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US3803847A - Energy conversion system - Google Patents

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US3803847A
US3803847A US00233460A US23346072A US3803847A US 3803847 A US3803847 A US 3803847A US 00233460 A US00233460 A US 00233460A US 23346072 A US23346072 A US 23346072A US 3803847 A US3803847 A US 3803847A
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heat
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heat exchanger
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Alister R Mc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for

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  • ABSTRACT An energy conversion system, particularly for use in heating, cooling, and generating electrical and mechanical power for an area such as a dwelling.
  • vapor is alternately directed into one of two reservoir tanks so that working fluid in that tank is forced out of that tank by the vapor pressure and through a hydraulic motor, which powers a compres- 2 "f 6-0/7211-2/467 sor and/or other devices such as an electrical power generator, garbage disposal, etc., before it returns to [5 Cl.
  • the invention relates to an energy conversion system for heating and cooling an area, such as the interior of a building.
  • the present invention relates to a'heating' and cooling system wherein a hydraulic motor is employed within a fluid configuration for cooling.
  • the hydraulic motor is operated by an energy conversion system of the type wherein high pressure vapor is altematelydirected into one of two reservoir tanks so that working fluid in that tank is forced out of that tank by the vapor pressure and through the hydraulic motor.
  • the hydraulic motor is mechanically linked to a conventional compressor which is connected in the loop in both the heating and cooling configurations, together with a conventional expansion valve and two heat exchangers, which serve respectively as a condensor and evaporator.
  • the compressed temperature control fluid in its gaseous state first passes through one heat exchanger which is disposed so that it exchanges heat with the surrounding air, which is then circulated throughout the building or the like.
  • the high pressure gaseous fluid transfers heat to the surrounding air, it passes through a conventional expansion valve which reduces the pressure to a relatively low value and accordingly lowers the temperature.
  • the expanded fluid next passes through a second heat exchanger from which it absorbs heat.
  • the selection of the temperature control fluid andits resulting physical properties may require the first heat exchanger to be designed as a condensor and the second as an evaporator because a significant portion of the fluid may be converted to the liquid state in the first heat exchanger.
  • the compressed temperature control fluid in its gaseous state first passes through the second heat exchanger where, because of the high pressure resulting from compression, it cools while being maintained at the compressor pressure by transferring heat, preferably to water flowing through the exchanger so that the heated water can be used for washing clothes, drying clothes, bathing, cooking, etc.
  • the compressed, but cooled liquid then passes through the thermally isolated expansion valve, which again reduces the pressure to alower value and thereafter the fluid is circuited through the first heat exchanger, which in this configuration may be required to serve as an evaporator or expander absorbing heat from the surrounding air
  • the first heat exchanger serves as an expander or evaporator and the second heat exchanger as a constant pressure heat rejector or condensor.
  • the mechanical output of the hydraulic motor can also be connected to an electrical generator for providing electrical power and/or other devices for performing other useful functions such as driving garbage disposals, washers, dryers, water pumps, air circulation fans, etc.
  • the novel system of this invention is a particularly simple and effective system for not only heating and cooling an area such as a building employing only a single simple basic energy conversion device for doing so, but also for performing many other functions presently accomplished by other devices. Any fuel can bebumed to derive heat to operate the energy conversion system and accordingly the system is very flexible.
  • FIG. 1 shows the novel heating and cooling system of this invention in its cooling configuration.
  • FIG. 2 shows the novel heating and cooling system of this invention in its heating configuration.
  • FIG. 1 shows one embodiment of this invention in the cooling configuration.
  • the system includes an energy conversion device 18 of the type wherein fluid is alternately forced from one reservoir tank through at least one fluid motor or hydraulic cylinder into the other tank.
  • energy conversion device 18 of the type wherein fluid is alternately forced from one reservoir tank through at least one fluid motor or hydraulic cylinder into the other tank.
  • Such devices are described in further detail in a McAlister application, Ser. No. 58,981 filed July 28, 1970, now U.'S. Pat. No. 3,756,086, and entitled VAPOR PRESSURIZED HYDROSTATIC DRIVE, the disclosure of which is explicitly incorporated herein by reference.
  • the system is particularly suitable for use with one or more hydrostatic motors in parallel with each other or in series.
  • vapor is alternately directed into one of the two reservoir tanks 20 and 22 so that the working fluid in the tank is forced .out of .the tank by the pressure of the vapor, and
  • a suitable reservoir 24 or a fluid such as water is connected to a conventional phase converter or boiler 26, which converts the fluid from a liquid to a vapor phase. This conversion may be accomplished by burning a suitable fuel such as the hydrocarbons, so that the generated heat changes the phase of at least a portion of the fluid in boiler 26. Any other suitable arrangements for generating the vapor which is employed to impart motion to the working fluid can be employed.
  • the vapor pressure output of boiler 26 is directed to either reservoir tank 20 or tank 22 via master valve 28, which may be a conventional solenoid valve or any othe suitable type of valve mechanism. As depicted schematically in FIG. 1, valve 28 is operated by a suitable control apparatus 30, which alternately causes valve 28 to direct the vapor pressure generated by boiler 26 into one of the reservoir tanks 20 and 22.
  • Control 30 may be mechanically or otherwise linked to the fluid motor 38, so that the position of the valve 28 is responsive to the physical position of the rotating part of fluid motor 38.
  • control 30 may include means for sensing the fluid level by electrical or thermal information in tanks and 22 and switching the vapor flow from tank to tank whenever the fluid in either tank is detected above or below a certain predetermined level.
  • control has shifted valve 28 to a position such that the vapor pressure generated by boiler 26 is transmitted into tank 22 as depicted, causing the fluid in tank 22 to exit from the bottom of tank 22 and to flow theough motor 38 via one way check valve 32 as well as the other check valves in this and the other embodiments set forth below, permit fluid flow in one direction but prevent it in the other.
  • Those valves may be of any suitable type and are well known in the art. After passage through motor 38, the moving fluid passes through check valve 34 and enters tank 20.
  • An exhaust vlave 40 which also is shown under the control of apparatus 30, is preferentially vented to heat exchanger 50 when the dwelling is being heated and vented to the atmosphere during times when the dwelling is being cooled, so that thefluid can freely enter tank 20.
  • Valve 42 at the same time, is closed to prevent the loss of the vapor pressure generated by the flow of vapor into tank 22 via valve 28.
  • control mechanism 30 shifts the position of valve 28 so that the vapor pressure generated by boiler 26 is now directed into tank 20 and begins to force the fluid which has refilled it out of tank 20 and through fluid motor 38 via check valve 36.
  • exhaust valve 40 is closed and valve 42 opened by apparatus 30, so that the fluid now flowing through motor 38 bia check valve 36 returns to tank 32 via check valve 39.
  • Open valve 42 permits the vapor pressure in chamber 22 to escape to the atmosphere, so that tank 22 can refill.
  • a portion of the fluid flowing out of one or the other of the tanks 20 or 22 also returns to reservoir 24 via valve 32 or 36.
  • Fluid entering the boiler from reservoir 24 may be manually or otherwise adjusted by apparatus 20 to provide a suitable flow of liquid for vaporization within boiler 26.
  • any other suitable fluid which can be satisfactorily converted from its liquid to its vapor phase can be employed.
  • the use of a common fluid in the air conditioning loop and the boiler loop with heat exchange to the air from closed heat exchangers would be recommended in situations where gound water was of low quality or unavailable.
  • Hydraulic motor 38 is mechanically lined to a conventional compressor 52, which causes both compression of the temperature control fluid and circulation of the temperature control fluid about a closed loop in both the heating and cooling configurations.
  • Motor 38 or another hydraulic motor in series or parallel may also be connected to a conventional electrical generator 54 for providing electrical power for the building.
  • Other hydraulic motors and hydraulic cylinders may be employed to other devices 56 such as fans, garbage disposals, dish washers, clothes washers, clothes dryers, and trash compactors.
  • Devices 56 can include any apparatus capable of being operated from the mechanical output of motor 38 or from a hydraulic cylinder.
  • valves 60, 62, 64, and 66 are shifted manually or automatically to their open positions as shown in FIG. 1 and valves 68, 70, 72, and 74 to their closed positions.
  • the temperature control fluid compressed by compressor 52 flows through line 80, valve 60, line 82, and heat'exchanger 50 in the direction indicated by the arrows.
  • valves 84 and 86 are closed and valve 91 open so that ground water at a relatively low temperature T, flows into heat exchanger 50.
  • the reservoirs filling pressure generally is below the pressure of chamber 50, and enables the evaporating fluid exiting chamber 50 at T to be added to reservoirs 20 and 22 through valves 40 and 42, or through separate circuits, with the result of a depressed temperature (T due to increased evaporative cooling at the reservoir filling pressure.
  • valves 60, 62, 64, and 66 are shifted to their closed positions and valves 68, 70, 72, and 74 to their open positions as shown in FIG. 2. Accordingly, the compressed temperature control fluid in its gaseous state first passes through heat exchanger 102 via valve 68. Because of the relatively high pressure produced by compressor 52, heat is transferred to the air about exchanger 102 in the process. The air thus heated is then conventionally circulated. The fluid via valves and 96 and then enters exchanger 50 via vlave 72.
  • tanks 20 and 22 are preferably vented to heat exchanger 50 as shown. This allows the tank being filled to beat a partial pressure equal to the water vapor pressure.
  • exchanger 50 may be evacuated allowing the development of a lower temperature in the heat exchanger than the entering ground water temperature T
  • An energy conversion system comprising a heat engine and a heat pump circuit, said heat engine including means defining a first energy input zone within which a high energy gaseousvapor is utilized to increase the energy level of fluid medium at a low energy level therein, I means defining a second energy inputzone within which a high energy gaseous vapor is utilized to increase the energy level of the fluid medium at a low energy level therein, means defining an energy conversion zone,
  • said heat pump circuit including means for confining a temperature control fluid for circulation in a closed loop
  • compressor means operatively connected with said energy conversion means to be driven by said motive force and disposed within said closed loop to compress the temperature control fluid and effect circulation of the latter in said closed loop when driven by said motive force,
  • first heat exchanger means operatively connected in heat exchange relation with air to be conditioned and disposed within said closed loop for flow of temperature control fluid therethrough
  • second heat exchanger means operatively connected in heat exchange relation to engine fluid medium and disposed within said closed loop for flow of temperature control fluid therethrough,

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

An energy conversion system, particularly for use in heating, cooling, and generating electrical and mechanical power for an area such as a dwelling. In one embodiment, vapor is alternately directed into one of two reservoir tanks so that working fluid in that tank is forced out of that tank by the vapor pressure and through a hydraulic motor, which powers a compressor and/or other devices such as an electrical power generator, garbage disposal, etc., before it returns to refill the other tank. The system includes a closed loop circuit involving a heat pump compressor for circulating fluid to heat and cool air within a building or the like. When the loop is set in a cooling configuration, compressed fluid passes through a first heat exchanger rejecting heat, and then through an expansion valve to a second heat exchanger, cooling the air about that exchanger before returning to the compressor. When the loop is set in a heating configuration, the compressed fluid in its gaseous state passes first through the second heat exchanger, where it transmits heat to the surrounding air, through the expansion valve and then through the first exchanger, where it receives heat not converted into shaft work by the hydraulic motor before returning to the compressor.

Description

United StatesPatent 1191 McAlister 1451 Apr. 16, 1974 ENERGY CONVERSION SYSTEM [21] Appl. No.: 233,460
[ ABSTRACT An energy conversion system, particularly for use in heating, cooling, and generating electrical and mechanical power for an area such as a dwelling. in one embodiment, vapor is alternately directed into one of two reservoir tanks so that working fluid in that tank is forced out of that tank by the vapor pressure and through a hydraulic motor, which powers a compres- 2 "f 6-0/7211-2/467 sor and/or other devices such as an electrical power generator, garbage disposal, etc., before it returns to [5 Cl. :4 re ll t e ot er ta he y em in lud a c e o p [58] new of Search 62/324 circuit involving a heat pump compressor for circulat- 91/4 ing fluid to heat and cool air Within a building or the like. When the loop is set in a cooling configuration, [56] References Cited compressed fluid passes through a first heat exchanger UNITED STATES PATENTS rejecting heat, and then through an expansion valve to 2,562,748 7/1951 Smith et al 62/324 X a second heat exchanger, cooling the air about that 3,100,965 8/1963 Blackburn 91/4 X exchanger before returning to the compressor. When 3,275,067 9/1966 Smader 62/324 X the loop is Set in a heating onfiguration the com- 3'304'735 2/1967 Alexander 62/324 X pressed fluid in its gaseous state passes first through 3,608,31] 9/1971 Roesel, Jr. 60/108 R the second heat exchanger, where it transmits heat to the surrounding air, through the expansion valve and f' Exam".lerEd]gar Geoghegan then through the first exchanger, where it receives Amstam Exammer A ocstrzger heat not converted into shaft work by the hydraulic Attorney Agent or F'rm us D arby & motor before returning to the compressor. Cushman 1 Claim, 2 Drawing Figures 4m a a Ck z M4 ix/wms/a/v rare fume/v a) {0 yam-wink PATENTEDAPR as W SHE'EI 1 OF 2 (fakvrza;
ff/mz me G/Fm/Aw wan-1e INVENTOR Far Z/Vafluwre ww wfw/ ATTORNEYS mm be m 3,8347
SBEEI 2 N 2 ATTORNEYS I MW? @f M ENERGY CONVERSION SYSTEM BRIEF DESCRIPTION OF THE PRIOR ART AND SUMMARY OF THE INVENTION The invention relates to an energy conversion system for heating and cooling an area, such as the interior of a building.
Most heating and cooling systems now in use include one device which burns fuel or resistively heat wire for providing heat in the winter and another device for cooling in the summer. Although the two devices frequently share the same air handling duct work, such devices are generally inefficient and less than completely satisfactory in many instances. In the summer, for instance, an electric motor driven heat pump provides cooling, but in the winter the heat pump often is not able to absorb sufficient heat at the evaporator due to icing and subsequent inefficiencies.
The present invention relates to a'heating' and cooling system wherein a hydraulic motor is employed within a fluid configuration for cooling. The hydraulic motor is operated by an energy conversion system of the type wherein high pressure vapor is altematelydirected into one of two reservoir tanks so that working fluid in that tank is forced out of that tank by the vapor pressure and through the hydraulic motor.
In the embodiment described below, the hydraulic motor is mechanically linked to a conventional compressor which is connected in the loop in both the heating and cooling configurations, together witha conventional expansion valve and two heat exchangers, which serve respectively as a condensor and evaporator. In the heating configuration, the compressed temperature control fluid in its gaseous state first passes through one heat exchanger which is disposed so that it exchanges heat with the surrounding air, which is then circulated throughout the building or the like. After the high pressure gaseous fluid transfers heat to the surrounding air, it passes through a conventional expansion valve which reduces the pressure to a relatively low value and accordingly lowers the temperature. The expanded fluid next passes through a second heat exchanger from which it absorbs heat. The selection of the temperature control fluid andits resulting physical properties may require the first heat exchanger to be designed as a condensor and the second as an evaporator because a significant portion of the fluid may be converted to the liquid state in the first heat exchanger.
In the cooling configuration, the compressed temperature control fluid in its gaseous state first passes through the second heat exchanger where, because of the high pressure resulting from compression, it cools while being maintained at the compressor pressure by transferring heat, preferably to water flowing through the exchanger so that the heated water can be used for washing clothes, drying clothes, bathing, cooking, etc. The compressed, but cooled liquid then passes through the thermally isolated expansion valve, which again reduces the pressure to alower value and thereafter the fluid is circuited through the first heat exchanger, which in this configuration may be required to serve as an evaporator or expander absorbing heat from the surrounding air In this configuration, the first heat exchanger serves as an expander or evaporator and the second heat exchanger as a constant pressure heat rejector or condensor.
Further, the mechanical output of the hydraulic motor can also be connected to an electrical generator for providing electrical power and/or other devices for performing other useful functions such as driving garbage disposals, washers, dryers, water pumps, air circulation fans, etc. Thus, the novel system of this invention is a particularly simple and effective system for not only heating and cooling an area such as a building employing only a single simple basic energy conversion device for doing so, but also for performing many other functions presently accomplished by other devices. Any fuel can bebumed to derive heat to operate the energy conversion system and accordingly the system is very flexible.
Many other objects and purposes of the invention will become clear from thefollowing detailed description of the drawings.
. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows the novel heating and cooling system of this invention in its cooling configuration.
FIG. 2 shows the novel heating and cooling system of this invention in its heating configuration.
DETAILED DESCRIPTION OF THE DRAWINGS Reference is now made to FIG. 1 which shows one embodiment of this invention in the cooling configuration. As mentioned above, the system includes an energy conversion device 18 of the type wherein fluid is alternately forced from one reservoir tank through at least one fluid motor or hydraulic cylinder into the other tank. Such devices are described in further detail in a McAlister application, Ser. No. 58,981 filed July 28, 1970, now U.'S. Pat. No. 3,756,086, and entitled VAPOR PRESSURIZED HYDROSTATIC DRIVE, the disclosure of which is explicitly incorporated herein by reference. The system is particularly suitable for use with one or more hydrostatic motors in parallel with each other or in series. In this embodiment, as in many of the other embodiments of the invention as set forth in the above mentioned McAlister application, vapor is alternately directed into one of the two reservoir tanks 20 and 22 so that the working fluid in the tank is forced .out of .the tank by the pressure of the vapor, and
through a conventional hydraulic motor 38 to generate a mechanical output before it returns to refill the other tank. When the first tank is substantially depleted, the vapor pressure is directed into the refilled tank so that the fluid from the tank now flows again through motor 38 to refill the first, now depleted, tank.
In FIG. I, a suitable reservoir 24 or a fluid such as water is connected to a conventional phase converter or boiler 26, which converts the fluid from a liquid to a vapor phase. This conversion may be accomplished by burning a suitable fuel such as the hydrocarbons, so that the generated heat changes the phase of at least a portion of the fluid in boiler 26. Any other suitable arrangements for generating the vapor which is employed to impart motion to the working fluid can be employed. The vapor pressure output of boiler 26 is directed to either reservoir tank 20 or tank 22 via master valve 28, which may be a conventional solenoid valve or any othe suitable type of valve mechanism. As depicted schematically in FIG. 1, valve 28 is operated by a suitable control apparatus 30, which alternately causes valve 28 to direct the vapor pressure generated by boiler 26 into one of the reservoir tanks 20 and 22.
Control 30 may be mechanically or otherwise linked to the fluid motor 38, so that the position of the valve 28 is responsive to the physical position of the rotating part of fluid motor 38. Alternately, control 30 may include means for sensing the fluid level by electrical or thermal information in tanks and 22 and switching the vapor flow from tank to tank whenever the fluid in either tank is detected above or below a certain predetermined level.
Assume for purposes of describing the operating of the embodiments of FIG. 1 and 2, that control has shifted valve 28 to a position such that the vapor pressure generated by boiler 26 is transmitted into tank 22 as depicted, causing the fluid in tank 22 to exit from the bottom of tank 22 and to flow theough motor 38 via one way check valve 32 as well as the other check valves in this and the other embodiments set forth below, permit fluid flow in one direction but prevent it in the other. Those valves may be of any suitable type and are well known in the art. After passage through motor 38, the moving fluid passes through check valve 34 and enters tank 20. An exhaust vlave 40, which also is shown under the control of apparatus 30, is preferentially vented to heat exchanger 50 when the dwelling is being heated and vented to the atmosphere during times when the dwelling is being cooled, so that thefluid can freely enter tank 20. Valve 42, at the same time, is closed to prevent the loss of the vapor pressure generated by the flow of vapor into tank 22 via valve 28.
The cyclic venting of tanks 20 and 22 to heat exchanger 50 in the heating configuration and to the atmosphere in the cooling configuration may in some duty cycles result in a gradual reduction in the quantity of working fluid in the'sustem. Reservoir 24, provides some make-up fluid since some of the vapor directed into the tanks condenses therein and is thus added to the supply of working fluid. However, it may be desirable to provide some suitable arrangement for automatically or otherwise replenishing the working fluid from time to time. I
.When tank 22 has been depleted or substantially depleted, control mechanism 30 shifts the position of valve 28 so that the vapor pressure generated by boiler 26 is now directed into tank 20 and begins to force the fluid which has refilled it out of tank 20 and through fluid motor 38 via check valve 36. At the same time, exhaust valve 40 is closed and valve 42 opened by apparatus 30, so that the fluid now flowing through motor 38 bia check valve 36 returns to tank 32 via check valve 39. Open valve 42 permits the vapor pressure in chamber 22 to escape to the atmosphere, so that tank 22 can refill.
A portion of the fluid flowing out of one or the other of the tanks 20 or 22 also returns to reservoir 24 via valve 32 or 36. Fluid entering the boiler from reservoir 24 may be manually or otherwise adjusted by apparatus 20 to provide a suitable flow of liquid for vaporization within boiler 26. As mentioned above, while water is one suitable material which exits in the vapor and gaseous phase and can be suitably used in this arrangement, any other suitable fluid which can be satisfactorily converted from its liquid to its vapor phase can be employed. The use ofa common fluid in the air conditioning loop and the boiler loop with heat exchange to the air from closed heat exchangers would be recommended in situations where gound water was of low quality or unavailable.
Hydraulic motor 38 is mechanically lined to a conventional compressor 52, which causes both compression of the temperature control fluid and circulation of the temperature control fluid about a closed loop in both the heating and cooling configurations. Motor 38 or another hydraulic motor in series or parallel may also be connected to a conventional electrical generator 54 for providing electrical power for the building. Other hydraulic motors and hydraulic cylinders may be employed to other devices 56 such as fans, garbage disposals, dish washers, clothes washers, clothes dryers, and trash compactors. Devices 56 can include any apparatus capable of being operated from the mechanical output of motor 38 or from a hydraulic cylinder.
When system 18 is to be operated in the cooling configuration, valves 60, 62, 64, and 66 are shifted manually or automatically to their open positions as shown in FIG. 1 and valves 68, 70, 72, and 74 to their closed positions. When the valves are in the positions shown in FIG. 1, the temperature control fluid compressed by compressor 52, flows through line 80, valve 60, line 82, and heat'exchanger 50 in the direction indicated by the arrows. Further, when in the cooling configuration, valves 84 and 86 are closed and valve 91 open so that ground water at a relatively low temperature T, flows into heat exchanger 50. It is further preferred while in cooling operation to open valves 1 18 and 1 19 allowing fluid returning from the motors or hydraulic cylinders, which has been cooled by passing from a high pressure state to a low pressure state by doing work in the motor and further by dissipating heat to the surroundings to enter the reservoirs 20 and 22 in a means accomplishing condensation of residual vapors so that the pressure in a reservoir during filling approaches the working fluids vapor pressure at the temperature of the return fluid. Thus, the reservoirs filling pressure generally is below the pressure of chamber 50, and enables the evaporating fluid exiting chamber 50 at T to be added to reservoirs 20 and 22 through valves 40 and 42, or through separate circuits, with the result of a depressed temperature (T due to increased evaporative cooling at the reservoir filling pressure.
When the system to operate in the heating configuration, valves 60, 62, 64, and 66 are shifted to their closed positions and valves 68, 70, 72, and 74 to their open positions as shown in FIG. 2. Accordingly, the compressed temperature control fluid in its gaseous state first passes through heat exchanger 102 via valve 68. Because of the relatively high pressure produced by compressor 52, heat is transferred to the air about exchanger 102 in the process. The air thus heated is then conventionally circulated. The fluid via valves and 96 and then enters exchanger 50 via vlave 72. Water at a temperature T,, which may be considerably higher than outside air because of heat gained from exchanger 109 consisting of heat not converted into mechanical power by the energy conversion engine system, enters the heat exchanger 50, transfers heat to the expanded temperature control fluid and exits at a temperature T as shown, which is less than T,. Thus, heat not used in powering convenience devices is used to heat the home.
Further, when the system is in the cooling configuration, FIG. 1, tanks 20 and 22 are preferably vented to heat exchanger 50 as shown. This allows the tank being filled to beat a partial pressure equal to the water vapor pressure. By placing the line between tanks 20 and 22 and exchanger 50 in a position causing Bernoulli pumping while the tank is filling, exchanger 50 may be evacuated allowing the development of a lower temperature in the heat exchanger than the entering ground water temperature T Many changes and modifications in the above em bodiments of the invention can of course, be made without departing from the scope of the invention which is intended to be limited only by the scope of the appended claims.
What is claimed is:
1. An energy conversion system comprising a heat engine and a heat pump circuit, said heat engine including means defining a first energy input zone within which a high energy gaseousvapor is utilized to increase the energy level of fluid medium at a low energy level therein, I means defining a second energy inputzone within which a high energy gaseous vapor is utilized to increase the energy level of the fluid medium at a low energy level therein, means defining an energy conversion zone,
means for alternately communicating the increased energy level medium within said first and second energy input zones in first and second fluid energy transmitting relationships with said first energy conversion zone and for causing flow of increased energy level medium out of said first and second energy input zones and flow of increased energy level medium in a liquid phase into said energy conversion zone,
means for converting within said energy conversion zone a portion of the energy of said increased energy level medium in said first and second fluid energy transmitting relationships into motive force thereby reducing the energy level of said medium in said first and second energy transmitting relationships,
means for alternately communicating reduced energy level medium in a liquid phase within said'energy conversion zone with said first and second energy input zones and for causing reduced energy level medium in a liquid phase to flow out of said energy conversion zone and reduced energy level medium to flow alternately into said first and second energy input zones, and
means for obtaining the high energy gaseous vapor utilized within said first and second energy input zones by adding heat to medium which has been energized by energy transfer with fluid medium in said first and second fluid energy transmitting relationships,
said heat pump circuit including means for confining a temperature control fluid for circulation in a closed loop,
compressor means operatively connected with said energy conversion means to be driven by said motive force and disposed within said closed loop to compress the temperature control fluid and effect circulation of the latter in said closed loop when driven by said motive force,
first heat exchanger means operatively connected in heat exchange relation with air to be conditioned and disposed within said closed loop for flow of temperature control fluid therethrough,
second heat exchanger means operatively connected in heat exchange relation to engine fluid medium and disposed within said closed loop for flow of temperature control fluid therethrough,
expansion valve means disposed within said closed loop,
means for alternately directing the circulation of temperature control fluid in said closed loop from said compresser means (1) through said first heat exchanger means, said expansion valve means, and then said second heat exchanger means and (2) through said second heat exchanger means, said expansion valve means and then 'said first heat exchanger menas, and
means for alternately communicating the working fluid in heat exchange relation with said second heat exchanger means l with the reduced energy level medium flowing alternately into said first and second energy input zones when the circulation within said closed loop is directed as set forth in (2) 1 above and (2) in heat exchange relation with the increased medium in said first and second fluid energy transmitting relationships when the circulation within said closed loop is directed as set forth in (1) above.

Claims (1)

1. An energy conversion system comprising a heat engine and a heat pump circuit, said heat engine including means defining a first energy input zone within which a high energy gaseous vapor is utilized to increase the energy level of fluid medium at a low energy level therein, means defining a second energy input zone within which a high energy gaseous vapor is utilized to increase the energy level of the fluid medium at a low energy level therein, means defining an energy conversion zone, means for alternately communicating the increased energy level medium within said first and second energy input zones in first and second fluid energy transmitting relationships with said first energy conversion zone and for causing flow of increased energy level medium out of said first and second energy input zones and flow of increased energy level medium in a liquid phase into said energy conversion zone, means for converting within said energy conversion zone a portion of the energy of said increased energy level medium in said first and second fluid energy transmitting relationships into motive force thereby reducing the energy level of said medium in said first and second energy transmitting relationships, means for alternately communicating reduced energy level medium in a liquid phase within said energy conversion zone with said first and second energy input zones and for causing reduced energy level medium in a liquid phase to flow out of said energy conversion zone and reduced energy level medium to flow alternately into said first and second energy input zones, and means for obtaining the high energy gaseous vapor utilized within said first and second energy input zones by adding heat to medium which has been energized by energy transfer with fluid medium in said first and second fluid energy transmitting relationships, said heat pump circuit including means for confining a temperature control fluid for circulation in a closed loop, compressor means operatively connected with said energy conversion means to be driven by said motive force and disposed within said closed loop to compress the temperature control fluid and effect circulation of the latter in said closed loop when driven by said motive force, first heat exchanger means operatively connected in heat exchange relation with air to be conditioned and disposed within said closed loop for flow of temperature control fluid therethrough, second heat exchanger means operatively connected in heat exchange relation to engine fluid medium and disposed within said closed loop for flow of temperature control fluid therethrough, expansion valve means disposed within said closed loop, means for alternately directing the circulation of temperature control fluid in said closed loop from said compresser means (1) through said first heat exchanger means, said expansion valve means, and then said second heat exchanger means and (2) through said second heat exchanger means, said expansion valve means and then said first heat exchanger menas, and means for alternately communicating the working fluid in heat exchange relation with said second heat exchanger means (1) with the reduced energy level medium flowing alternately into said first and second energy input zones when the circulation within said closed loop is directed as set forth in (2) above and (2) in heat exchange relation with the increased medium in said first and second fluid energy transmitting relationships when the circulation within said closed loop is directed as set forth in (1) above.
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US3890784A (en) * 1973-04-26 1975-06-24 Europ Propulsion Thermohydraulic engines
US4055964A (en) * 1976-11-01 1977-11-01 Consolidated Natural Gas Service Company Heat pump system
US4103493A (en) * 1975-03-06 1978-08-01 Hansen, Lind, Meyer Solar power system
US4178772A (en) * 1976-11-01 1979-12-18 Consolidated Natural Gas Service Company, Inc. Heat pump system
US4312188A (en) * 1977-10-25 1982-01-26 Consolidated Natural Gas Service Company, Inc. Heat pump system
US4378785A (en) * 1981-05-28 1983-04-05 Dale Fleischmann Solar heating system
US4378787A (en) * 1981-05-28 1983-04-05 Dale Fleischmann Solar heating system
USRE31281E (en) * 1976-11-01 1983-06-21 Consolidated Natural Gas Service Company, Inc. Heat pump system
US4783961A (en) * 1987-06-16 1988-11-15 Walters Randall W Natural gas pressure differential energy recovery system
US5127369A (en) * 1991-05-21 1992-07-07 Goldshtik Mikhail A Engine employing rotating liquid as a piston
US6250199B1 (en) * 1999-04-27 2001-06-26 Deep Oil Technology, Incorporated Subsea power module
US20040237525A1 (en) * 2001-07-07 2004-12-02 Gerhard Stock Assembly of gas expansion elements and method of operating said assembly
WO2007137315A2 (en) 2006-06-01 2007-12-06 International Innovations Limited Method and device for converting thermal energy into mechanical work
US20090113740A1 (en) * 2007-11-06 2009-05-07 Bsh Bosch Und Siemens Hausgeraete Gmbh Dryer with heat pump
US20090293301A1 (en) * 2006-06-06 2009-12-03 BSH Bosch und Siemens Hausgeräte GmbH Device and Method for Drying Laundry
US20100089063A1 (en) * 2008-04-09 2010-04-15 Sustainx, Inc. Systems and Methods for Energy Storage and Recovery Using Rapid Isothermal Gas Expansion and Compression
US20100205960A1 (en) * 2009-01-20 2010-08-19 Sustainx, Inc. Systems and Methods for Combined Thermal and Compressed Gas Energy Conversion Systems
US20100229544A1 (en) * 2009-03-12 2010-09-16 Sustainx, Inc. Systems and Methods for Improving Drivetrain Efficiency for Compressed Gas Energy Storage
US20100307156A1 (en) * 2009-06-04 2010-12-09 Bollinger Benjamin R Systems and Methods for Improving Drivetrain Efficiency for Compressed Gas Energy Storage and Recovery Systems
US20110107755A1 (en) * 2009-09-11 2011-05-12 Mcbride Troy O Energy storage and generation systems and methods using coupled cylinder assemblies
US20110131966A1 (en) * 2009-11-03 2011-06-09 Mcbride Troy O Systems and methods for compressed-gas energy storage using coupled cylinder assemblies
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US8104274B2 (en) 2009-06-04 2012-01-31 Sustainx, Inc. Increased power in compressed-gas energy storage and recovery
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US8171728B2 (en) 2010-04-08 2012-05-08 Sustainx, Inc. High-efficiency liquid heat exchange in compressed-gas energy storage systems
US8191362B2 (en) 2010-04-08 2012-06-05 Sustainx, Inc. Systems and methods for reducing dead volume in compressed-gas energy storage systems
US8234863B2 (en) 2010-05-14 2012-08-07 Sustainx, Inc. Forming liquid sprays in compressed-gas energy storage systems for effective heat exchange
US8240140B2 (en) 2008-04-09 2012-08-14 Sustainx, Inc. High-efficiency energy-conversion based on fluid expansion and compression
US8240146B1 (en) 2008-06-09 2012-08-14 Sustainx, Inc. System and method for rapid isothermal gas expansion and compression for energy storage
US8250863B2 (en) 2008-04-09 2012-08-28 Sustainx, Inc. Heat exchange with compressed gas in energy-storage systems
US8272212B2 (en) 2011-11-11 2012-09-25 General Compression, Inc. Systems and methods for optimizing thermal efficiencey of a compressed air energy storage system
US20120297761A1 (en) * 2010-03-17 2012-11-29 Alexander Anatolyevich Strognaov Method of conversion of heat into fluid power and device for its implementation
US8359856B2 (en) 2008-04-09 2013-01-29 Sustainx Inc. Systems and methods for efficient pumping of high-pressure fluids for energy storage and recovery
US8448433B2 (en) 2008-04-09 2013-05-28 Sustainx, Inc. Systems and methods for energy storage and recovery using gas expansion and compression
US8474255B2 (en) 2008-04-09 2013-07-02 Sustainx, Inc. Forming liquid sprays in compressed-gas energy storage systems for effective heat exchange
US8479505B2 (en) 2008-04-09 2013-07-09 Sustainx, Inc. Systems and methods for reducing dead volume in compressed-gas energy storage systems
US8495872B2 (en) 2010-08-20 2013-07-30 Sustainx, Inc. Energy storage and recovery utilizing low-pressure thermal conditioning for heat exchange with high-pressure gas
US8522538B2 (en) 2011-11-11 2013-09-03 General Compression, Inc. Systems and methods for compressing and/or expanding a gas utilizing a bi-directional piston and hydraulic actuator
US8539763B2 (en) 2011-05-17 2013-09-24 Sustainx, Inc. Systems and methods for efficient two-phase heat transfer in compressed-air energy storage systems
US8567303B2 (en) 2010-12-07 2013-10-29 General Compression, Inc. Compressor and/or expander device with rolling piston seal
US8572959B2 (en) 2011-01-13 2013-11-05 General Compression, Inc. Systems, methods and devices for the management of heat removal within a compression and/or expansion device or system
US8578708B2 (en) 2010-11-30 2013-11-12 Sustainx, Inc. Fluid-flow control in energy storage and recovery systems
US8667792B2 (en) 2011-10-14 2014-03-11 Sustainx, Inc. Dead-volume management in compressed-gas energy storage and recovery systems
US8677744B2 (en) 2008-04-09 2014-03-25 SustaioX, Inc. Fluid circulation in energy storage and recovery systems
US8997475B2 (en) 2011-01-10 2015-04-07 General Compression, Inc. Compressor and expander device with pressure vessel divider baffle and piston
US9109511B2 (en) 2009-12-24 2015-08-18 General Compression, Inc. System and methods for optimizing efficiency of a hydraulically actuated system
US9109512B2 (en) 2011-01-14 2015-08-18 General Compression, Inc. Compensated compressed gas storage systems
WO2015134672A1 (en) * 2014-03-04 2015-09-11 Wave Solar, Llc Liquid piston engine
US9540963B2 (en) 2011-04-14 2017-01-10 Gershon Machine Ltd. Generator
CN106567748A (en) * 2016-11-02 2017-04-19 西安交通大学 Nonadiabatic gas expansion compressed air energy storage system
CN106677848A (en) * 2016-12-29 2017-05-17 西安交通大学 Joint energy storage system and method with air and water as energy storage working media
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US3890784A (en) * 1973-04-26 1975-06-24 Europ Propulsion Thermohydraulic engines
US4103493A (en) * 1975-03-06 1978-08-01 Hansen, Lind, Meyer Solar power system
US4055964A (en) * 1976-11-01 1977-11-01 Consolidated Natural Gas Service Company Heat pump system
US4178772A (en) * 1976-11-01 1979-12-18 Consolidated Natural Gas Service Company, Inc. Heat pump system
USRE31281E (en) * 1976-11-01 1983-06-21 Consolidated Natural Gas Service Company, Inc. Heat pump system
US4312188A (en) * 1977-10-25 1982-01-26 Consolidated Natural Gas Service Company, Inc. Heat pump system
US4378787A (en) * 1981-05-28 1983-04-05 Dale Fleischmann Solar heating system
US4378785A (en) * 1981-05-28 1983-04-05 Dale Fleischmann Solar heating system
US4783961A (en) * 1987-06-16 1988-11-15 Walters Randall W Natural gas pressure differential energy recovery system
US5127369A (en) * 1991-05-21 1992-07-07 Goldshtik Mikhail A Engine employing rotating liquid as a piston
WO1994001665A1 (en) * 1991-05-21 1994-01-20 Goldshtik Mikhail A Engine employing rotating liquid as a piston
US6250199B1 (en) * 1999-04-27 2001-06-26 Deep Oil Technology, Incorporated Subsea power module
US20040237525A1 (en) * 2001-07-07 2004-12-02 Gerhard Stock Assembly of gas expansion elements and method of operating said assembly
CN101484683B (en) * 2006-06-01 2012-02-22 国际创新有限公司 Method and device for converting thermal energy into mechanical work
WO2007137315A2 (en) 2006-06-01 2007-12-06 International Innovations Limited Method and device for converting thermal energy into mechanical work
WO2007137315A3 (en) * 2006-06-01 2008-12-04 Int Innovations Ltd Method and device for converting thermal energy into mechanical work
AT503734B1 (en) * 2006-06-01 2008-11-15 Int Innovations Ltd METHOD FOR CONVERTING THERMAL ENERGY TO MECHANICAL WORK
US20090293301A1 (en) * 2006-06-06 2009-12-03 BSH Bosch und Siemens Hausgeräte GmbH Device and Method for Drying Laundry
US20090113740A1 (en) * 2007-11-06 2009-05-07 Bsh Bosch Und Siemens Hausgeraete Gmbh Dryer with heat pump
US8418377B2 (en) * 2007-11-06 2013-04-16 Bsh Bosch Und Siemens Hausgeraete Gmbh Dryer with heat pump
US8713929B2 (en) 2008-04-09 2014-05-06 Sustainx, Inc. Systems and methods for energy storage and recovery using compressed gas
US20100089063A1 (en) * 2008-04-09 2010-04-15 Sustainx, Inc. Systems and Methods for Energy Storage and Recovery Using Rapid Isothermal Gas Expansion and Compression
US8763390B2 (en) 2008-04-09 2014-07-01 Sustainx, Inc. Heat exchange with compressed gas in energy-storage systems
US8733095B2 (en) 2008-04-09 2014-05-27 Sustainx, Inc. Systems and methods for efficient pumping of high-pressure fluids for energy
US8240140B2 (en) 2008-04-09 2012-08-14 Sustainx, Inc. High-efficiency energy-conversion based on fluid expansion and compression
US8733094B2 (en) 2008-04-09 2014-05-27 Sustainx, Inc. Systems and methods for energy storage and recovery using rapid isothermal gas expansion and compression
US8250863B2 (en) 2008-04-09 2012-08-28 Sustainx, Inc. Heat exchange with compressed gas in energy-storage systems
US20110219760A1 (en) * 2008-04-09 2011-09-15 Mcbride Troy O Systems and methods for energy storage and recovery using compressed gas
US8225606B2 (en) 2008-04-09 2012-07-24 Sustainx, Inc. Systems and methods for energy storage and recovery using rapid isothermal gas expansion and compression
US8677744B2 (en) 2008-04-09 2014-03-25 SustaioX, Inc. Fluid circulation in energy storage and recovery systems
US8627658B2 (en) 2008-04-09 2014-01-14 Sustainx, Inc. Systems and methods for energy storage and recovery using rapid isothermal gas expansion and compression
US8479505B2 (en) 2008-04-09 2013-07-09 Sustainx, Inc. Systems and methods for reducing dead volume in compressed-gas energy storage systems
US8474255B2 (en) 2008-04-09 2013-07-02 Sustainx, Inc. Forming liquid sprays in compressed-gas energy storage systems for effective heat exchange
US8209974B2 (en) 2008-04-09 2012-07-03 Sustainx, Inc. Systems and methods for energy storage and recovery using compressed gas
US8359856B2 (en) 2008-04-09 2013-01-29 Sustainx Inc. Systems and methods for efficient pumping of high-pressure fluids for energy storage and recovery
US8448433B2 (en) 2008-04-09 2013-05-28 Sustainx, Inc. Systems and methods for energy storage and recovery using gas expansion and compression
US8240146B1 (en) 2008-06-09 2012-08-14 Sustainx, Inc. System and method for rapid isothermal gas expansion and compression for energy storage
US8122718B2 (en) 2009-01-20 2012-02-28 Sustainx, Inc. Systems and methods for combined thermal and compressed gas energy conversion systems
US20100205960A1 (en) * 2009-01-20 2010-08-19 Sustainx, Inc. Systems and Methods for Combined Thermal and Compressed Gas Energy Conversion Systems
US8234862B2 (en) 2009-01-20 2012-08-07 Sustainx, Inc. Systems and methods for combined thermal and compressed gas energy conversion systems
US7958731B2 (en) * 2009-01-20 2011-06-14 Sustainx, Inc. Systems and methods for combined thermal and compressed gas energy conversion systems
US20100229544A1 (en) * 2009-03-12 2010-09-16 Sustainx, Inc. Systems and Methods for Improving Drivetrain Efficiency for Compressed Gas Energy Storage
US7963110B2 (en) 2009-03-12 2011-06-21 Sustainx, Inc. Systems and methods for improving drivetrain efficiency for compressed gas energy storage
US8234868B2 (en) 2009-03-12 2012-08-07 Sustainx, Inc. Systems and methods for improving drivetrain efficiency for compressed gas energy storage
US20100307156A1 (en) * 2009-06-04 2010-12-09 Bollinger Benjamin R Systems and Methods for Improving Drivetrain Efficiency for Compressed Gas Energy Storage and Recovery Systems
US8104274B2 (en) 2009-06-04 2012-01-31 Sustainx, Inc. Increased power in compressed-gas energy storage and recovery
US8479502B2 (en) 2009-06-04 2013-07-09 Sustainx, Inc. Increased power in compressed-gas energy storage and recovery
US20110138797A1 (en) * 2009-06-04 2011-06-16 Bollinger Benjamin R Systems and methods for improving drivetrain efficiency for compressed gas energy storage and recovery systems
US8046990B2 (en) 2009-06-04 2011-11-01 Sustainx, Inc. Systems and methods for improving drivetrain efficiency for compressed gas energy storage and recovery systems
US8468815B2 (en) 2009-09-11 2013-06-25 Sustainx, Inc. Energy storage and generation systems and methods using coupled cylinder assemblies
US20110107755A1 (en) * 2009-09-11 2011-05-12 Mcbride Troy O Energy storage and generation systems and methods using coupled cylinder assemblies
US8109085B2 (en) 2009-09-11 2012-02-07 Sustainx, Inc. Energy storage and generation systems and methods using coupled cylinder assemblies
US8037678B2 (en) 2009-09-11 2011-10-18 Sustainx, Inc. Energy storage and generation systems and methods using coupled cylinder assemblies
US8117842B2 (en) 2009-11-03 2012-02-21 Sustainx, Inc. Systems and methods for compressed-gas energy storage using coupled cylinder assemblies
US20110131966A1 (en) * 2009-11-03 2011-06-09 Mcbride Troy O Systems and methods for compressed-gas energy storage using coupled cylinder assemblies
US9109511B2 (en) 2009-12-24 2015-08-18 General Compression, Inc. System and methods for optimizing efficiency of a hydraulically actuated system
US9140273B2 (en) * 2010-03-17 2015-09-22 Alexander Anatolyevich Stroganov Method of conversion of heat into fluid power and device for its implementation
US20120297761A1 (en) * 2010-03-17 2012-11-29 Alexander Anatolyevich Strognaov Method of conversion of heat into fluid power and device for its implementation
US8171728B2 (en) 2010-04-08 2012-05-08 Sustainx, Inc. High-efficiency liquid heat exchange in compressed-gas energy storage systems
US8245508B2 (en) 2010-04-08 2012-08-21 Sustainx, Inc. Improving efficiency of liquid heat exchange in compressed-gas energy storage systems
US8661808B2 (en) 2010-04-08 2014-03-04 Sustainx, Inc. High-efficiency heat exchange in compressed-gas energy storage systems
US8191362B2 (en) 2010-04-08 2012-06-05 Sustainx, Inc. Systems and methods for reducing dead volume in compressed-gas energy storage systems
US20120079825A1 (en) * 2010-04-15 2012-04-05 Gershon Machine Ltd. Generator
US8800280B2 (en) * 2010-04-15 2014-08-12 Gershon Machine Ltd. Generator
US8234863B2 (en) 2010-05-14 2012-08-07 Sustainx, Inc. Forming liquid sprays in compressed-gas energy storage systems for effective heat exchange
US8495872B2 (en) 2010-08-20 2013-07-30 Sustainx, Inc. Energy storage and recovery utilizing low-pressure thermal conditioning for heat exchange with high-pressure gas
US8578708B2 (en) 2010-11-30 2013-11-12 Sustainx, Inc. Fluid-flow control in energy storage and recovery systems
US8567303B2 (en) 2010-12-07 2013-10-29 General Compression, Inc. Compressor and/or expander device with rolling piston seal
US8997475B2 (en) 2011-01-10 2015-04-07 General Compression, Inc. Compressor and expander device with pressure vessel divider baffle and piston
US8572959B2 (en) 2011-01-13 2013-11-05 General Compression, Inc. Systems, methods and devices for the management of heat removal within a compression and/or expansion device or system
US9260966B2 (en) 2011-01-13 2016-02-16 General Compression, Inc. Systems, methods and devices for the management of heat removal within a compression and/or expansion device or system
US9109512B2 (en) 2011-01-14 2015-08-18 General Compression, Inc. Compensated compressed gas storage systems
US9540963B2 (en) 2011-04-14 2017-01-10 Gershon Machine Ltd. Generator
US8806866B2 (en) 2011-05-17 2014-08-19 Sustainx, Inc. Systems and methods for efficient two-phase heat transfer in compressed-air energy storage systems
US8539763B2 (en) 2011-05-17 2013-09-24 Sustainx, Inc. Systems and methods for efficient two-phase heat transfer in compressed-air energy storage systems
US8667792B2 (en) 2011-10-14 2014-03-11 Sustainx, Inc. Dead-volume management in compressed-gas energy storage and recovery systems
US8272212B2 (en) 2011-11-11 2012-09-25 General Compression, Inc. Systems and methods for optimizing thermal efficiencey of a compressed air energy storage system
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US8522538B2 (en) 2011-11-11 2013-09-03 General Compression, Inc. Systems and methods for compressing and/or expanding a gas utilizing a bi-directional piston and hydraulic actuator
WO2015134672A1 (en) * 2014-03-04 2015-09-11 Wave Solar, Llc Liquid piston engine
CN106567748A (en) * 2016-11-02 2017-04-19 西安交通大学 Nonadiabatic gas expansion compressed air energy storage system
CN106677848A (en) * 2016-12-29 2017-05-17 西安交通大学 Joint energy storage system and method with air and water as energy storage working media
CN106677848B (en) * 2016-12-29 2018-03-02 西安交通大学 A kind of joint energy-storage system and method using air and water as energy storage working medium
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WO2020256620A1 (en) * 2019-06-17 2020-12-24 Sigvard Weisbjerg An electric power-generating device and method of operating such a device
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