WO2017068209A1

WO2017068209A1 - Gas vacuum pump and operating methods thereof

Info

Publication number: WO2017068209A1
Application number: PCT/ES2016/000118
Authority: WO
Inventors: Sergio SALAS LAMELAS
Original assignee: Salas Lamelas Sergio
Priority date: 2015-10-20
Filing date: 2016-10-19
Publication date: 2017-04-27

Abstract

The invention relates to a gas vacuum pump and to the operating methods thereof, disclosing the operation of a new pumping system and four operating methods.

Description

Gas depression pump and its operating procedures.

The gas depression pump of my invention introduces a new high performance pressure liquid delivery system with multiple applications.

There are currently three basic types of pumps that have a stable flow, centrifugal pumps, rotary pumps and reciprocating pumps. Apart from their mechanical differences, they all involve different mechanical systems that directly push the liquid with a mechanical system driven by an engine. On the other hand, there are ram pumps that, by discarding part of the liquid, accumulate their kinetic and potential energy for a while and then give the liquid a push in a shorter time, causing part of the liquid to exceed the hydrostatic height of the initial liquid. These accumulate the energy in a pneumatic way by discarding liquid and this pressurized gas drives part of the liquid.

Finally, it is also necessary to mention the pumping systems by means of a pneumatic compressor, which compress gas to decompress it by expelling liquid from a closed container.

The reality is that my invention, the gas depression pump introduces a new high performance pumping system. The gaseous depression pump is different from all current pumping systems, it is a pumping system but it needs its own classification system within the oil-hydraulic pumps, the gaseous depression pumping system needs to operate by nature liquid with depth in a stable gravitational system. And apart from this it needs a very low energy expenditure with respect to all current pumping systems.

The invention of the gas depression pumping system has as a consequence that the current centrifugal, rotary, reciprocating, ram and pumping pump systems and pneumatic compressor systems become obsolete given their low performance with respect to the pump for gas depression and the operation procedures of it.

To pump pressurized liquids with the gaseous depression pump, a very low energy expenditure is needed. This high performance means that industrial processes where pressure fluids are needed are improved.

In this text I describe the components of the pump for gas depression and the four operating procedures that I have invented for it.

In the first procedure of operation of the pump for gas depression I describe its application of simple pumping. In the second pump operation procedure by

Gas depression described its application as a complex pumping system. In the third procedure of operation of the pumping system for gas depression I describe its

Application as hydroelectric generator. In the fourth operation procedure of the pumping system by

Gas depression described its application as a hydropneumatic generator.

Because of its usefulness to humanity, it is necessary to describe these four operating procedures. The first procedure of operation of the gas depression pump is the most usual, the second procedure of

operation gives an example of use that has certain industrial advantages in specific situations with respect to the first, maintenance costs are reduced, since it is not necessary to have auxiliary pumps at the stops and in addition the stability of the supply without complexes is guaranteed

control systems.

The third and fourth operating procedure of the gaseous depression pump describes its application as an energy generator that provides a basic, clean and high availability energy, this application is not evident if it is not properly stated and given the important energy and environmental problems that humanity is suffering today, that they come to threaten their own survival, it is an act of responsibility to describe these two procedures of operation of the pump for gas depression in their

application to generate energy where for its production it is necessary to reuse a small part of the generated energy.

The gas depression pump and its operating procedures have an important industrial application since it introduces a significant improvement in performance

mechanic of the previous systems arriving in the applications of pumping system to multiply the performance of the previous technology in something more than 3000 times and in its

Hydropneumatic generator application multiplies by more than 600 times the performance of my previous inventions. The fact that the gas depression pump and

operating procedures of the same use less energy to achieve the same results means a significant improvement in costs in all its applications, which makes its use economically interesting

industrial in all available applications.

The fact that the gas depression pump and

operating procedures use less energy to achieve the same result in your pumping applications, it means that it will be necessary to emit less greenhouse gases to pump the same amount of liquid and therefore will make your industrial application more interesting from the point of view environmental. The fact that the gas depression pump and

operating procedures of the same use less energy means that in your application of power generator,

specifically in the application of the pumping system of gaseous depression as a hydropneumatic generator will be

I need to reuse less energy than in my previous inventions ES201201016, ES2Q1400920 and ES2C1401065 so that it works better than more than six hundred times the

ES201201016, ES201400920 and ES201401065 performance. My invention of ES201201016 was an important advance in the transmission system that to date had been in systems that generated movement based on the variation of buoyancy in tanks that flow through the

depth of a liquid because in none of the previous inventions there is a real mechanical solution so that the coupling axis of the electric generator always rotates in the same direction and allows when the mobile tank moves up and has to change direction to reach the surface and move down the generator shaft keep moving in the same direction.

With my invention of the ES201400920 there is an important advance in terms of the performance of this type of power generation machines due to buoyancy variation, because here I describe a system that improves and greatly improves its performance, by reusing compressed gas.

With my subsequent invention of ES201401065 I introduce a much more profitable way to make the gas liquid exchange, making the reuse of compressed gas more profitable.

With my last invention gas depression pump and

operating procedures of the same I introduce a new system and four new procedures that follow other operating principles regarding the currently known pumping systems, centrifugal pumps, rotary pumps, reciprocating pumps, ram pumps and pneumatic compressor pumping systems. The pump for gas depression takes advantage of the lower state

energy of the pressurized gas in motion that passes through a narrowing with respect to liquids with some depth. The fundamental fact is that pumping liquid by moving gas in the way that the gaseous depression pump does and

Operating procedures require less energy than moving a liquid using centrifugal, rotary, reciprocating, ram and pneumatic compressor systems.

The gaseous depression pump and its operating procedures move pressurized gas in a closed circuit for the pressurized gas, but open for the liquid, which allows the depressurized liquid to enter and exit to the liquid

Pressurized by another part of the pressurized gas circuit in motion of the gas depression pump, which is a new method, with inventive activity and high industrial application.

If you have a machine like ES201201016, ES201400920 and

ES201401065 that is capable of producing energy base, environmentally responsible, high availability in a stable gravitational environment, with a liquid with depth by reusing part of the generated energy, it is interesting, it is even more interesting to use the new invention gas depression pump and its operating procedures in its generator application

Hydropneumatic that takes the advantages ES201201016, ES2014G0920 and ES201401065 and improves the best previous performance in more than 600 times what it generates, high availability and environmentally responsible base energy, much better, reusing much less energy from the generated and increasing in more than 60G times its industrial application.

In addition to that it takes less work hours to build it.

To understand the industrial application of the gas depression pumping system and its operating procedures in its applications as an energy generator, I must also explain the obvious differences from the standpoint of availability. Current renewable energy systems are highly variable in their power due to the vagaries of the

nature, lack of wind, night, lack of rain, lack of waves, and that the rest of the energies carry certain ecological-sanitary risks, as well as economic ones because fossil energies tend to end, I understand that the gaseous depression pump and Operating procedures of the same in its application of energy generator due to the fact that its operation does not depend on the vagaries of nature, and is available all the time improve its interest from the industrial point of view.

Recall that for the gaseous depression pump to work in its application as a hydropneumatic generator described in the fourth procedure, only liquid with depth, a stable gravitational environment and an initial energy source is needed and this is something that does not vary over long periods of time So the gas depression pump in its fourth application gives us an available energy that does not depend on the vagaries of nature and that we can scale to deliver the power we need in a clean way, for long periods of time and

reusing only a small part of its produced energy.

On the inventive activity that exists in the gas depression pump and its operating procedures in its applications as an energy generator, it should only be said that in the educational systems and in the existing bibliography, the energy is very clear. neither created nor se

it destroys, it is only transformed and on the energy of the true gravity of the buoyancy thrust and of the hydrostatic pressure, it is repeated again and again that the sum of potential energy due to the height and kinetic energy due to the velocity describes the total energy of a system where energy is gravity; and that to obtain this potential energy, work of the same amount or higher must be carried out if we take into account the performance of the machines. From now on they can teach that this cycle must be added the energy part of the inventive capacity of the gas depression pump and its use procedures in its two applications as an energy generator. And you can say that the energy continues to transform only to achieve a potential gravitational flotation energy, thanks to the inventive capacity of the gaseous depression pump and its use procedures, it is no longer necessary to spend a job greater than or equal to the that the potential energy generated when released due to the inventive activity that there is the gas depression pump and its operating procedures. If one of the major problems facing humanity today is climate change and it is not confronted with more force, it is basically because all environmentally responsible technologies, known as renewable energies are not available energies, that is, these technologies They always need another contaminant backup technology because the existence of wind, sun and rain is variable over time, so electrical systems based 100% on these technologies are unviable. If we based the electricity supply on solar energy at night we would run out of supply. Wind turbine technology is highly variable, it would be as if today we based the transport of the merchant marine on sailing, the goods could arrive or not, depending on the weather conditions. On the hydraulic energy this is a true clean basic energy, but the rivers have flow limits, so the power of the hydroelectric plants is conditioned to the place where it is installed, you can not put a dam anywhere, so they make it inferior technology that depends on the natural conditions and not on the

needs of humanity. On the other hand, polluting technologies have the disadvantage that they are based on finite resources subject to the demands of the

availability, so its price increases or decreases throughout. time, necessitating a greater supply of funds and higher energy prices in addition to causing significant environmental damage. On the inventive activity in the invention of the gas depression pump and its operating procedures in its simple and complex pumping applications, it can only be said that if it were so obvious to invent a system that would improve both the pumping performance and not current low performance systems would continue to be used and offered for clear economic, environmental and engineering pride reasons.

That no one has given this solution until the presentation of this patent and the fact that this machine has such benefits for humanity, has a clear consequence, the fact that in the invention of the gas depression pump and procedures for using the There is inventive activity itself. All irrefutable.

Explanation of the figures:

Figure 1: Plant from above the floating platform of the gas depression pump and operating procedures the same, it can be seen the mechanical transmission system by chains, pulleys, axles, pulleys with ratchet gear and coupling to take advantage of the force generated by the hydropneumatic generator with heat exchanger

gas depression

Figure 2: cut of the elevation of the floating platform of the gas depression pump and its operating procedures, it can be seen the mechanical chain transmission system, the mobile tanks, the liquid-gas intermediate chamber, the weight tensioner, and part of the pulley system. The drawing is not scaled, it is a drawing

sketched, the upward movement of the mobile deposits could reach a few hundred meters

depending on the material

Figure 3 and 4: Cut the pulleys with coupling for ratchet 33 and 34 where you can see the shaft, the pulleys

Bearings of these that are coupled on the shaft, the ratchet system with the hinges or hinges of the keys. Operation is simple if the shaft rotates clockwise, the pulley 33 is disengaged and the pulley 34 is engaged. If the shaft rotates counterclockwise the pulley 34 is disengaged and the 33 is engaged. If the shaft stops, both pulleys 33 and 34 remain disconnected and at rest, either moving until their kinetic energy decreases from

rotation or stops until they are moved again by the axis.

Figure 5: plan and elevation of the cut of the mobile tank (1), where you can see the different inlet and outlet pipes, as well as the connection valve with the surrounding external liquid.

Figure 6: plan and elevation of the cut of the mobile tank (2), where you can see the different inlet and outlet pipes, as well as the connection valve with the surrounding external liquid.

Figure 7: elevation of the intermediate liquid-gas chamber, where the valve system is appreciated, the liquid injection system which works by variation of gaseous pressure, the mobile tanks, the transmission chain and the tensioning weight. Figure 8: elevation and semi-cut of the intermediate chamber

liquid-gas and elevation of the gas depression exchanger, where the example of arrangement of the valves can be seen in greater detail. Figure 9: elevation to a larger scale of the Gas Depression Exchanger.

Figure 10: elevation showing the gas depression exchanger, the liquid outlet valve and the compressor.

Figure 11: Profile of the gas depression exchanger. Figure 12: fan. Figure 13: a gaseous depression pump immersed in liquid with depth. The pump is connected to a reservoir or reservoir on the surface and in height that has permanent hydrostatic pressure and is connected to the supply. This hydrostatic pressure allows the pump to be stopped for maintenance and to continue supplying without having auxiliary pumps.

Figure 14: a gaseous depression pump immersed in liquid with depth. The pump is connected to a reservoir or reservoir on the surface and at height that has permanent hydrostatic pressure and is connected to a hydraulic turbine for power generation. The fact is that less energy is needed to raise the liquid to the height of the tank with the gaseous depression pump than the energy that this liquid can return by means of a turbine

hydraulics. The system could be connected directly to the turbine without tank or reservoir in height, but this gives it more stability of delivery. The gas depression pump and its operating procedures comprise the following components according to figures 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13 and 14. Mobile tanks ( 1 and 2); a liquid-gas intermediate chamber (3); a gas depression exchanger (4); liquid injection valves to the exchanger (5) through which the external liquid surrounding the gas depression exchanger passes once it is opened because the gas has the proper speed produced by the fan; pressurized gas injection valve (6) through which the pressurized gas is introduced during the start-up cycle in the gas-liquid exchanger; a pressurized liquid outlet valve or liquid injection valve to the intermediate chamber (7) through which the pressurized liquid exits; pressure detector or pressure switch (8); low liquid level detector (9);

high level liquid detector (10); bearings with bearing (11) that allow different machine elements to rotate; a compressor (12) that allows the pressurized air to be generated in the first cycle or start cycle; rotation axes (13); a connection valve between the compressor and the intermediate liquid-gas chamber (14) that allows the air to pass into the first cycle and then keep the compressor isolated; a connection valve between the intermediate liquid-gas chamber and the atmosphere (15); a connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16); a valve

connection between the second mobile tank and the upper part of the intermediate liquid-gas tank (17); a fan (18) that gives the gas the necessary speed; fan blades (19); a connection valve between the lower part of the first mobile tank and the lower part of the intermediate liquid-gas tank (20); a connection valve between the lower part of the second mobile tank and the lower part of the intermediate liquid-gas tank (21); a connection valve between the first mobile tank and the external liquid (22); a connection valve between the second mobile tank and the external liquid (23); a transmission chain (24); a tensioning weight (25) the weight constituted by a pulley system allows the movement of the chain; a nozzle (26) that increases the gas velocity when it is in motion and decreases its pressure; a diffuser (27) that decreases the gas velocity when it is in motion and increases its pressure; curved pipe outlet (28) that prevents gas from entering the intermediate chamber to the gas depression exchanger when the flow valve is opened; gas depression exchanger brackets (29) used to hold the exchanger; rotation axis of the fan (30) where the fan blades are coupled; flexible gas pipes (31); coupling for use of force generated by the hydropneumatic generator with

mechanical exchanger and its use procedure

(32); can be coupled pulleys for ratchet (33) and (34) that are coupled to the shaft depending on the direction of rotation of this; transmission pulleys permanently attached to the shaft (35) through which the transmission chain passes; transmission belts (36); a floating or sustained platform on the ground (37); flexible pipes for liquid (38); rigid air pipes (39); rigid water pipes (40); transmission chain brake (41); supports (42); pressurized liquid outlet pipe (43) through which the liquid exits once pressurized in the gas depression pump; reservoir or reservoir in height (44); consumer supply network (45); hydraulic turbine (46);

outlet valve of the reservoir or reservoir in height (47);

narrow conduction of the gas depression exchanger (48); wide conduction of the gas depression exchanger (49); an anemometer (50) that marks the speed of the pressurized gas moved by the fan; pipe of

turbine supply (51); unusual liquid discharge valve (52). After talking about the elements that comprise the gas depression pump and its operating procedures, I must now talk about some characteristics that comprise these elements of the gas depression pump and

procedures for using it in your application of

Hydropneumatic generator for the correct operation of the same and totally necessary, so that it is interpreted correctly by an expert; To begin with in the case of the intermediate liquid-gas chamber it is obvious that if we use the property that the less dense fluids float over the denser ones, for the transfer of liquid-gas the different mobile tanks, the pipes and the intermediate chambers have a dimension interval where the machine works. The mobile tanks (1) and (2) must be below the folds of the flexible air pipes (31), the flexible air pipes (31} and the flexible water pipes (38) at their lowest point must be below the rigid air pipes (39) and rigid water pipes (40) The mobile tanks (1) and (2) as well as the flexible pipes (38) and (31) must be below of the intermediate liquid-gas chamber (3) It is preferable in case some fluid enters mixed in the wrong or rigid rigid flexible pipe that these always have a certain inclination and that are never completely horizontal; in the case of flexible pipes, it is it is preferable that the closest parts of the pipes to the rigid pipes should be at a higher level than the furthest parts of these flexible pipes with respect to the connection with the rigid pipes.For the correct operation of the hydropneumatic generator with exchange It is also necessary that the intermediate chamber (3) as well as the liquid injection valves to the exchanger (5) be submerged underwater. On the other hand to avoid losing energy during the

Gas liquid exchange is recommended to put in each machine several pairs of mobile tanks (1) and (2) with its transmission chain (24) and the entire pulley system with coupling for ratchet (33) and (34) each with a transmission chain brake (41) causing them to give stability to the power delivery and thus allow the gas liquid exchange in each pair of tanks (1) and (2) with them stopped, thus avoiding the loss of energy in this process, since if we take into account the viscosity of the fluids and the tendency to cling to the pipes we will know that it takes a while to make the exchange, and if there is no brake, the progress of the mobile tanks begins without being completely filled with air , so the maximum power of the machine without a brake (41) and several pairs of tanks (1) and (2).

The elements with some characteristics already mentioned of the gaseous depression pump and its operating procedures collaborate with each other as follows.

The first operating procedure of the gas depression pump is characterized in that, starting from a situation prior to the start of the usual cycle where all the valves are closed and the gas depression exchanger (4) is filled with gas at atmospheric pressure and covered by out of liquid with certain hydrostatic pressure, so that at least the liquid injection valves to the exchanger (5) are covered.

The previous preparations for the operation of the machine begin. The compressor (12) is started and the pressurized gas injection valve (6) is opened, thus filling the gas depression exchanger (4) of pressurized gas. When the pressure switch (8) marks the required working pressure, the compressor (12) is stopped and the pressurized gas injection valve (6) is closed. Now we have the gas depression exchanger (4) filled with pressurized gas.

Once these initial operations have been carried out, we can start the operating cycle of the gas depression pump.

The fan (18) which, located in the wide conduit of the gas depression exchanger (49), starts to move the pressurized gas and starts it at the proper working speed, marked by it. anemometer (50).

The pressurized gas has a velocity and a pressure in the wide conduit of the gas depression exchanger (49), when the pressurized gas enters the nozzle (26) the pressurized gas pressure, its velocity and its density vary. The pressure and density of the pressurized gas that is moving through the narrow conduction of the gas depression exchanger (48) is lowered, which makes the external hydrostatic pressure of the liquid greater than that of the pressurized gas that is passing through the narrow conduction of the gas depression exchanger (48).

For these facts, once the adequate speed of the pressurized gas, marked by the anemometer (50), the liquid injection valves to the exchanger (5) are opened. The higher liquid pressure causes it to enter the gas depression exchanger (4).

When the pressurized gas mixed with the liquid passes through the diffuser (27), the gas decreases its velocity and increases its pressure causing the liquid to precipitate in the lower part of the wide conduit of the gas depression exchanger (49). The pressure of the pressurized gas in motion during its passage through the wide conduction of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the gas depression exchanger (4). When the liquid reaches the high liquid level detector (10) the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out until the level of this in the gas depression exchanger (4) exceeds the detector Low level of liquid (9). At that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again.

This is the first gaseous depression pump operation procedure in which it has simple pumping application.

The second operation procedure of the pump

Gas depression is characterized by starting from a situation prior to the start of the usual cycle where all the valves are closed and the gas depression exchanger (4) is filled with gas at atmospheric pressure and covered by outside liquid with certain pressure

hydrostatic, so that at least the liquid injection valves to the exchanger (5) are covered.

The previous preparations for the operation of the machine begin. The compressor (12) is started and the pressurized gas injection valve (6) is opened, thus filling the gas depression exchanger (4) of pressurized gas. When the pressure switch (8) marks the required working pressure, the compressor (12) is stopped and the pressurized gas injection valve (6) is closed. Now we have the gas depression exchanger (4) filled with pressurized gas. Once these initial operations have been carried out, we can start the operating cycle of the gas depression pump.

The fan (18) which, located in the wide line of the gas depression exchanger (49), starts to move the pressurized gas and starts it at the proper working speed, marked by the anemometer (50).

The pressurized gas has a speed and pressure in the wide conduit of the gas depression exchanger

(49) _/ when the pressurized gas enters the nozzle (26) the pressure of the pressurized gas, its velocity and its density vary.

The pressure and density of the pressurized gas that is moving through the narrow conduction of the gas depression exchanger (48) is lowered, which makes the external hydrostatic pressure of the liquid greater than that of the pressurized gas that is passing through the narrow conduction of the gas depression exchanger (48).

When the pressurized gas mixed with the liquid passes through the diffuser (27), the gas decreases its velocity and increases its pressure causing the liquid to precipitate in the lower part of the wide conduit of the gas depression exchanger (49).

The pressure of the pressurized gas in motion during its passage through the wide conduction of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the gas depression exchanger (4). When the liquid reaches the high liquid level detector (10), the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out through the pressurized liquid outlet pipe (43) to fill the tank or reservoir in height (44). The pressurized liquid outlet valve (7) remains open until the level of the pressurized liquid in the gas depression exchanger (4) exceeds the low liquid level detector (9). At that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again. This process can continue until we have the deposit or reservoir in height (44) full. Once the liquid is in the tank at height it will maintain a stable pressure in the supply network to consumers (45), giving a margin of time to the possible maintenance needs of the gas depression pump. The delivery of pressurized liquid can be adjusted to the demand by increasing or decreasing the fan speed (18), but it is simpler and avoids many problems having a reservoir or reservoir in height (44).

The third operating procedure of the gas depression pump is characterized by starting from a situation prior to the start of the usual cycle where all the valves are closed and the gas depression exchanger (4) is filled with gas at atmospheric pressure and covered on the outside of liquid with a certain hydrostatic pressure, so that at least the liquid injection valves to the exchanger (5) are covered.

The previous preparations for the operation of the machine begin. The compressor (12) is started and the pressurized gas injection valve (6) is opened, thus leaving

filling the gas depression exchanger (4) with pressurized gas. When the pressure switch (8) marks the required working pressure, the compressor (12) is stopped and the pressurized gas injection valve (6) is closed. Now we have the gas depression exchanger (4) filled with pressurized gas.

Once these initial operations have been carried out, we can start the operating cycle of the gas depression pump. The fan (18) which, located in the wide line of the gas depression exchanger (49), starts to move the pressurized gas and starts it at the proper working speed, marked by the anemometer (50). The pressurized gas has a velocity and a pressure in the wide conduit of the gas depression exchanger (49), when the pressurized gas enters the nozzle (26) the pressurized gas pressure, its velocity and its density vary. The pressure and density of the pressurized gas that is moving through the narrow conduction of the gas depression exchanger (48) lower, which makes the external hydrostatic pressure of the liquid greater than that of the gas pressurized which is going through the narrow conduction of the gas depression exchanger (48).

For these facts, once the adequate speed of the pressurized gas, marked by the anemometer (50), the liquid injection valves to the exchanger (5) are opened.

The higher liquid pressure causes it to enter the gas depression exchanger (4). When the pressurized gas mixed with the liquid passes through the diffuser (27), the gas decreases its speed and increases its pressure causing the liquid to precipitate in the lower part of the wide conduit of the gas depression exchanger (49).

The pressure of the pressurized gas in motion during its passage through the wide conduction of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the gas depression exchanger (4). When the liquid reaches the high liquid level detector (10), the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out through the pressurized liquid outlet pipe (43) to fill the tank or reservoir in height (44). The pressurized liquid outlet valve (7) remains open until the level of the pressurized liquid in the gas depression exchanger (4) exceeds the low liquid level detector (9). At that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again. This process can continue until we have the reservoir or reservoir in height (44) full. Once the liquid is in the tank at height, it will maintain a stable pressure in the turbine supply pipe (51), giving a margin of time to the possible maintenance needs of the gas depression pump. By opening the outlet valve of the reservoir or reservoir at height (47), the supply of pressurized liquid to the hydraulic turbine (46) is initiated, making the mechanical power of this can be used to generate electricity or other purposes. For the generation of excess energy, the gas depression pump will need to reuse a small part of the energy generated by moving the hydraulic turbine (46) to continue moving the fan (18) and the valve assembly of the gas depression pump.

The highly superior performance of the gas depression exchanger (4) results in the energy needed to raise the liquid to the reservoir or reservoir in height (47) with the gaseous depression pump is less than the potential energy of the liquid at that height.

With what once a small part of the energy for the operation of the gaseous depression pump is reused, the excess energy generated by the turbine

Hydraulics (46) can be used for other purposes.

The fourth operating procedure of the gas depression pump is characterized in that, starting from a situation prior to the start of the usual cycle where all the valves are closed, the mobile tank (2) is filled with pressurized gas previously introduced, the mobile tank ( 1) and the intermediate liquid-gas chamber (3) are filled with liquid and the gas depression exchanger (4) is filled with gas at atmospheric pressure and covered outside of liquid with certain hydrostatic pressure, so that at least the liquid injection valves to the exchanger (5) are covered. The mobile tank (1) is in the depths and the mobile tank (2) is at the high point of the route. The transmission chain brake (41) is braked.

The previous preparations for the operation of the machine begin. The compressor (12) is started and the pressurized gas injection valve (6) and the connection valve between the compressor and the liquid-gas intermediate chamber (14) are opened, in addition to opening the unusual liquid discharge valve (52).

With these actions the liquid-gas intermediate chamber (3) is emptied of liquid, when this occurs we close the unusual liquid discharge valve (52) and the connection valve between the compressor and the liquid-gas intermediate chamber (14) , the compressor (12) continues to work so that after a while we will reach the situation of having the

gas depression exchanger (4) filled with gas at the working pressure for which it is designed, which will always be somewhat higher than that of the intermediate liquid-gas chamber.

At this point the compressor (12) is stopped and the pressurized gas injection valve (6) is closed. From now on the normal operation of the gas depression pump in its generator application

Simplified hydropneumatic with only one pair of mobile tanks (1) and (2) repeats the same 4 phases over time, for normal operation of the depression pump Soda and operating procedures of the same in its application of hydropneumatic generator.

In phase Ά the mobile tank (1) is filled with gas and the mobile tank (2) with liquid -

In phase B the transmission chain brake (41) is released and the ascent takes place through the liquid of the mobile tank (1) and the descent through the liquid of the mobile tank (2).

In phase C the mobile tank (2) is filled with gas and the mobile tank (1) is filled with water.

In phase D the transmission chain brake (41) is released and the ascent takes place through the mobile deposit liquid (2) and the descent through the mobile deposit liquid (1).

Phase A, the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16) and the connection valve between the first mobile tank and the external liquid (22) are opened, the fan is started ( 18) that located in the wide conduit of the gas depression exchanger (49) begins to move the pressurized gas and takes it to the proper speed of

work, marked by the anemometer (50).

Once this speed is reached, the liquid injection valves to the exchanger (5) are opened.

The higher liquid pressure causes it to enter the gas depression exchanger (4).

The liquid begins to precipitate in the lower part of the wide conduit of the gas depression exchanger (49).

When the liquid reaches the high liquid level detector (10) the liquid injection valve is opened to the intermediate chamber (7), the pressurized liquid goes out through the pressurized liquid outlet pipe (43) falling inside of the intermediate liquid-gas chamber (3) and displacing the pressurized gas from it that begins to empty the mobile tank (1).

Once the mobile tank (1) is full of gas

Pressurized, the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16) is closed, the connection valve between the First mobile tank and the external liquid [22), the liquid injection valves to the exchanger (5) and also the fan (18) is stopped.

The connection valve is opened between the lower part of the second mobile tank and the lower part of the tank

intermediate liquid-gas (21) and the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17). The liquid contained in the intermediate liquid-gas chamber (3) flows to the mobile tank (2) and the pressurized gas contained therein flows into the intermediate liquid-gas chamber (3). Once the mobile tank (2) is filled with liquid, the connection valve between the lower part of the second mobile tank and the lower part of the intermediate liquid-gas tank (21) are closed and the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17).

Phase B, the mobile deposit (1) is in the

depths and full of pressurized gas, the mobile tank (2) is close to the surface and filled with liquid. The transmission chain brake (41) that braked the transmission chain (24) is released, so that the mobile tank (1) filled with pressurized gas begins to float towards the

surface, and the mobile tank (2) filled with liquid begins to sink.

This causes the drive chain (24) to move, which moves the drive pulleys permanently attached to the shaft (35), and the pulley with ratchet coupling (34) being engaged by moving the rotation shafts (13) and giving a usable movement in the coupling for harnessing force generated by the hydropneumatic generator with

mechanical exchanger and its use procedure (32).

Once the mobile tank (1) arrives and the mobile tank (2) below, the transmission chain (24) is braked with the transmission chain brake (41).

We have the mobile tank (2) full of liquid and the mobile tank (1) full of gas under pressure, as well as the chamber

intermediate liquid-gas (3) filled with gas under pressure.

Phase C, the connection valve between the second mobile tank and the upper part of the intermediate tank is opened liquid-gas (17) and the connection valve between the second mobile tank and the external liquid (23), the fan (18) that located in the wide conduction of the gas depression exchanger (49) starts to move the gas pressurized and takes it at the proper speed of

work, marked by the anemometer (50).

Once this speed is reached, the liquid injection valves are opened to the exchanger (5). The higher liquid pressure causes it to enter the gas depression exchanger (4).

When the liquid reaches the high liquid level detector (10) the liquid injection valve is opened to the intermediate chamber (7), the pressurized liquid goes out through the pressurized liquid outlet pipe (43) falling inside of the intermediate liquid-gas chamber (3) and displacing the pressurized gas from it that begins to empty the mobile tank (2). Once the mobile tank (2) is full of gas

Pressurized, the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17), the connection valve between the second mobile tank and the external liquid (23), are closed.

Liquid injection valves to the exchanger (5) and the fan (18) is also stopped.

The connection valve between the lower part of the first mobile tank and the lower part of the intermediate liquid-gas tank (20) is opened and the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16) .

The liquid contained in the intermediate liquid-gas chamber (3) flows into the mobile tank (1) and the pressurized gas contained therein flows into the intermediate liquid-gas chamber (3).

Once the mobile tank (1) is filled with liquid, the connection valve between the lower part of the first mobile tank and the lower part of the intermediate liquid-gas tank (20) are closed and the connection valve between the first mobile tank and the top of the. intermediate liquid-gas tank (16). Phase D, the mobile deposit (2) is in the

depths and full of pressurized gas, the mobile tank

(1) It is close to the surface and full of liquid.

The transmission chain brake (41) that braked the transmission chain (24) is released, thereby moving the mobile tank

(2) full of gas under pressure begins to float towards the

surface, and the mobile tank (1) filled with liquid begins to sink. This causes the drive chain (24) to move, to move the drive pulleys permanently attached to the shaft (35), and the pulley with ratchet coupling (33) to move the rotation shafts (13) and giving a usable movement in the coupling for harnessing force generated by the hydropneumatic generator with

mechanical exchanger and its use procedure (32).

Once the mobile tank (2) arrives and the mobile tank (1) below, the transmission chain (24) is braked with the transmission chain brake (41).

Claims

CLAIMS:

1-Gas depression pump characterized in that it comprises: a gas depression exchanger (4); liquid injection valves to the exchanger (5) through which the external liquid surrounding the gas depression exchanger passes once it is opened because the gas reached the operating speed range produced by the fan; pressurized gas injection valve (6) through which the pressurized gas is introduced during the cycle of

start-up in the gas-liquid exchanger; a pressurized liquid outlet valve or liquid injection valve to the intermediate chamber (7) through which the pressurized liquid exits; pressure detector or pressure switch (8); low level liquid detector (9); high level liquid detector (10); a compressor (12) that allows the pressurized air to be generated in the first cycle or start cycle; a fan (18) that moves the gas to the operating speed range; fan blades (19); a nozzle (26) that increases the gas velocity when it is in motion and decreases its pressure; a diffuser (27) that decreases the gas velocity when it is in motion and increases its pressure; curved pipe outlet (28) that prevents the entry of gas from the intermediate chamber to the

gas depression exchanger when the stop valve is opened; gas depression exchanger brackets

(29) that serve to hold the exchanger; axis of rotation of the fan (30) where the blades of the

fan; pressurized liquid outlet pipe (43) through which the liquid exits once pressurized in the gas depression pump; narrow conduction of the gas depression exchanger (48); wide conduction of the gas depression exchanger (49); an anemometer (50) that marks the speed of the pressurized gas moved by the fan. 2-Operating procedure of the gas depression pump contained in claim 1 characterized in that

starting from a situation prior to the beginning of the cycle

usual where all the valves are closed and the gas depression exchanger (4) is filled with gas at atmospheric pressure and covered by outside liquid with some hydrostatic pressure, so that at least the liquid injection valves are covered at

exchanger (5). The previous preparations for the operation of the machine begin. The compressor (12) is started and the pressurized gas injection valve (6) is opened, thus leaving

filling the gas depression exchanger (4) with pressurized gas. When the pressure switch (8) marks the pressure of work required, the compressor (12) is stopped and the pressurized gas injection valve (6) is closed. Now we have the gas depression exchanger (4) filled with pressurized gas. 3-Operating procedure of the gas depression pump contained in claim 2 characterized in that once the previous initial operations have been carried out, the operating cycle of the gas depression pump begins. The fan (18) which, located in the wide conduit of the gas depression exchanger (49), starts to move the pressurized gas and takes it to the operating speed range / marked by the anemometer (50). The pressurized gas has a velocity and a pressure in the wide conduit of the gas depression exchanger (49), when the pressurized gas enters the nozzle (26) the pressurized gas pressure, its velocity and its density vary. The pressure and density of the pressurized gas that is moving through the narrow conduction of the gas depression exchanger (48) is lowered, which makes the external hydrostatic pressure of the liquid greater than that of the pressurized gas that is passing through the narrow conduction of the gas depression exchanger (48).

For these facts, once the operating speed range of the pressurized gas, marked by the anemometer (50), the liquid injection valves to the exchanger (5) are opened.

The higher liquid pressure causes it to enter the gas depression exchanger (4). When the pressurized gas mixed with the liquid passes through the diffuser (27), the gas decreases its velocity and increases its pressure causing the liquid to precipitate in the lower part of the wide conduit of the gas depression exchanger (49).

The pressure of the pressurized gas in motion during its passage through the wide conduction of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the gas depression exchanger (4). When the liquid reaches the high liquid level detector (10) the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out until the level of this in the gas depression exchanger (4) exceeds the detector Low level of liquid (9). In that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again.

4-Gas depression pump characterized in that it comprises: a gas depression exchanger (4); liquid injection valves to the exchanger (5) through which the surrounding external liquid passes to the gas depression exchanger once it is opened because the gas reached the operating speed range produced by the fan; pressurized gas injection valve (6) through which the pressurized gas is introduced during the cycle of

start-up in the gas-liquid exchanger; a pressurized liquid outlet valve or liquid injection valve to the intermediate chamber (7) through which the pressurized liquid exits; pressure detector or pressure switch (8); low liquid level detector (9); high level liquid detector (10); a compressor (12) that allows the pressurized air to be generated in the first cycle or start cycle; a fan (18) that moves the gas to the operating speed range; fan blades (19); a nozzle (26) that increases the gas velocity when it is in motion and decreases its pressure; a diffuser (27) that decreases the gas velocity when it is in motion and increases its pressure; curved pipe outlet (28) that prevents the entry of gas from the intermediate chamber to the

gas depression exchanger when the stop valve is opened; gas depression exchanger brackets (29) used to hold the exchanger; axis of rotation of the fan (30) where the blades of the

fan; pressurized liquid outlet pipe (43) through which the liquid exits once pressurized in the gaseous depression pump; reservoir or reservoir in height (44); consumer supply network (45); narrow conduction of the gas depression exchanger (48); wide conduction of the gas depression exchanger (49); an anemometer (50) that marks the speed of the pressurized gas moved by the fan.

5-Operating procedure of the gas depression pump contained in claim 4 characterized in that

starting from a situation prior to the beginning of the cycle

6-Procedure for the operation of the gas depression pump contained in claim 5, characterized in that once the initial operations have been carried out we can start the operating cycle of the gas depression pump. The fan (18) which, located in the wide line of the gas depression exchanger (49), starts to move the pressurized gas and takes it to the operating speed range, marked by the anemometer (50).

The higher liquid pressure causes it to enter the gas depression exchanger (4).

The pressure of the pressurized gas in motion during its passage through the wide conduit of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the depression exchanger soda (4). When the liquid reaches the high liquid level detector (10), the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out through the pressurized liquid outlet pipe (43) to fill the tank or reservoir in height (44). The pressurized liquid outlet valve (7) remains open until the level of pressurized liquid in the gas depression exchanger (4) exceeds the low liquid level detector (9). At that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again. This process can continue until we have the reservoir or reservoir in height (44) full. Once the liquid is in the tank, it will maintain a stable pressure in the supply network to consumers (45). The delivery of pressurized liquid can be adjusted to the demand by increasing or decreasing the fan speed (18), but it can also be done by having a reservoir or reservoir in height (44). 7-Gas depression pump characterized in that it comprises: an exchange of gas depression (4); liquid injection valves to the exchanger (5) through which the external liquid surrounding the gas depression exchanger passes once it is opened because the gas reached the operating speed range produced by the fan; pressurized gas injection valve (6) through which the pressurized gas is introduced during the cycle of

start-up in the gas-liquid exchanger; a pressurized liquid outlet valve or liquid injection valve to the intermediate chamber (7) through which the pressurized liquid exits; pressure detector or pressure switch (8); low level liquid detector (9); high level liquid detector (10); a compressor (12) that allows the pressurized air to be generated in the first cycle or start cycle; a fan (18) that moves the gas to the operating speed range; fan blades (19); a nozzle (26) that increases the gas velocity when it is in motion and decreases its pressure; a diffuser (27) that decreases the speed of the. gas when it is moving and its pressure increases; curved pipe outlet (28) that prevents the entry of gas from the intermediate chamber to the

gas depression exchanger when the stop valve is opened; supports of the gas depression exchanger (29) used to support the exchanger; axis of rotation of the fan (30) where the blades of the

fan; pressurized liquid outlet pipe (43) through which the liquid exits once pressurized in the gas depression pump; reservoir or reservoir in height (44); consumer supply network (45); hydraulic turbine (46); outlet valve of the reservoir or reservoir in height (47);

narrow conduction of the gas depression exchanger

(48); wide conduction of the gas depression exchanger (49); an anemometer (50) that marks the speed of the pressurized gas moved by the fan; pipe of

turbine supply (51).

a-Operating procedure of the gas depression pump contained in claim 7 characterized in that

starting from a situation prior to the beginning of the cycle

usual where all the valves are closed and the

gas depression exchanger (4) is filled with gas at atmospheric pressure and covered by outside liquid with some hydrostatic pressure, so that at least the liquid injection valves are covered at

exchanger (5).

9-Operating procedure of the gas depression pump contained in claim 8 characterized in that once the initial operations have been carried out, we can start the operating cycle of the gas depression pump.

The fan (18) which, located in the wide conduit of the gas depression exchanger (49), starts to move the pressurized gas and takes it to the operating speed, marked by the anemometer (50).

(49), when the pressurized gas enters the nozzle (26) the pressure of the pressurized gas, its velocity and its density vary.

The pressure and density of the pressurized gas that is moving through the narrow conduction of the gas depression exchanger (48) lower, which makes the external hydrostatic pressure of the liquid greater than that of the pressurized gas that is passing through the narrow conduction of the gas depression exchanger (48). For these facts, once the operating speed interval of the pressurized qas, marked by the anemometer (50), the liquid injection valves to the exchanger (5) are opened. The higher liquid pressure causes it to enter the

gas exchange exchanger (4).

When the pressurized gas mixed with the liquid passes through the diffuser (27), the gas decreases its speed and increases its pressure causing the liquid to precipitate in the lower part of the wide conduit of the gas depression exchanger (49).

The pressure of the pressurized gas in motion during its passage through the wide conduction of the gas depression exchanger (49) pressurizes the liquid that enters from outside and accumulates in the lower part of the gas depression exchanger (4). When the liquid reaches the. high liquid level detector (10) the pressurized liquid outlet valve (7) is opened, the pressurized liquid goes out through the pressurized liquid outlet pipe (43) to fill the reservoir or reservoir in height ( 44). The pressurized liquid outlet valve (7) remains open until the level of the pressurized liquid in the gas depression exchanger (4) exceeds the low liquid level detector (9). At that moment the pressurized liquid outlet valve (7) is closed until the liquid reaches the high liquid level detector (10) again. This process can continue until we have the reservoir or reservoir in height (44) full. Once the liquid is in the tank at height it will maintain a stable pressure in the turbine supply pipe (51). By opening the outlet valve of the reservoir or reservoir at height (47), the supply of pressurized liquid to the hydraulic turbine (46) is initiated, making the mechanical power of this can be used to generate electricity or other purposes. For the generation of excess energy, the gas depression pump will need to reuse a small part of the energy generated by moving the hydraulic turbine (46) to continue moving the fan (18) and the valve assembly of the gas depression pump.

The highly superior performance of the gas depression exchanger (4) results in the energy required to raise the liquid to the reservoir or reservoir in height (47) with the gas depression pump being less than the potential energy of the liquid at that height . With what once a small part of the energy for the operation of the gaseous depression pump is reused, the excess energy generated by the turbine

Hydraulics (46) can be used for other purposes.

10-Gas depression pump characterized in that it comprises: Mobile deposits (1) and (2); a liquid-gas intermediate chamber (3); a gas depression exchanger (4); liquid injection valves to the exchanger (5) through which the external liquid surrounding the gas depression exchanger passes once it is opened because the gas reached the operating speed range produced by the fan; pressurized gas injection valve (6) through which the pressurized gas is introduced during the start-up cycle in the gas-liquid exchanger; a pressurized liquid outlet valve or liquid injection valve to the intermediate chamber (7) through which the pressurized liquid exits; pressure detector or pressure switch (8); low level liquid detector (9); high level liquid detector (10); bearings with bearing (11) that allow different machine elements to rotate; a compressor (12) that allows the pressurized air to be generated in the first cycle or start cycle; rotation axes (13); a connection valve between the compressor and the intermediate liquid-gas chamber (14) that allows the air to pass in the first cycle and then keep the compressor isolated; a connection valve between the liquid-gas intermediate chamber and the

atmosphere (15); a connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16); a connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17); a fan (18) that moves the gas to the operating speed range; fan blades (19); a connection valve between the lower part of the first mobile tank and the lower part of the intermediate liquid-gas tank (20); a connection valve between the lower part of the second mobile tank and the lower part of the intermediate liquid-gas tank (21); a connection valve between the first mobile tank and the external liquid (22); a connection valve between the second mobile tank and the external liquid (23); a transmission chain (24); a tensioning weight (25) the weight constituted by a pulley system allows the movement of the chain; a nozzle (26) that increases the gas velocity when it is in motion and decreases its pressure; a diffuser (27) that decreases the gas velocity when it is in motion and increases its pressure; curved pipe outlet (28) that prevents the entry of gas from the intermediate chamber to the gas depression exchanger when the flow valve is opened; gas depression exchanger brackets (29) used to hold the exchanger; rotation axis of the fan (30) where the fan blades are coupled; flexible gas pipes (31); coupling for use of force generated by the hydropneumatic generator with

mechanical exchanger and method of use thereof (32); pulleys with coupling for ratchet (33) and (34) that are coupled to the shaft depending on the direction of rotation of this; transmission pulleys permanently attached to the shaft (35) through which the transmission chain passes; transmission belts (36); a floating or sustained platform on the ground (37); flexible pipes for liquid (38); rigid air pipes (39); rigid water pipes (40); transmission chain brake (41); supports (42); pressurized liquid outlet pipe (43) through which the liquid exits once pressurized in the gas depression pump; reservoir or reservoir in height (44); consumer supply network (45); hydraulic turbine (46);

outlet valve reservoir or reservoir in height (47);

turbine supply (51); unusual liquid discharge valve (52).

11-Operating procedure of the gas depression pump contained in claim 10 characterized in that, starting from a situation prior to the start of the usual cycle where all the valves are closed, the mobile tank (2) is filled with pressurized gas introduced

previously, the mobile tank (1) and the intermediate liquid-gas chamber (3) are filled with liquid and the

exchanger (5). The mobile tank (1) is in the depths and the mobile tank (2) is at the high point of the route. The transmission chain brake (41) is braked.

The previous preparations for the operation of the machine are started. The compressor (12) is started and the pressurized gas injection valve (6) and the connection valve between the compressor and the liquid-gas intermediate chamber (14) are opened, in addition to opening the unusual liquid discharge valve (52).

With these actions, the intermediate liquid-gas chamber (3) is emptied of liquid, when this happens we close the valve Unusual liquid discharge (52) and the connection valve between the compressor and the intermediate liquid-gas chamber (14), the compressor (12) continues to work so that after a while we will reach the situation of having the

At this point the compressor (12) is stopped and the pressurized gas injection valve (6) is closed.

12-Operational procedure of the gas depression pump contained in claim 11 characterized in that the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16) and the connection valve between the first mobile tank and the external liquid (22), the fan (18) that located in the wide conduction of the gas depression exchanger (49) starts to move the pressurized gas and takes it to the operating speed range, marked marked by the anemometer (50).

Once this speed is reached, the liquid injection valves to the exchanger (5) are opened. The higher liquid pressure causes it to enter the gas depression exchanger (4).

The liquid begins to precipitate in the lower part of the wide conduit of the gas depression intercarabrador (49).

Once the mobile tank (1) is full of gas

Pressurized, the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16), the connection valve between the first mobile tank and the external liquid (22), the liquid injection valves are closed to the exchanger (5) and the fan (18) is also stopped.

The connection valve is opened between the lower part of the second mobile tank and the lower part of the tank liquid-gas intermediate (21) and the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17).

The liquid contained in the intermediate liquid-gas chamber (3) flows into the mobile tank (2) and the pressurized gas contained therein flows into the intermediate liquid-gas chamber (3).

Once the mobile tank (2) is filled with liquid, the connection valve between the lower part of the second mobile tank and the lower part of the intermediate liquid-gas tank (21) are closed and the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17). 13-Operating procedure of the gas depression pump contained in claim 12 characterized in that the mobile tank (1) is located in the

depths and full of pressurized gas, the mobile tank (2) is close to the surface and filled with liquid.

The transmission chain brake (41) that braked the transmission chain (24) is released, so that the mobile tank (1) filled with pressurized gas begins to float towards the

surface, and the mobile tank (2) filled with liquid begins to sink.

mechanical exchanger and its use procedure (32).

Once the mobile tank (1) arrives and the mobile tank (2) below, the transmission chain (24) is braked with the transmission chain brake (41). We have the mobile tank (2) full of liquid and the mobile tank (1) full of gas under pressure, as well as the chamber

intermediate liquid-gas (3) filled with gas under pressure.

14-Operating procedure of the gas depression pump contained in claim 13 characterized in that the connection valve between the second mobile tank and the upper part of the intermediate liquid-gas tank (17) and the connection valve between the second are opened mobile deposit and the external liquid (23), the fan (18) that located in the wide conduit of the gas depression exchanger (49) begins to move the pressurized gas and takes it to the operating speed range, marked by the anemometer (50). Once this speed is reached, the liquid injection valves are opened to the exchanger (5).

The higher liquid pressure causes it to enter the gas depression exchanger (4).

When the liquid reaches the high liquid level detector (10) the liquid injection valve is opened to the intermediate chamber (7), the pressurized liquid goes out through the pressurized liquid outlet pipe (43) falling inside of the intermediate liquid-gas chamber (3) and displacing the pressurized gas from it that begins to empty the mobile tank (2).

Once the mobile tank (2) is full of gas

Liquid injection valves to the exchanger (5) and the fan (18) is also stopped.

Once the mobile tank (1) is filled with liquid, the connection valve between the lower part of the first mobile tank and the lower part of the intermediate liquid-gas tank (20) are closed and the connection valve between the first mobile tank and the upper part of the intermediate liquid-gas tank (16).

15-Operation procedure of the gas depression pump contained in claim 14 characterized because the mobile deposit (2) is in the

depths and full of pressurized gas, the mobile tank

(1) It is close to the surface and filled with liquid.

(2) full of gas under pressure begins to float to the surface, and the mobile tank (1) filled with liquid begins to sink. This causes the drive chain (24) to move, to move the drive pulleys permanently attached to the shaft (35), and the pulley with ratchet coupling (33) to move the rotation shafts (13) and giving a usable movement in the coupling for harnessing force generated by the hydropneumatic generator with

mechanical exchanger and its use procedure (32).