fittings with compression fittings designed for 16 bar pressure. The device is controlled through four supply hoses, one end of which is connected to the air and solvent distribution units under the platform, and the other ends are connected to the control unit located on the coastline of the facility, which includes a compressor, pump, shutoff and distribution valves. Through the nodes of the distribution of air and solvent, a uniform distribution of solvent and air occurs over the entire area and volume of the object using the cellular structure of the platform.

The air and solvent distribution nodes of the platform are a distribution cell with minimal pressure loss and are located at the same distance from each other and from the center of the platform. Each air and solvent distribution unit is located under the frame pipes, and under the air and solvent distribution units there is a maximum volume of auxiliary hoses when filling them with solvent or above-water waters during immersion and maximum buoyancy when surfacing. When compressed air is supplied, auxiliary hoses and air and solvent distribution units are pumped first in the device and form an air cushion in each part of the platform.

When lowering the platform to the surface of the sludge, under the weight of its weight, the platform captures part of the sludge and above-water, which is included in the support bends. When compressed air is supplied to two diagonally opposite parts of the platform, forming an air cushion under the platform, the other two diagonally opposite parts of the platform, mechanically connected with them, move upward with silt and water to the water surface together with the two parts into which air is supplied, as the supply hoses connected to them and the control unit are blocked by shut-off equipment. When the platform reaches the water surface, air is supplied to all parts of the platform, and thus the sludge captured by two diagonally opposite parts of the platform is pushed into the upper layers of the above-water, and the sludge captured by those parts of the platform into which air is immediately supplied is pushed out from the total thickness of the silt in the lower part of the above-sea water, creating a decompression space in the thickness of the silt. Then the shutoff valves on the braid of the hoses remain open, and the air supply stops, in this position the platform is immersed in the silts, capturing new layers.

The proposed design should be individually designed, depending on the shape of the object and its size, while it is possible to increase the number of platform cells or reduce the length of the frame pipes. The design should be modeled individually for each object, subject to the basic principles of descent and ascent.

As the solution, suspension or air will constantly reverse in the hollow space of the device, the issue of hogging is not a concern.

The platform is not a stable floating device, but the hydraulic isolation of all four parts makes the operation of the platform easily controllable with unplanned immersion of one or several of its parts (an experiment was conducted on a laboratory model of the device). The buoyancy of the platform is maintained when it is boosted by air.

A complete revolution of the platform is excluded due to the dimensions of the structure itself, since the side of the platform should be at least twice as deep as the object is being worked out, and also half the platform weight in air (7 t) exceeds half its weight (3.5 t) in water or suspension .

Figure 1 shows a General view of the device located in the perimeter of an object in the ascent;

figure 2 illustrates a top view of one platform and the General scheme. The supply hoses and air and solvent distribution units passing under the platform are shown from above. The platform control unit located on the coastal part of the object, as well as the pumping manifold and the perimeter of the object are shown;

figure 3 illustrates the angular outer cell of the platform (Y1);

figure 4 illustrates the inner cell of the platform (II);

5 illustrates an adjacent cell of the platform (Y3), which is waterproofing and combines two hollow working parts;

figure 6 illustrates the edge cell of the platform (R4), adjacent to the Central cross;

7 illustrates a cell (Y5), uniting the corners of its four parts in the center of the platform, and also shows the places of the outlets of the supply hoses for connecting them to the braid;

on Fig illustrates the edge cell of the platform (6), not adjacent to the Central cross;

figure 9 shows in detail the node distribution of air and solvent (Y7);

figure 10 shows in detail the device bends-supports, exciting the timing of the sludge, and the connection of auxiliary hoses to the frame pipes;

figure 11 shows the structural links of the platform as a whole;

12 shows a platform control unit.

As shown in figure 1, each platform 1 is made with the possibility of immersion, ascent and capture of the timing of the sludge, their discharge into the upper layers of the above-water of technogenic deposits, is controlled from the coastline using the control unit 2.

As shown in figure 2, the solvent for leaching suspended matter is fed into the platform 1 from the pumping manifold 3, through a braid of hoses 4, each platform 1 consists of four hydraulically isolated and mechanically interconnected parts - A, B, C and G.

Each part of the platform A, B, C, D, in turn, consists of cells of various types I1, I2, I3, I4, I5, I6, I7.

Figure 3, 4, 5, 6, 7, 8 shows the component parts of the cells Y1, Y2, Y3, Y4, Y5, Y6 and the types of their connections: the cells consist of PE hollow frame pipes and hollow fittings - elbows, tees and crosses.

Figure 3 shows a cell Я1, consisting of whole blind pipes 5, perforated pipes 6, interconnected by blind tees 7, a square 8, pipes 9, a cross 10 having four outlets for connecting pipes in the form of a cross, and a fifth outlet directed vertically downward from the center of the crosspiece for connection with a branch support (not shown in the drawing).

Figure 4 shows a cell H2 consisting of whole pipes 9, cross pieces 10, cross pieces 11 having four exits for connecting pipes in the form of a cross, and the fifth outlet is directed vertically downward from the center of the connection for attaching an auxiliary hose (not shown in the drawing).

Figure 5 shows a cell Y3, consisting of perforated pipes 6, whole pipes 9, interconnected by crosspieces 10, crosspieces 11 and crosspieces 12 having four outlets for connecting pipes in the form of a cross.

Figure 6 shows cell Я4, consisting of perforated pipes 6, whole pipes 9, interconnected by blind tees 7, cross 10, cross 11 and blind tee 13, equipped with a fourth outlet directed vertically downward from the center of the connection.

Figure 7 shows a cell Y5, consisting of perforated pipes 6 and whole pipes 9, interconnected by crosses 10 and crosses 12. In addition, the cell is equipped with four outlets 14 of the hoses 4.

On Fig depicts a cell 6, consisting of perforated pipes 6 and whole pipes 9, interconnected by a blind tee 7, cross 10, cross 11 and blind tee 13.

In Fig. 9, cell Y7 is shown — a distribution unit consisting of a crosspiece 15 provided with a fifth outlet directed vertically downward from the center of the connection, hollow whole PE hoses 16, combs 17 having ten outlets equipped with outlets 18 with adapter fittings — compression couplings, connected PE curved hoses 19, with bends 18, to which auxiliary hoses 20 are attached.

Figure 10 shows the device of bends-supports, capturing the timing of the sludge, and the connection of auxiliary hoses to pipes 9 interconnected by a spider 11, to the lower output of which an auxiliary hose 20 is connected, and a spider 10, to the lower output of which a support-branch 21 is connected , with holes 22 provided with valves for squeezing air (not shown), formed in a conical welded adapter 23.

11 shows the structural links and components of the platform 1, the base of which are cells of types I1, I2, I3, I4, I5, I6. Cell Y7, part of the supply hoses 4, auxiliary hoses 20, bends-supports 21 are shown. The control unit 2 and the pumping manifold 3 are shown on the shoreline. The platform 1 is connected by hoses 4 woven into a braid with the control unit 2, the device of which is shown in FIG. 12.

As shown in FIG. 12, each control unit 2 comprises a compressor 24 and a pump 25 connected by hoses 26, 27, 28, 29 and 30 to a distribution unit 31 to which hoses 4 of the platform 1 are connected, including four central hoses with taps a, b, c and d, summed up to the corresponding parts of the platform A, B, C and D, through which the control process takes place. Hoses with valves a, b, c and d have the ability to connect and disconnect from the distribution node 31 quick-detachable fittings 32 type "american". A tee 33 is installed in front of distribution unit 31 with a fitting, a tap and a manometer (not shown in the drawing), all hoses in the control unit 2 are equipped with shut-off valves: 34 and 35 on the hose 26; 36 on the hose 27; 37 and 38 on hose 28; 39 and 40 on the hose 29; 41 on the hose 30. A water meter for metering the injected solvent (not shown) is installed on tap 40, and a meter for metering the pumped-out PR solution (not shown) is installed on tap 41.

The evacuation manifold 3 is equipped with a nozzle 42 for injecting solvent, as well as a nozzle 43, for supplying solvent to the perimeter of the tailings, through a hose 30, pump 25 and hoses 28 and 29. The ready-made PR solutions are pumped out to the pumping manifold 3 and their further transportation is carried out through the hose 27 , pump 25 and hose 30. Using a laser diffractometer 44, the depth of the platform 1 is measured and the density of the resulting suspension is measured, and the density of the solvent in the pump manifold 3 is measured with the help of instrumentation 45. Pump 25 s connected to the DES 46 electric wire 47.

The device operates as follows.

All preparatory work is carried out on the shore of the mining facility: installation of equipment and apparatus, assembly of platform 1, installation of pumping manifold 3 and filling it with solvent.

Platform 1 is lowered to the surface of the superficial water. Hoses 4 are connected to the control unit 2. When launching, all the taps (a, b, c and d) on the hoses 4 of the platform 1 are closed.

During the immersion of the first descent part of the platform 1, the supply of compressed air to the immersed part of the platform 1 through the distribution unit 31, and then to the other parts, until the platform 1 acquires a stable floating state, is started. Then, each platform 1 is transported via above-ground water to the place where the irrigated technogenic object is mined mechanically using hoses 4 detached from the distribution unit 31.

The platform 1 has the ability to float to the surface of the above-water by supplying air using a compressor 24. The immersion of the platform 1 into the sludge occurs due to the displacement of air by suspension or above-water, as well as when the solvent is supplied. At each ascent, platform 1 has the ability to capture up to 20 m ^{3 of} sludge and discharge it into the upper and above-water layers, forming an easily leached suspension. Platform 1 is a hollow communicating vessel, divided into four parts A, B, C and G hydraulically isolated from each other, which are controlled by pump 25 and the corresponding valves a, b, c, d.

The immersion of the platform 1 occurs after the cranes a, b, c, d open and the platform 1 is lowered in the above-water water to the surface of the sludge. Above-water, suspension or solvent through the support branches 21 pass into the crosses 10, and from them fall into the crosses 11, from which the flow rushes into the auxiliary hoses 20, then into the cell Y7, and from it into the supply hoses.

In this case, the perforated pipes 6 throughout the dive pass through the contents of the perimeter of the object.

A laser diffractometer 44 tracks the depth of immersion and density of above-water using a detector attached to the center of platform 1 through hoses 4.

The capture of sludge, suspended matter and above-water occurs as follows.

At the end of each dive, when cranes a, b, c, d are open, in platform 1 there are more than 50 m ^{3 of a} mixture of water and sludge. When the laser diffractometer 44 registered the required immersion depth, the taps of two diagonally opposite parts of the platform 1, for example taps (a and d), are shut off and air is supplied through taps (b and c). Cranes (b and c) are blocked as soon as platform 1 is in the middle of the path. Thus, the compressed air supplied in two parts of platform 1 (B and C) forms an air cushion under the pipes 9 and a gas-water suspension in them, which raises the entire platform and a suspension of 20 m ³ in parts (A B, C, D) . Since when lifting platform 1 to parts (A and D), only the lifting force of Archimedes acts, and hydrostatic pressure acts only from below, the whole suspension remains in the hollow volume of the two parts of platform 1 (A and D), and the suspension in parts (B and D) ) is thrown right away. The bends-supports 21 of the platform 1 perform the function of core pipes when drilling wells, and instead of the lifting mechanism, air is used.

The process of air passage is as follows.

From the compressor 24, the compressed air enters the distribution unit 31 through the hoses 26 and 29. During the air intake, the taps 37 and 38 on the hose 28 are closed. While the valve 40 is closed, the taps on the hoses 26 and 29 are open. The pressure gauge on the fitting in front of the valve 40 shows the working pressure of the compressed air supplied.

From the distribution unit 31, the compressed air enters two outlets 13 of the hoses 4, and from them into the cell Я7, which is the distribution unit of the air and the solvent. From each cell R7, through the auxiliary hoses 20, air enters the whole pipes 9, and from them into the openings 22, leaving the perimeter of the object and forming a gas-water mixture and pushing out the timing of the sludge that fell into the outlet support 21, while in two diagonally opposite parts of the platform 1, the timing of the sludge remains in the bends-supports 21 until approaching the water surface.

The air supply for the ascent of the platform can be calculated as follows.

To supply air to the well, the necessary pressure is calculated by the formula (1) (“Heap and underground metal leaching,” edited by S. N. Voloshchuk. M .: Nedra, 1982, p. 47), taking into account the pressure loss

γ is the density of the foamed liquid.

Lx - = (L + S) D ² / d ² - immersion depth of the discharge pipe.

In this case, due to the fact that air injection is only necessary to create an air cushion under the platform, for example, for an object depth of 20 m and a suspension density of 1.15 t / m ^{3, the} starting pressure for floating the platform can be determined by the same formula (one),

where Lx = 20 m and γ = 1.15 t / m ³ .

Thus, P _start = 0.23 MPa or 2.3 atm.

It must be borne in mind that the design of the device involves a large volume of hoses of various diameters and lengths for capturing and moving sludge and water, which are also designed to uniformly supply a large amount of solvent, as well as placing air for ascent. Therefore, the starting and then the operating pressure of the compressor is calculated taking into account pressure losses during air injection.

For example: to ascend a platform

ΔР - pressure drop, bar, = 5.2,

450 is an empirical coefficient,

q _v - productivity, l / s, = 160,

L - hose length, m, = 2560,

d - inner diameter of the hoses, mm, = 77.7,

P is the initial absolute pressure, bar, = 15.

To pop up the device in this case, an operating pressure of 2.5 bar is required to force hydrostatic pressure, pressure loss over the length and fittings and to the transitions of hose diameters will be 5.2 bar, the pressure drop across the receiver is 3.0 bar.

Total, the starting pressure will be (2.5 + 5.2 + 3.0) = 10.7 bar, with a maximum pressure of 15 bar and an operating pressure of 7.7 bar.

With a capacity of 10 m ³ / min, the compressor operating time is 2 minutes.

Calculation of the mass of cargo and the amount of air required to lift the platform.

For example:

The mass of cargo (M _g ) of one platform = 15 t.

Platform Weight supraore water immersion (M _present)

where M _vp - platform displacement

where V _p - platform volume, ρ _n.v. - density of above-water.

Determine the mass of cargo that raises in above-water waters 1 m ^{3 of} air, according to the formula

where ρ of _air is the density of air.

Thus, 1 m ^{3 of} air can lift 0.998 tons of cargo in water with a density of 1 t / m ³ .

Accordingly, 1 m ^{3 of} air can lift in suspension with a density of 1.15 t / m ³ 1.1487 tons of cargo.

where ρ _suspension is the density of the suspension.

For example:

platform weight = 15 t.

Platform weight in water = 15 t - (8 m ³ × 1 t / m ³ ) = 7 t.

The weight of the sludge in four parts of the platform when the bends-supports are fully filled = 20 m ³ * 2.0 t / m ³ = 40 t.

Half of the sludge will be displaced when air is supplied to two parts of the platform, i.e. sludge weight in two parts of the platform, in water = 20 t- (10 m ³ * 1 t / m ³ ) = 10 t.

1 m ^{3 of} air with a density of 0.00129 t / m ³ can lift 998 kg of cargo in water.

The weight of the platform with sludge during the ascent of the platform (10 t silt + 7 t platform) = 17 t.

Two parts of the platform contain air when inflated:

(23/2 + 6.4 / 2) = 14.8 m ³ + 2.8 m ³ stock of buoyancy = 17.6 m ^{3 of} air,

which can lift 17.6 m ³ * 0.998 t / m ³ = 17.57 tons of cargo in water for a given platform weight of 17 tons.

Reliable ascent of the platform is possible in 2 minutes, since 20 m ^{3 of} compressed air will be pumped into the device with a compressor capacity of 10 m ³ / min.

Stirring.

The alternation of air supply to the diagonally opposite parts of the platform and the alternation of overlapping of diagonally opposite parts of the platform during ascent provides for the capture of contents, and then when air is pumped all parts of the platform alternately on the surface of the water, the contents of the object are ejected and mixed.

Solvent supply.

The area of the object is ensured by the uniform distribution of the solvent due to the design of the platform 1, in which for every 6.25 m ^{2 there} are two exits for supplying the solvent. Laser diffractometers are also used to uniformly supply solvent along the depth of the object, which measure the immersion depth of the platform and the varying density of the suspension.

The supply of solvent also occurs through the whole pipes 9 of the platform 1 using the pump 25 and alternating the supply of air and solvent to the diagonally opposite parts of the platform.

Lightening and pumping solutions.

Clarification of solutions occurs in the perimeter of the object when mixing is stopped due to sedimentation of suspended particles under the influence of gravity immediately after the design concentrations of PC in the solution are obtained.

The clarification of the solutions will last from 7 to 14 days, after which the pump 25 is turned 180 ° and the solutions are pumped out through the hose 27 and the hose 30, brought to the pipe 43 in the pump manifold 3.

Surface pumps ХЦМ 20/25 with a capacity of 20 m ³ / h with a pressure of 25 m are most convenient for the proposed pumping of solutions.

The solution is pumped into the pumping manifold 3, and then transported along it to obtain commodity regenerates.

Thus, it is possible to increase the efficiency of the development of irrigated technogenic objects and reduce the terms of development by creating a device for the enrichment of the above-water of technogenic deposits, in particular, a single capture of the timing of sludge with support bends is comparable to the removal of core material in the form of shortened 1.5 m runs from 80 wells simultaneously in one round-trip operation, after which full contact of the entire removed sludge component of the tailings with the solvent at the place of occurrence due to equal solvent supply by area and volume of the object. The uniformity of mining is achieved due to the cellular structure of the platform and the alternation of the work of its hydraulically isolated parts.

The proposed device allows you to get in a short time (up to 1 year) a large number of productive solutions containing important for industry and strategically important PCs, including Au, U, Re, W, Cu. In addition, the proposed device allows to simplify the management of the metal beneficiation process, reliably and in a short time to clean the insoluble residual content of the sludge from the processed objects from environmentally harmful components, and thereby increase the environmental safety of the regions.

It will be apparent to one skilled in the art that various modifications and changes are possible in the present invention. Accordingly, it is intended that the present invention covers the modifications and variations as well as their equivalents without departing from the spirit and scope of the invention disclosed in the appended claims.

Claims (7)

1. A device for enriching the above-water of technogenic deposits, comprising a platform with distribution units made with the possibility of immersion and ascent, a control unit and pumping manifold connected by hoses to the distribution units of the platform, consisting of several parts hydraulically isolated from each other, made in the form of hollow communicating vessels, and each of the parts of the platform consists of a set of cells formed from frame tubes and nodes of their connection. 2. The device according to claim 1, characterized in that the platform consists of four parts. 3. The device according to claim 1, characterized in that the frame pipes are made blind and / or hollow, intact and / or perforated, the connection nodes of the frame pipes are made in the form of fittings with bends equipped with compression couplings, and some of the fittings are equipped with bends-supports . 4. The device according to claim 3, characterized in that the distribution nodes are located in the center of each part of the platform and consist of four combs, each of which is equipped with ten bends for connecting additional hoses connected under the platform to the frame pipe connection nodes. 5. The device according to claim 1, characterized in that the control unit includes a compressor, a pump, shut-off, control valves and a distributor associated with hoses using quick-release fittings. 6. The device according to claim 5, characterized in that the hoses connecting the control unit to the pumping manifold are located under the platform. 7. The device according to claim 3, characterized in that the bends-supports are equipped with conical adapters with holes equipped with valves.

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