WO2017068209A1 - Pompe à dépression de gaz et ses procédés de fonctionnement - Google Patents

Pompe à dépression de gaz et ses procédés de fonctionnement Download PDF

Info

Publication number
WO2017068209A1
WO2017068209A1 PCT/ES2016/000118 ES2016000118W WO2017068209A1 WO 2017068209 A1 WO2017068209 A1 WO 2017068209A1 ES 2016000118 W ES2016000118 W ES 2016000118W WO 2017068209 A1 WO2017068209 A1 WO 2017068209A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
liquid
exchanger
pressurized
depression
Prior art date
Application number
PCT/ES2016/000118
Other languages
English (en)
Spanish (es)
Inventor
Sergio SALAS LAMELAS
Original Assignee
Salas Lamelas Sergio
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from ES201500756A external-priority patent/ES2622802B1/es
Application filed by Salas Lamelas Sergio filed Critical Salas Lamelas Sergio
Publication of WO2017068209A1 publication Critical patent/WO2017068209A1/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03B—MACHINES OR ENGINES FOR LIQUIDS
    • F03B17/00—Other machines or engines
    • F03B17/02—Other machines or engines using hydrostatic thrust
    • F03B17/04—Alleged perpetua mobilia
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G7/00—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for
    • F03G7/06—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for using expansion or contraction of bodies due to heating, cooling, moistening, drying or the like
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F1/00—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
    • F04F1/18—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium being mixed with, or generated from the liquid to be pumped

Definitions

  • the gas depression pump of my invention introduces a new high performance pressure liquid delivery system with multiple applications.
  • 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.
  • the first procedure of operation of the gas depression pump is the most usual, the second procedure of
  • 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 civilization 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
  • the gas depression pump and its operating procedures have an important industrial application since it introduces a significant improvement in performance
  • Hydropneumatic generator application multiplies by more than 600 times the performance of my previous inventions. The fact that the gas depression pump and
  • 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
  • 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.
  • 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.
  • 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
  • polluting technologies have the disadvantage that they are based on finite resources subject to the demands of the
  • 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
  • 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
  • Figure 3 and 4 Cut the pulleys with coupling for ratchet 33 and 34 where you can see the shaft, the pulleys
  • 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
  • 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
  • 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);
  • (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);
  • 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 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.
  • 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.
  • 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).
  • 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).
  • 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.
  • 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
  • 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.
  • the pressure switch (8) marks the required working pressure
  • the compressor (12) is stopped and the pressurized gas injection valve (6) is closed.
  • the gas depression exchanger (4) filled with pressurized gas.
  • 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
  • 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).
  • 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 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.
  • 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 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).
  • the higher liquid pressure causes it to enter the gas depression exchanger (4).
  • 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 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.
  • the liquid 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.
  • the outlet valve of the reservoir or reservoir at height (47) 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.
  • 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.
  • 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 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).
  • 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.
  • phase ⁇ the mobile tank (1) is filled with gas and the mobile tank (2) with liquid -
  • 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).
  • phase C the mobile tank (2) is filled with gas and the mobile tank (1) is filled with water.
  • 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).
  • 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).
  • the liquid injection valve 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).
  • 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.
  • connection valve is opened between the lower part of the second mobile tank and the lower part of the tank
  • Phase B the mobile deposit (1) is in the
  • 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
  • the liquid injection valves are opened to the exchanger (5).
  • 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).
  • the liquid injection valve 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
  • 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.
  • 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).
  • the transmission chain brake (41) that braked the transmission chain (24) is released, thereby moving the mobile tank

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Jet Pumps And Other Pumps (AREA)

Abstract

L'invention concerne une pompe à dépression de gaz et ses procédés d'opération, dans lesquels est présenté le fonctionnement d'un nouveau système de pompe et quatre procédés d'opération.
PCT/ES2016/000118 2015-10-20 2016-10-19 Pompe à dépression de gaz et ses procédés de fonctionnement WO2017068209A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ES201500756A ES2622802B1 (es) 2012-11-22 2015-10-20 Bomba de depresión gaseosa y procedimientos de operación de la misma
ES201500756 2015-10-20

Publications (1)

Publication Number Publication Date
WO2017068209A1 true WO2017068209A1 (fr) 2017-04-27

Family

ID=58556758

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/ES2016/000118 WO2017068209A1 (fr) 2015-10-20 2016-10-19 Pompe à dépression de gaz et ses procédés de fonctionnement

Country Status (1)

Country Link
WO (1) WO2017068209A1 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3840216A (en) * 1972-10-26 1974-10-08 Clark & Vicario Corp Vacuum aeration of liquid waste effluent
US20060017292A1 (en) * 2004-07-21 2006-01-26 Hideo Matsubara Electric power generator equipment
US20060032374A1 (en) * 2004-08-11 2006-02-16 Vrana Julius S Hydraulic liquid pumping system
US20080264056A1 (en) * 2007-04-26 2008-10-30 Jui-Chi Tung Hydraulic buoyancey kinetic energy apparatus
US20080303282A1 (en) * 2007-06-08 2008-12-11 Ziegenfuss Mark R Water cycling system with compressor motive force and with turbine electric power generator
EP2924277A1 (fr) * 2012-11-22 2015-09-30 Soluciones Científico Técnicas, S.R.L.U. Générateur hydropneumatique d'énergie et son procédé de fonctionnement

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3840216A (en) * 1972-10-26 1974-10-08 Clark & Vicario Corp Vacuum aeration of liquid waste effluent
US20060017292A1 (en) * 2004-07-21 2006-01-26 Hideo Matsubara Electric power generator equipment
US20060032374A1 (en) * 2004-08-11 2006-02-16 Vrana Julius S Hydraulic liquid pumping system
US20080264056A1 (en) * 2007-04-26 2008-10-30 Jui-Chi Tung Hydraulic buoyancey kinetic energy apparatus
US20080303282A1 (en) * 2007-06-08 2008-12-11 Ziegenfuss Mark R Water cycling system with compressor motive force and with turbine electric power generator
EP2924277A1 (fr) * 2012-11-22 2015-09-30 Soluciones Científico Técnicas, S.R.L.U. Générateur hydropneumatique d'énergie et son procédé de fonctionnement

Similar Documents

Publication Publication Date Title
US6447243B1 (en) Buoyancy prime mover
DK3049667T3 (en) Process and system for combined pump water pressure-compressed air-energy storage with constant turbine-water pressure
US20030145589A1 (en) Fluid displacement method and apparatus
CN102884319A (zh) 水动力循环发电技术
CN103016236A (zh) 叶轮缩放式流体动力发电装置
US20110289913A1 (en) Wave energy transfer system
JP2023533746A (ja) Ｆｆｗｎクリーンエネルギー発電プラント
JP2016517923A (ja) 潜水式水力発電機装置およびかかる装置から水を排出する方法
CN103906918A (zh) 用于通过在封闭的气体/液体系统中造成压差产生驱动力的方法和装置
ES2622802B1 (es) Bomba de depresión gaseosa y procedimientos de operación de la misma
WO2017068209A1 (fr) Pompe à dépression de gaz et ses procédés de fonctionnement
US8646265B2 (en) Hydraulic power apparatus
CN105020088A (zh) 大气压力和地心引力发电装置
AU2019203242A1 (en) Harnessing wave power
WO2014035267A1 (fr) Centrale d'énergie à flottaison
US8360205B1 (en) System for rotation of a shaft using the force of gravity
JP2005023799A (ja) 沈水式発電装置
ES1301844U (es) Dispositivo de generacion de energia electrica a partir de la energia de las olas del mar
CN114251215A (zh) 基于抽水蓄能的复合发电系统
WO2010119283A2 (fr) Électro-générateur à flot entraîné par l'eau
US20190032627A1 (en) Method and Apparatuses for Generating-Green Energy Source- using the weight of Tidal Body of Water
JP2010275936A (ja) 浮力を利用した動力システム
ES2633840B1 (es) Sistema de bombeo hidráulico a alta presión sin consumo energético externo y procedimiento para la puesta en práctica del mismo
RU2790113C2 (ru) Гидросиловая установка
ES2596531B1 (es) Motor gravitatorio por presión de líquido

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16856967

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 16856967

Country of ref document: EP

Kind code of ref document: A1