EP2313710A1 - Dispositifs et systèmes d'absorption et de libération d'énergie - Google Patents

Dispositifs et systèmes d'absorption et de libération d'énergie

Info

Publication number
EP2313710A1
EP2313710A1 EP09785239A EP09785239A EP2313710A1 EP 2313710 A1 EP2313710 A1 EP 2313710A1 EP 09785239 A EP09785239 A EP 09785239A EP 09785239 A EP09785239 A EP 09785239A EP 2313710 A1 EP2313710 A1 EP 2313710A1
Authority
EP
European Patent Office
Prior art keywords
zeolite
molecular sieve
water vapour
absorbing
thermal energy
Prior art date
Legal status (The legal status 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 status listed.)
Withdrawn
Application number
EP09785239A
Other languages
German (de)
English (en)
Inventor
Douglas Nangle
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carbon Zero Ltd
Original Assignee
Carbon Zero Ltd
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
Application filed by Carbon Zero Ltd filed Critical Carbon Zero Ltd
Publication of EP2313710A1 publication Critical patent/EP2313710A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B17/00—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type
    • F25B17/08—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0011—Heating features
    • B01D1/0017—Use of electrical or wave energy
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0011—Heating features
    • B01D1/0029—Use of radiation
    • B01D1/0035—Solar energy
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0082—Regulation; Control
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S10/00—Solar heat collectors using working fluids
    • F24S10/70—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits
    • F24S10/75—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits with enlarged surfaces, e.g. with protrusions or corrugations
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S60/00—Arrangements for storing heat collected by solar heat collectors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S60/00—Arrangements for storing heat collected by solar heat collectors
    • F24S60/10—Arrangements for storing heat collected by solar heat collectors using latent heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S60/00—Arrangements for storing heat collected by solar heat collectors
    • F24S60/20—Arrangements for storing heat collected by solar heat collectors using chemical reactions, e.g. thermochemical reactions or isomerisation reactions
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/003—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08—Seawater, e.g. for desalination
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00—Fins
    • F28F2215/10—Secondary fins, e.g. projections or recesses on main fins
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y02A20/138—Water desalination using renewable energy
    • Y02A20/142—Solar thermal; Photovoltaics
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20—Controlling water pollution; Waste water treatment
    • Y02A20/208—Off-grid powered water treatment
    • Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/44—Heat exchange systems
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14—Thermal energy storage
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E70/00—Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin

Definitions

  • This invention relates to systems and devices for absorbing and releasing thermal energy.
  • the invention can be used in a number of ways, examples include systems and devices:
  • One particular aspect of the invention describes a device for converting rotational energy to thermal energy, absorbing it, subsequently releasing thermal energy.
  • Energy storage means are well known, for example normal electrical rechargeable batteries, ceramic materials used in storage heaters and hot water cylinders. But all are relatively inefficient.
  • the systems and devices described in this invention can operate efficiently directly using energy generated from so called green sources, such as wind generators and solar power. In both cases peak energy generation does not usually match peak demand and a relatively efficient means of absorbing and subsequently releasing energy is needed.
  • Patent Citation 0001 JP 2004003832 A (DENSO CORP). 2004-01-18. proposes a thermal storage system comprising a material which releases heat when water is supplied and absorb heat by ejecting water when heated.
  • the material can be a hydrate of calcium chloride, calcium bromide, lithium bromide, or zeolite. This device requires the material to be sprayed with water droplets on top of the material and absorption of water by the material is poor.
  • Patent Citation 0002 US 4741028 B (ALEFELD). 1983-10-18. describes a system for storing and upgrading heat in which a zeolite is used to absorb relatively warm water under pressure and requires significant energy supply and is not an energy storage system of the kind being addressed here.
  • Patent Citation 0003 US 4742868 B (MITANI). 1988-05-18. describes a thermal energy storage system using, inter-alia, a zeolite medium for storage. But the system does not ensure widespread distribution of heat within the zeolite during discharge or efficient distribution of water vapour within the zeolite on recharge, thus the system is relative inefficient.
  • Patent Citation 0004 EP 1666140 A (TOSOH CORPORATION). 2006-06-07. describes a zeolite- water heat pump system and an open cycle moisture adsorption- desorption system. Total efficiency is still relatively poor as heat and water vapour is not distributed widely and quickly within the zeolite, and a separate pump is needed to evacuate the zeolite.
  • This invention provides a device for absorbing and releasing thermal energy comprising a container containing zeolite characterised in that the zeolite is in the form of a molecular sieve.
  • said device incorporates a means to provide for unidirectional flow of water vapour on its expulsion from the zeolite molecular sieve and includes means to admit water vapour to the zeolite molecular sieve whereby the zeolite molecular sieve may be charged by heating it from an heat energy source to drive water vapour from there from and discharged by admitting water vapour into the zeolite molecular sieve under reduced pressure created within the container by cooling of the zeolite, thus releasing heat by the exothermic reaction between the water vapour and the zeolite.
  • the invention can also be used with conventional energy sources.
  • the invention can also be used as a sink for unwanted energy, say as part of an air conditioning system for a closed room or building; and subsequent discharge of that energy externally.
  • the said one or more ducts may be in a central core disposed generally around a central axis of the container. In another embodiment the one or more ducts may be disposed on an inner wall of the container, and preferably be part of said wall.
  • the container has with at least one electrical heating element at the core of the container thermally connected to the zeolite molecular sieve by radiating fingers and fins extending laterally therefrom.
  • the core may also contain the ducts. If the cylinder is cylindrical greater efficiency is obtained as heat and water vapour are distributed evenly throughout the device.
  • the heat energy source is a solar panel.
  • the heat energy source is provided by magnetic fields generating a magnetic flux in the device.
  • the ducts are conveniently formed on the inside wall of the container.
  • the means to allow expulsion of water vapour may be connected to a condenser and means is provided to recover heat from the condenser.
  • the device of this invention may incorporate a switchable valve at any one time to allow expulsion of water vapour to a condenser or entry of water vapour from an evaporator.
  • the means to admit water is coupled an evaporator to evaporate water at low pressure and temperature, which evaporator is connected to a low grade heat source.
  • the heat recovered from the condenser may be used to provide low grade heat to an evaporator and/or to a de- aerator.
  • the means to admit water vapour is connected to the evaporator, which in turn is connectable to a source of impure water.
  • a de-aerator is connected between the source of impure water and the evaporator.
  • the means to admit water vapour is connected to an evaporator and the evaporator has a heat exchanger to take heat from a cooling system to vaporise water in the evaporator.
  • a number of devices of this invention may be linked with the means to allow expulsion of water vapour from each container being connected to a single condenser and the means to admit water vapour is connected to a single evaporator.
  • a control system can be provided such that the zeolite in different containers may be at different stages of their charging and or discharging.
  • the device By passing a heat transfer medium in a conduit going through the container, the heat generated by the exothermic reaction can be removed from the system. It will be seen that the device is thus a thermal storage battery charged when water vapour is driven from the zeolite absorbing thermal energy from the heat source, and discharged by releasing thermal energy when water vapour is admitted to the zeolite molecular sieve. In this specification the words "battery" is used accordingly.
  • discharge herein describes the action of driving water vapour from the zeolite molecular sieve in the container
  • discharge herein describes the action of allowing water vapour into the zeolite molecular sieve creating heat by water vapour rejoining the zeolite structure and releasing heat exothermically.
  • zeolite molecular sieve herein describes a presentation of zeolite with pore sizes similar to the molecular size of a water molecule in which when water vapour is able to react with and be absorbed into the pores or be driven from the pores of the zeolite structure.
  • the rate at which water vapour enters the zeolite molecular sieve can be used to control the rate of heat generation and thus the rate of discharge.
  • heat is transferred from the device to the place at which it is to be used by a heat transfer fluid passing through ducts.
  • the ducts can be heated by the heat being released from the zeolite molecular sieve during discharge.
  • the heat transfer fluid can be liquid or gas. Water, however, is cheap and is suitable for most applications.
  • the thermal energy generated by the exothermic reaction during full discharge of the battery is only a little less than the thermal energy absorbed during charging, and the device is very efficient.
  • Thermal efficiency is improved even further by condensing the water vapour driven off from the zeolite molecular sieve during charging and using the latent heat released by condensation and also by using heat released from the device as it cools after charging, and before discharge starts.
  • Efficiency is improved further if the container is surrounded with a conventional thermal insulator, which can be spaced apart from the container itself to provide an additional insulating air gap.
  • the zeolite molecular sieve is supported in a metal matrix, comprising thermally conducting fins extending substantially though the zeolite molecular sieve, with spines extending laterally from the spines into the body of the zeolite molecular sieve to ensure excellent thermal connection between the source of heat and the zeolite molecular sieve.
  • a metal matrix comprising thermally conducting fins extending substantially though the zeolite molecular sieve, with spines extending laterally from the spines into the body of the zeolite molecular sieve to ensure excellent thermal connection between the source of heat and the zeolite molecular sieve.
  • zeolite matrix Such a structure is called a "zeolite matrix”. Aluminium is particularly suited for use at the spines and fins and for the container itself as it has good thermal conductivity and is light.
  • the container itself can be of modular construction using extruded aluminium sections.
  • electrical heating is used as the heat energy source it can be mains supplied, more economically. More economically, however, the electrical heating can come from a wind turbine or wave generator.
  • Solar heating from a solar panel is also a very economic form of heat, and the heat energy from such a source is very conveniently stored in the device of this invention by linking the panel to the device by a high thermal conductivity material.
  • the device When the device is part of a cooling system, for example, an air conditioning system, power can be drawn from solar energy or from more normal conventional sources. Such device is discharged by drawing water vapour from an evaporator which has a heat exchanger with circulating fluid being the part of a conventional air conditioning system which evaporates water vapour.
  • energy say, from a solar panel is used to heat the zeolite molecular sieve and drive off water vapour absorbed by the zeolite into a condenser.
  • a vacuum is created in the zeolite container which in turn draws water vapour from the evaporator, repeating the cycle cooling the circulating fluid in the air conditioning system.
  • the device provides a low energy air-conditioning system particularly for use in hot sunny climates, where the power consumption of conventional air conditioning systems is very high.
  • the invention can be used as part of a water purification system, for example a desalination plant.
  • the device can draw power from solar energy or from more normal conventional sources.
  • the device is discharged by drawing water vapour from an evaporator which is fed by impure water.
  • the battery is discharged and charging begins the water vapour driven out is pure and can be collected in a condenser for use.
  • Latent heat released from condensation, and heat released from the device while cooling and discharging can be recycled to the evaporator to improve efficiency.
  • Such heat can also be used in a de-aeration stage for de-aerating the impure water before it enters the evaporator.
  • a system of this kind can be used for emergency sterilization.
  • a number of devices according to the invention can be connected to the heat energy source to ensure constant operation, for example in a desalination plant.
  • the device can be heated inductively by a magnetic field rotating at the core of the battery. This is particularly useful in thermal storage applications and in water purification.
  • the rotatable magnetic field is coupled directly to an input shaft coupled to a wind turbine which can be used to charge the device when wind conditions are suitable.
  • the input shaft can be driven form other rotatable outputs
  • the output shafts of wave energy devices would be one possibility.
  • Figure IA shows a partial section through a device according to the invention forming a thermal storage battery
  • Figure IB is an end on view of the section shown in Figure IA;
  • Figure 2 shows schematically a thermal storage battery system comprising a number of thermal batteries of the kind shown in figure 1.
  • FIG. 3 shows a section through a thermal storage battery according to the invention in which the heat source is a solar panel.
  • Figure 4A shows a number of thermal storage batteries according to the invention mounted in an insulating container
  • Figure 4B is a plan view of the thermal storage batteries of figure 4A;
  • Figure 4C is a section on the line A-A' of figure 4B;
  • Figure 4D is a detail view of the area B in figure 4C;
  • Figure 5A shows a partial section of a device according to the invention similar to that of figures 3A and 3B but used as part of a cooling system;
  • Figure 5B is an end on view of the section of Figure 5A;
  • FIG. 6 is a schematic diagram of such a cooling system
  • Figure 7 is a schematic diagram illustrating the use of a device according to the invention as part of a desalination system
  • Figure 8 shows device according to the invention used in a desalination system and charged by a rotating magnetic field.
  • a device according to the invention used as a thermal storage battery comprises a cylindrical container 1 having an inner wall 2 made of extruded aluminium sections. The ends (not shown) of the cylinder are closed by aluminium caps. The container 1 is separated by a gap 3 from an insulating outer wall 4. The gap 3 is filled with insulating material such as rock wool.
  • An extruded aluminium central core 5 has a plurality of radial aluminium fins 6 extruding to the inner wall 2. Each fin 6 has a number of aluminium spines 7 extending the length of the cylinder and formed as arcs around the central core 5.
  • the region between the inner wall 2 and the central core 5 is filled with a zeolite forming a zeolite molecular sieve 8.
  • the zeolite known as X13 is particularly efficient in this application.
  • the configuration of the fins 6, spines 7 makes for good heat transfer to the central core 5 and the zeolite 8, the spines 7 forming a fine mesh to contact the zeolite molecular sieve 8. It will be seen that the combination of zeolite8, fins 6 and spines 7 forms a zeolite matrix.
  • the central core itself has a number of slots 9 on its periphery in which the fins 6 are mounted. Close to the surface of the core are a number of ducts 10 for water vapour.
  • the ducts 10 have slots 11 to the zeolite molecular sieve 8, through which water vapour may pass.
  • a series of heat transfer pipes 12 run the length of the central core 5.
  • water would often be used as the heat transfer medium.
  • the heat transfer pipes would connect to a hot water supply and/or a heat exchanger that is part of a central heating system. But there is no reason why other heat transfer media should not be used, including steam or air as part of the warm air supply in an air conditioning system.
  • an electrical heater 13 connected to a source of electricity.
  • the ducts 10 are connected through the end caps of the cylinder, on one side via a non-return valve to a condenser and on the other side to a low-pressure evaporator. Initially, the zeolite molecular sieve 8 is fully charged with water molecules.
  • the electric heater is connected to its supply. This heats the zeolite molecular sieve 8 forcing the chemically absorbed water in the zeolite out as water vapour, through the slots 11 and ducts 10 out of the cylinder. This water vapour passes through a non- return valve to a condenser (not shown). This charges the battery. After charging, water is passed through the heat transfer pipes 12, cooling the interior of the cylinder. Any water vapour remaining in the cylinder is reabsorbed into the zeolite molecular sieve 8, creating a vacuum. This vacuum draws low-pressure water vapour through the ducts 10 and slots 11 into the zeolite molecular sieve 8.
  • FIG 2 shows a schematic heating system that is more likely to be adopted in practice.
  • a plurality of thermal batteries 20 of the kind shown in figure 1 is shown.
  • the vapour duct 10 of each of the batteries 20 is connected to the combined condenser and evaporation unit 16, with low pressure vapour capable of being drawn from the evaporator, and vapour forced out of the cylinders being passed through a non-return valve to the condensing side of the unit.
  • the heat transfer pipes of each battery are connected through a common duct 17 to the system output. Electrical energy is passed through a control system 18 to be directed to the batteries being charged. At the same time charged batteries can be discharged to provide heat output to the duct 17.
  • Latent heat from the condensation of water vapour can be used for heating purposes.
  • This system is an economic solution to thermal energy. It may also be more reliable than existing systems over long periods of time.
  • conventional storage heaters which discharge as soon as they are warm
  • the battery would only need to be discharged when there is a need for thermal energy in contrast to conventional storage heaters, which discharge as soon as they are warm.
  • the input to such a system could be from a variety of sources, solar or a wind turbine driven heat operating device. With large enough storage cylinders, substantial amounts of thermal energy could be stored (up to 275 KW per cubic meter).
  • One option would be to convert the output to electricity. Such converting devices do exist, such as heat engines coupled to generators. Steam turbines and Stirling engines are particularly suitable.
  • a thermal storage battery 21 comprises a container 22 filled with a zeolite molecular sieve 23. Fins 24 extend from the wall of container 22 into a zeolite molecular sieve 23 to help transmit heat into and out of the zeolite molecular sieve.
  • a tube 25 runs within the container and through the container's end caps (not shown).
  • a slot 26 through the wall of the tube 25 allows passage of water vapour into and out of the zeolite molecular sieve 23 via the tube 25.
  • Ducts 27 thermally connected to the container allow the flow of a heat transfer medium. For many applications, water is perfectly satisfactory as the heat transfer medium.
  • Thermally coupled to the container is a thermal collector 28. In this example, it is a large surface planer collector.
  • the thermal collector has a thermally absorbing coating 29 which in its simplest for is matt black paint, but commercially available solar absorbing paints would be preferred.
  • the solar collector is further supported on the container by spars 30, which also provide the thermal coupling to the container.
  • the container 22, fins 24, ducts 25 and 27, collector 28 and spars 29 are manufactured in extruded aluminium. Aluminium has high thermal conductivity, is robust and easily fabricated, however, other high thermal conductivity materials such as copper could be used.
  • the container 22 is oval in cross section to allow for maximum transmission of heat from the panel 28 to the entire zeolite molecular sieve 23.
  • the assembly is mounted in an open topped box (not shown) which is made of insulating material, and the volume between the box and the assembly filled with conventional insulating material. In this configuration the solar panel is exposed to the sun beneath a solar glass plate closing the top of the box.
  • thermal storage batteries can be controlled such that some may be charging and others discharging at the same time, providing a continuous source of energy.
  • the devices can be charged at times when plenty of thermal energy is available and maintained in a charged condition until energy is needed.
  • a single thermal storage battery would have a solar collector 28 which is 200mm wide by 1000mm long. The speed of charging will vary depending on location and weather conditions.
  • Pipes connected to the ducts 25 to carrying water vapour should be sealed and evacuated of air. These pipes are connected to a small vessel, which would act as a condenser and evaporator of water vapour during use. Control of a panel to release its heat energy would be in the form of a simple solenoid valve between evaporator and the thermal storage battery, controlled by a straightforward end user clock / timer system to call for heat as in a typical heating system control.
  • the vapour is absorbed into the sieve, maintaining the low pressure until the molecular sieve can absorb no more vapour.
  • an exothermic reaction takes place within the molecular sieve, and heat energy is generated, approximately 275 watts per litre of molecular sieve of type X13 zeolite.
  • the rate of energy release is a function of volume of water vapour allowed into the container area and also the rate at which heat energy is taken away. If no heat energy is taken from the system the temperature of the sieve during discharge could rise above 200 0 C and reach an upper limit.
  • FIGS 4A to 4D illustrate a large thermal system storage battery system suitable for mounting as a panel on a roof.
  • a box 34 has mounted within it a plurality of individual thermal storage batteries 31 of the kind described in figure 3.
  • the thermal collectors 28 are visible mounted below a glass plate 33, which insulates the contents of the box.
  • Each of the batteries has water vapour ducts and ducts for heat transfer medium, water in this example, as in figures 3A and 3B.
  • the water vapour ducts are connected together and to a condenser and evaporator, now shown.
  • the heat transfer ducts are connected to a hot water circulating system, again not shown.
  • Control valves are mounted below a panel 32.
  • a 3m 2 panel of this kind could collect and store 12KWhs of thermal energy a day, and be available for use long after collection. Such a panel can provide the basis for space heating and hot water for a house.
  • a device 41 for absorption and subsequent release of energy comprises a container 42 within which is a zeolite molecular sieve 43. Fins 44 extend down into the zeolite molecular sieve 43. A water vapour duct 45 runs through the container with slots 46 connecting duct 45 to the zeolite molecular sieve 43. At the top of the container 42 a solar panel 48 is mounted with a solar energy absorbing surface 49 of matt black paint, or special solar absorbing paint. Spars 50 help support the solar panel on the container 42. Mounted below the container, but thermally connected thereto, are cooling fins 47.
  • FIG. 6 is a schematic diagram of a cooling system using the device of figure 5.
  • the water vapour duct 45 is connected to a condenser 51 having external cooling fins. Water vapour leaving the battery 41 condenses in the condenser 51.
  • the condenser 51 is connected to an evaporator 53 via a capillary tube 52. Within the evaporator 53 is a heat exchanger 56 through which fluid flows. The fluid can be water or another heat transfer fluid. Warm fluid is pumped through pipe 54 into the heat exchanger 56, wherein it gives up its heat to evaporate low pressure water arriving through the capillary 52 into evaporator 53.
  • the container 42, fins 44 and 47, solar collector 48 and spars 50 are all made from extruded aluminium, which has good thermal conductivity. Heat falling on the solar collector 48 is thus transmitted easily to the zeolite molecular sieve 43.
  • the water vapour thus created enters the zeolite molecular sieve 43 via duct 45 and slots 46 and combines with the zeolite, releasing heat in the process as a result of the exothermic reaction that occurs.
  • This heat is conducted from the thermal storage battery, through the walls of the container and fins 47.
  • this device is shown with a solar collector for heating purposes, it is also possible to construct it with an electrical heating system as in figure 1; the solar panel should thus be seen as just one example of a heat source. Nevertheless, the advantages of the solar heating system are particularly obvious in countries where cooling systems, such as in air conditioners, are most used. The more solar energy that is available the more effectively will the device work.
  • duct 45 is shown as two separate ducts in figure 6, in reality the evaporator and condenser can be connected through the opposite ends of container 42 through end covers, or a single entry point over to container 42 is provided with a solenoid control valve controlling whether duct 45 is connected to the condenser 51 or the evaporator 53.
  • FIG 7 a device for absorption and subsequent release according to the invention similar to that shown in figures 3A and 3B is used as part of a desalination system.
  • Water vapour duct 25 of the battery 21 is connected through a solenoid switch valve 71 to ducts 67 and 68.
  • Duct 67 is the water vapour outlet of an evaporator 64
  • duct 68 is the water vapour inlet of a condenser 66.
  • the heat transfer fluid duct 27 of the thermal storage battery is connected to the heat exchanger 72 of the evaporator 66.
  • Sea water (or other water needing purification) is admitted through a pipe 61 to a de- aerator holding vessel 62.
  • the air outlet low down the holding vessel connects through a further pipe 63 to the evaporator 64. Sea water can thus be drawn from the holding vessel 62 to the evaporator 64.
  • Water vapour that is condensed in the condenser 66 can be drained through pipe 69.
  • a conventional heat exchange system 70 connects the heat exchanger 73 of the condenser 66 with the heat exchanger 72, to the evaporator 64. Waste heat from the condenser 66 can then be used to assist evaporation in the evaporator.
  • the upper part of the evaporator is connected to a pump 65, to create low pressure in the evaporator.
  • sea water enters the holding vessel 62 which acts as a de- aerator. This water is at ambient temperature and pressure.
  • the de-aeration can be achieved by raising the water's temperature or reducing the pressure. Most economically this can be done by using heat from the condenser 66 or from the battery 21 by connecting the heat transfer fluid duct 27 through the holding vessel 62 (this connection is not shown).
  • the de-aerated salt water is fed at a controlled rate through pipe 63 to the evaporator 64. As some water is boiled in the evaporator 64, salt and/or other impurities will build up and concentrate in the remaining water, which can be drained away from time to time through duct 74 at the bottom of the evaporator.
  • the system is primed by reducing pressure in the evaporator using pump 65. As a result water in the condenser will boil. For maximum efficiency the heat to assist this can be supplied from the condenser heat exchanger 73 and/or from the heat exchange fluid in duct 27.
  • a water purification system of this kind can be used for emergency sterilization. If wished water can be prevented from entering the evaporator until it had reached a suitable temperature at which bacteria and viruses would have been substantially killed or deactivated. This can be achieved through the preheating of water in the de-aerator holding vessel 62 before it enters the evaporator 64, with a flow control valve (not shown) in pipe 63 which only opens when the required temperature had been reached, preventing unsterilized water from getting into the evaporator.
  • a flow control valve could be constructed in many different ways, but one possibility would be from single piece of memory metal another is to use a conventional bimetal combination that will change shape with temperature. This modification is not essential for safe operation as only water vapour is able to travel to the zeolite and the condenser and the temperature that the zeolite reaches in operation would be more than enough to destroy any bacteria and viruses that reached the container.
  • a number of batteries each connected to the evaporator and condenser can be used be used, the individual batteries will be at different stages of the cycle to ensure continuous operation,
  • the desalination system can also be used with electrically heated thermal storage batteries of the kind shown in figure 1.
  • FIG. 8 illustrates a particularly novel approach to providing a heat source in a battery of the kind described in the previous examples.
  • a battery 81 is shown having a cylindrical container 82 with end caps (not shown).
  • a hollow core 85 is disposed around the central axis of the cylinder.
  • a shaft (not shown) is free to rotate. The shaft would be driven by the output shaft of a wind turbine, or a wave energy device.
  • permanent magnets 84 are disposed around the inside of the hollow core and parallel to its axis.
  • An insulating layer 89 covers the inside of the core 85 thermally isolating the shaft on the shaft.
  • Fins 86 extend radially from the core 85 to the wall of the container 82, with spines 87 extending laterally from the fins forming arcs around the axis of the container.
  • the volume between the hollow core, the container wall, and the end caps is filled with a zeolite molecular sieve 88.
  • the combination of zeolite molecular sieve 88, fins 86 and spines 87 make a zeolite matrix.
  • the container 82, fins 86, and spines 87 are all constructed of a good electrically conducting material. Extruded aluminium was used in this case.
  • Ducts and openings to transport water vapour to and from the zeolite molecular sieve have not been shown in figure 8 for clarity, but they are formed at the inner wall of the container, in a similar way to ducts 45 and slots 46 in Figures 5 and 5B. If this device is being used as thermal storage battery, the duct for heat transfer fluid would also be placed along the container wall in a similar way to the ducts 27 in Figures 3 A and 3B. The battery is externally insulated.
  • the battery In operation the battery is charged by coupling the shaft to a rotary power source.
  • the output shaft of a wind turbine is particularly appropriate.
  • the magnetic field created by the permanent magnets rotates though the core 85, fins 86 and spines 87, heating these parts by induction. With good insulation this heat builds causing water vapour to be driven from the zeolite as described with the other examples. This water can be condensed in a condenser.
  • the magnetic field stops rotating the battery cools and any remaining water vapour is reabsorbed into the zeolite creating a vacuum as before. Water vapour is then allowed into the zeolite molecular sieve to recombine with the zeolite and create heat by an exothermal reaction as described before.
  • the battery shown in figure 8 is particularly suitable for use in the water purification system of Figure 7. With the source of water vapour being the evaporator 64 of Figure 7 and with expelled water vapour going to the condenser 66.
  • Performance of the battery shown in Figure 8 can be improved further by embedding annular steel or iron rings in the body of the battery, coaxial with the core 85.
  • several devices of the kind shown in figure 8 will be needed, each at different stages of the charge/ discharge cycle. This can be achieved, either by using a number of devices operating from separate inputs, or operating a number of devices from a single shaft coupled to, for example, a wind turbine, by mounting the permanent magnets on a slip ring around the shaft, and coupling or decoupling the slip rings from the shaft as desired.

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Abstract

La présente invention se rapporte à un procédé et à un appareil servant à absorber de la chaleur et à libérer ultérieurement de la chaleur. Dans cet appareil, un tamis moléculaire (8) en zéolite est chauffé dans un récipient afin de chasser la vapeur d'eau. On laisse le tamis moléculaire en zéolite refroidir, créant un vide dans le récipient par le biais de la réabsorption dans le tamis moléculaire en zéolite de toute vapeur d'eau restant dans le récipient. De la vapeur d'eau supplémentaire est introduite dans le tamis moléculaire en zéolite pour dégager de la chaleur lorsque la vapeur d'eau se combine avec la zéolite. L'invention comporte un certain nombre d'applications comprenant un dispositif de stockage de chaleur, en tant que partie d'un système de refroidissement et d'un système de purification et/ou de dessalement d'eau. Le chauffage est obtenu par un certain nombre de moyens de chauffe, électriques, (13) solaires et par induction, décrits.
EP09785239A 2008-06-16 2009-06-16 Dispositifs et systèmes d'absorption et de libération d'énergie Withdrawn EP2313710A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0810982.9A GB0810982D0 (en) 2008-06-16 2008-06-16 Energy absorption and release devices and systems
PCT/GB2009/050683 WO2010004302A1 (fr) 2008-06-16 2009-06-16 Dispositifs et systèmes d'absorption et de libération d'énergie

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EP2313710A1 true EP2313710A1 (fr) 2011-04-27

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GB0921857D0 (en) 2009-12-15 2010-01-27 Carbon Zero Ltd Thermal Collection and Storage Systems
EP3299759A1 (fr) * 2016-09-21 2018-03-28 Nederlandse Organisatie voor toegepast- natuurwetenschappelijk onderzoek TNO Système et procédé de stockage thermochimique d'énergie
GB2559779B (en) * 2017-02-17 2021-10-13 Anthony Richardson Nicholas System and method of supplying steam
CN115468330B (zh) * 2022-09-22 2023-05-23 哈尔滨商业大学 一种磁吸转换型吸附式制冷/热泵空气调节系统

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US5237827A (en) * 1974-11-04 1993-08-24 Tchernev Dimiter I Apparatus for cyclic production of thermal energy by plural adsorption stations and methods
US4584842A (en) * 1976-08-02 1986-04-29 Tchernev Dimiter I Solar refrigeration
BR8506713A (pt) * 1984-05-01 1986-09-23 Dimiter I Tchernev Bomba termica energizada por fonte termica de baixo indice
DE3610332A1 (de) * 1985-03-30 1986-10-09 Kabushiki Kaisha Toshiba, Kawasaki, Kanagawa Regenerativheizgeraet
US5813248A (en) * 1995-11-01 1998-09-29 Zornes; David A. Balanced adsorbent refrigerator
DE19645475B4 (de) * 1996-11-05 2006-05-18 Ludwig, Jürgen, Dipl.-Ing. Periodisch arbeitende Adsorptionswärmepumpe, Adsorptionskältemaschine oder Adsorptionswärmetransformator

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GB0810982D0 (en) 2008-07-23

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