Patent Application
20170248377
The present invention relates to a storage system of refrigeration or thermal energy through the use of phase change materials (PCM), in particular for air conditioning or heating of domestic, working, shopping, etc. environments.
More particularly, the invention relates to a system that allows to maximize the transfer of refrigeration or thermal energy between a material of the PCM type and a refrigeration or heating fluid both during storage and release phases of energy from tank storage system, thus increasing the potential applications of cold or heat storage systems, and to optimize the period of withdrawal of energy from the supply main or of use of self-produced energy.
It is known how, in industrial applications, cold storage is carried out by means of ice-water tanks which store frigories by the process of solidification of the water and release the same by the process of liquefaction of the ice. Such systems are integrated with non-standard refrigerators, wherein a solution of water and glycol circulates at a temperature lower than 0° C., in order to cool the water of the primary circuit of the refrigerating machine and thus allowing the solidification of the water with in the storage tank. Working temperatures lower than 0° C., however, limit the use of said ice-water systems in non-industrial field, particularly for conditioning environments. Also, the use of non-standard refrigerators results in a reduction of the Coefficient of Performance (COP) and an increase in the cost of the refrigerating machine.
It is also known, to overcome the limitations of the technologies currently available in the industrial field, the use of materials, such as special eutectic alloys, which are known as phase change materials (PCM), which possess a constant phase transition temperature, higher than 0° C. and depending on the composition of the alloy. In the literature, many materials of the PCM type are known, each one characterized by a certain degree of toxicity, flammability and supercooling, by its own phase transition temperature and by a low average solid phase thermal conductivity.
In conventional heat exchange systems, such as for example tube bundle and shell exchangers (shell and tube) wherein the fluid of the PCM type is stored within the shell and the exchange fluid is sent into the tubes, formation, inside the storage system tank, of PCM type fluid solid phase directly on the exchange surface involves a transfer of refrigeration energy by conduction rather than by convection, with consequent slow charging times of the tank.
The two proposed solutions currently available to obviate the decrease of the tank conductivity of PCM type materials during the energy storage are micro-encapsulation of liquid PCM type material and the use of phase change slurries (Phase Change Slurry, PCS). Microencapsulation of liquid PCM material allows to improve the thermal exchange introducing PCM material within suitably shaped capsules, immersed within the volume of primary water within the storage tank, so as to increase the contact surface between the PCM material and water. However, this solution presents several problems, such as not adequate charging times, high costs and excessively bulky systems, due to the reduced volumetric density of energy storage tank, due to packing problems and to the presence of the capsules.
Instead PCS, thanks to the dispersion of droplets or micro-capsules of PCM-type material within a liquid carrier, allow improving the kinetics of energy transfer between the refrigerating PCM type material and liquid carrier and ensuring an additional storage component constituted by the sensible heat of the continuous phase. However, PCS have application problems due to the high viscosity of the fluid to be handled and the reduced energy density storage.
Cold storage systems using PCM type materials currently available have, therefore, two main problems, which limit their potential applications: a charging/discharging power of the systems not adequate and volumetric density storage not satisfactory.
Even the hot storage systems currently available, which employ paraffin, present the same problems of cold storage systems using above said PCM type materials, i.e. a charging/discharging thermal power of the systems not adequate and volumetric density storage not satisfactory.
In the light of the above, the Applicants have realized a refrigeration or thermal energy storage system employing phase change materials (PCM) able to overcome the mentioned above drawbacks.
These results are obtained, according to the present invention, by refrigeration or thermal energy storage system employing PCM-type materials maximizing the transfer of refrigeration or thermal energy, ensuring an intimate contact between a PCM type fluid and a fluid stream flowing within a secondary closed circuit and that is cooled or heated by a heat exchanger.
U.S. Pat. No. 2,996,894 is the most relevant prior art document known to the Applicants with respect to the solution subject of the present patent application.
It is therefore specific object of the present invention a refrigeration, or thermal, energy storage system for storing refrigeration, or thermal, energy to be released when required by users, comprising a body, closed and insulated, said body being configured to contain two fluids within its volume, respectively a Phase Change Material (PCM) type fluid and a secondary fluid, said two fluids being immiscible each other and having different density, so as to be stratified within the volume of said body; withdrawal means configured to draw said secondary fluid from said body, and to convey the same inside a heat exchanger, said heat exchanger being configured to exchange frigories, or calories, with said secondary fluid; and distribution means configured to draw said secondary fluid from said heat exchanger, and to distribute, within said body, said secondary fluid into said PCM type fluid, so as that said secondary fluid exchanges with said PCM type fluid frigories, or calories, absorbed in said heat exchanger, said secondary fluid having a solidification temperature substantially lower than that of said PCM type fluid, said heat exchanger being housed inside said body, and being exchange frigories, or calories, between said secondary fluid and a primary fluid, said heat exchanger comprising a first pipe, connected at its ends respectively to said withdrawal means and to said distribution means, for the circulation of said secondary fluid, and a second pipe, concentric with respect to said first pipe, configured to be connected to a circuit external to said body, for the circulation of said primary fluid.
Preferably, said withdrawal means are placed at least partially in the upper, or lower, part of said body, depending on the density value of said secondary fluid, and in that said distribution means are placed at least partially in the upper, or lower, part of said body, in an opposite manner to the position of said withdrawal means.
Still according to the invention, said volume of said body comprises separation means to prevent the inlet of said PCM type fluid into said withdrawal means.
Preferably, according to the invention, said separation means comprise a grid, or a membrane, impermeable to said PCM type fluid and placed so as that only said secondary fluid is substantially present in correspondence of said withdrawal means.
Preferably, according to the invention, said separation means comprise an “S” path to prevent the inlet of said PCM type fluid into said withdrawal means.
Still, according to the invention, said withdrawal means comprises a pump to convey said secondary fluid into said heat exchanger.
Preferably, according to the invention, said distribution means comprise shower nozzles and/or nebulizers and/or hydraulic vortexes to distribute, inside said body, said secondary fluid into said PCM type fluid.
Preferably, according to the invention, said secondary fluid is present within said body with a percentage in volume preferably between 5% and 50%.
Preferably, according to the invention, said secondary fluid has a density greater than that of said PCM type fluid.
Preferably, according to the invention, said secondary fluid is water.
Furthermore, according to the invention, a storage system to store refrigeration, or thermal, energy to be released when required, comprising a refrigeration, or thermal, energy storage system as described in the above; a refrigeration, or thermal, unit connected to said heat exchanger, and configured to release frigories, or calories, to a primary fluid when said system is in a refrigeration, or thermal, energy storage configuration, so as that said frigories, o calories, are later released by said primary fluid to said secondary fluid in said heat exchanger, and further later exchanged between said secondary fluid and said PCM type fluid inside said body; users, connected to said heat exchanger so as that, when said system is in a energy release configuration, said PCM type fluid exchanges frigories, or calories, with said secondary fluid inside said body, and later said secondary fluid releases said frigories, or calories, to said primary fluid in said heat exchanger, and further later said primary fluid releases said frigories, or calories, to said users; and a valves and pumps system for the circulation of said primary fluid so as that said system can pass from a refrigeration, or thermal, energy storage configuration to a energy release configuration, and vice versa.
Still according to the invention, said refrigeration, or thermal, unit is connected to said heat exchanger and to said users, so as that, said refrigeration, or thermal, unit exchanges frigories, or calories, with said primary fluid, and later said primary fluid exchanges frigories, or calories, with said secondary fluid in said heat exchanger and with said users, and in that said valves and pumps system allows to operate in a refrigeration, or thermal, energy storage mode releasing frigories, or calories, to said secondary fluid in said heat exchanger or to said users or to both of them at the same time, and in a refrigeration, or thermal, energy release mode with release of frigories, or calories, to said primary fluid by said secondary fluid in said heat exchanger or by part of said refrigeration, or thermal, unit or by both of them at the same time.
The present invention will be now described for illustrative, but not limitative purposes, with particular reference to the drawings of the enclosed figures, wherein:
Making reference now to
Said storage system 1 comprises a tank 2 for storage of refrigeration energy, a secondary circuit 3 and a system of showers or nebulizers 4, contained within the volume of the tank 2.
Said tank 2 can be any insulated, closed, body of appropriate size to kWh to be stored and configured to contain within its volume a PCM type fluid and a secondary fluid, immiscible each other and having different density. In particular, said body is preferably cylindrical.
Physical characteristics of said fluids determine the layering of the same within the volume of the storage tank 2, with the consequent possibility of withdrawing the secondary fluid, depending on the density value of the latter, from the top or the bottom of tank 2.
In the following, the description of the storage system will be made with reference to a secondary fluid having a density greater than that of the type PCM fluid, but it should be understood that the elements distinguishing system 1 does not vary according to the type of secondary fluid employed.
In the embodiment shown, said PCM type fluid has a solidification temperature preferably equal to 5° C., while said secondary fluid, present within said tank 2 with a volume rate preferably between 5% and 50%, has a solidification temperature lower than that of said PCM type fluid.
Said secondary circuit 3 comprises a pump 5 for displacement of secondary fluid from inside the tank 2 towards a heat exchanger 6 and from this to the system showers or nebulizers 4.
Said heat exchanger 6 is preferably comprised of a system of double concentric tubes circular coils and is housed within said tank 2 and immersed within the PCM type fluid volume. In the embodiment shown, said coil system is comprised by two identical coils connected together to operate in parallel.
Secondary fluid circulates within inner tube 7 of said heat exchanger 6, while a primary fluid circulates in counter current within the outer tube 8, entering and exiting in and from a refrigeration system (not shown in these figures) by means of a primary circuit 9. it is evident that the two fluids may also circulate in co-current.
Said inner tube 7 of said heat exchanger 6 is connected, through a system of pipes 10, to a pipe union 11, the latter being connected, through the secondary circuit 3, to a pipe union 12 of the tank 2; said means 12, 3, 11 and 10 allow the flow of the secondary fluid from the storage tank 2 to the heat exchanger 6. Said inner tube 7 is also connected, through a system of pipes 13, to a pipe union 14, the latter being connected, by means of a circuit 15, to a pipe union 16, connected, through a system of pipes 17, to the showers or nebulizers system 4; said means 13, 14, 15, 16 and 17 allow the flow of the secondary fluid from heat exchanger 6 to the showers or nebulizers system 4.
Said outer pipe 8 is connected, through a system of pipes 18, to a pipe union 19, and, through a system of pipes 20, to a pipe union 21, connected to said pipe union 19 through the primary circuit 9; said means 9, 18, 19, 21 and 20 allow the flow of the primary fluid in, and from, the heat exchanger 6.
The showers or nebulizers system 4 is present in the upper part of the storage tank 2, for uniform distribution on the surface, and then in the PCM type fluid volume, of droplets of secondary fluid coming from the heat exchanger 6.
Separation means 22 are housed within the volume of the tank 2, to prevent the release of the type PCM fluid in the secondary circuit 3. Particularly, said separation means comprise a grid, disposed in such a way that only said secondary fluid is substantially present in correspondence with the nozzle 12.
Said heat exchanger 6, said showers or nebulizers system 4 and said separation means 22 are supported by a beam system 23.
Operation of the storage system 1 according to the present invention provides for the withdrawal of the secondary fluid from the bottom of the tank 2 and the circulation of said fluid, thanks to the pump 5, within the secondary circuit 3, in the heat exchanger 6 and in the circuit 15, until reaching the system showers or nebulizers system 4.
Secondary fluid absorbs frigories within the heat exchanger 6, during the storage of refrigerating energy within tank 2, and releases frigories during the release phase of refrigerating energy of tank 2, from, and to, the primary fluid circulating within said heat exchanger heat 6. Primary fluid is cooled by a refrigeration system during the storage of refrigeration energy within tank 2, while during the release phase of refrigerating energy from tank 2, before being sent to a final user, it is cooled by the current of the secondary fluid.
Secondary fluid, coming from heat exchanger 6, is introduced within the tank 2 through the showers or nebulizers system 4, which ensures a uniform distribution of the droplets of the secondary fluid in the PCM type fluid volume. The droplets of secondary fluid evenly run down along the PCM type fluid head optimally transferring refrigeration energy from secondary fluid to the PCM type fluid during the storage of refrigerating energy in tank 2 and by the PCM type fluid to the secondary fluid during the release phase of refrigerating energy from tank 2, so as to obtain, respectively, the solidification of the liquid PCM type fluid and the fusion of the solid PCM type fluid. Also, since the PCM type fluid solidifies creating crystals that are dispersed within the liquid volume, and in intimate contact with the droplets of the secondary fluid, in order to improve the mixing and make sure that the PCM type fluid solidifies by means of a high number of small crystals, secondary fluid can be introduced within tank 2 by means of spays having a suitable speed.
Solidification of PCM type fluid during the storage of refrigerating energy in tank 2, thus permits storage, in storage tank 2, of refrigerating energy which is then released during the release phase of refrigerating energy from tank 2, through the fusion of the solid PCM type fluid.
By the solution proposed according to the present invention it is maximized the energy transfer between the refrigeration fluid and the secondary PCM type fluid. The direct contact between said fluids, their different physical characteristics and the showers or nebulizers system guarantee, in fact, an excellent heat exchange efficiency and a rapid transfer of refrigerating energy, with consequent increase of the refrigeration capacity both during the phase of storage of refrigerating energy and during the release phase of refrigerating energy.
Particularly, showers or nebulizers system, by generating droplets of secondary fluid that evenly run down the PCM type fluid head, allows increasing the contact surface for heat exchange and, due to viscous forces, ensures handling the type PCM fluid, improving energy transportation coefficients.
Being then the type PCM fluid confined within the tank, it is prevented a movement of the type PCM fluid, under phase change conditions, especially during energy storage, that could generate operational problems such as blockage of pipelines or rupture the pumps.
Furthermore, the reduced time of energy storage and release from storage tank allow the use of the storage system according to the present invention to optimize the energy withdrawal period from the main supply or of use of self-produced energy.
Another embodiment of the present invention provides the application of coatings on the inner surface of the pipes in which circulates the secondary fluid, avoiding the adhesion of the solid PCM type fluid.
According to a further embodiment of the present invention, the storage tank 2 can have cubic shape, conical shape, frustum-conical shape, parallelepiped shape, etc. and/or composite shape obtained by the union of one or more of the mentioned above shapes. According to another embodiment of the present invention, structures having a rough surface, such as filaments, grids or nets, immersed within the PCM type fluid volume, in order to promote and manage the formation of first PCM type fluid crystals during storage of refrigeration energy.
A further embodiment of the present invention involves the use of ultrasound systems, or similar systems, in order to facilitate the formation of first PCM type fluid crystals during the storage of refrigeration energy by tank 2 and thus reduce the eventual supercooling effect of PCM type fluid.
Another embodiment of the present invention involves the use of only the PCM type fluids and of the primary fluid, thereby avoiding the use of a secondary circuit. In this configuration, it is the primary fluid which, descending through the PCM type fluid head, releases, during the storage phase, and absorbs, during the release phase, the refrigerating energy.
According to a further embodiment of the present invention, the heat exchanger 6 may be located outside the storage tank 2, in order to increase the PCM type fluid volume the that can be contained within the tank 2, and/or different technologies may be used compared to the double concentric pipes coils system, such as rube bundle exchanger, plate exchangers, horizontal or vertical exchangers, shirt exchangers.
Another embodiment of the present invention provides the use of separation means different from the grid, such as a selective membrane to only the secondary fluid, placed on the surface or within the secondary fluid volume.
According to another embodiment of the present invention (shown in
The presence of said devices 24 can ensure an additional level of separation, avoiding that the particles of solid PCM type fluid deposited on the bottom occlude the suction duct 25.
Another embodiment of the present invention provides the use of movable, continuous and discrete showers or nebulizers systems.
Referring now to
In the following, the description of the circuit 29 will be made with reference to a heat exchanger 6 in which the primary fluid and the secondary fluid circulate in counter current, but it should be understood that the elements distinguishing the circuit does not vary if the two fluids circulate in co-current.
Said valve 32 allows, during the storage of refrigerating energy, the flow of the primary fluid, cooled by the refrigerator group 30, in the heat exchanger 6, while, during the release phase of refrigerating energy, allows the flow of the primary fluid, cooled by the secondary fluid circulating in the heat exchanger 6, towards the user 31.
If during the storage of refrigerating energy it is provided the transfer of frigories from the primary fluid either to the user 31 and to the secondary fluid, the mixing valve 33 allows the mixing of the primary fluid coming from the heat exchanger 6 with the primary fluid coming 31 from the user, by sending the mixed fluids to the intake of pump 34 and then in the refrigerator group 30. If, instead, during the storage of refrigerating energy it is provided only the transfer of refrigeration from the cooled primary fluid to the secondary fluid, said mixing valve 33 allows only the circulation of the primary fluid coming from the heat exchanger 6 to the intake of pump 34 and then in the refrigerator group 30.
Moreover, during the release phase of refrigerating energy, said valve 33 allows only the circulation of the primary fluid coming from the user 31 to the intake of the pump 34.
Said diverting valve 35 enables, during the storage of refrigerating energy, the flow of the primary fluid leaving the heat exchanger 6 through the valve 33 and then through the pump 34, toward the refrigeration group 30, while, during the phase of release of refrigerating energy, allows the flow of the primary fluid coming from the user 31 through the valve 33, and then through the pump 34, toward the refrigeration group 30 and/or to the heat exchanger 6.
The operation of the circuit 29 according to the present invention provides that, during the storage of refrigerating energy, the primary fluid cooled by the refrigeration group 30 can refrigerate the secondary fluid circulating in the heat exchanger 6 and/or provide the refrigeration power required by the user 31. However, during the release phase of refrigerating energy, the refrigerating power required by the user 31 can be provided by the primary fluid cooled by the refrigeration unit 30 and/or the primary fluid cooled by the secondary fluid circulating in the heat exchanger 6.
Therefore, the integration proposed according to the present invention of the cold storage system with a refrigeration system and a user allows to optimize the withdrawal period of the energy from the mains, reducing load peaks (peak shaving), or the use of self-produced energy.
In fact, frigories, or part of frigories, required by the user during the peak hours may be supplied from the cold storage tank, previously loaded during the non-peak time period, with a consequent reduction of the peak power and increase the refrigerating machines COP. Moreover, the presence of the cold storage tank in the circuit 29, operating to support the refrigerating machine, allows to reduce the power of the latter, with a consequent reduction of production costs, and of the price, of the refrigerating machine. By the application of a suitable management system of the energy flows, it is possible to operate the refrigerating machine at constant, or nearly constant, power, and at the optimum operation point (greater COP), by providing the peaks of refrigeration energy required by the user to the storage system.
Making reference to
Particularly, keeping closed valves 40 and 41 and opened valves 43 and 42, an operation of energy storage in parallel is obtained, which can be managed by modulating the opening of valves 38 and 39.
Keeping instead closed valves 39 and 42 and opened valves 43 and 40, an operation of energy release in parallel is obtained, which can be managed by modulating the opening of valves 38 and 41.
Keeping closed valves 38, 41 and 42 and opened valves 39, 40 and 43, an operation of energy storage in series is obtained, while keeping closed valves 39, 40 and 43 and opened valves 38, 41 and 42, an operation of energy release in series is obtained. In configurations in series, the primary fluid undergoes progressive thermal jumps, passing from the refrigeration group 30 to the heat exchanger 6 to the user 31, and vice versa.
The present invention has been described for illustrative but not limitative purposes, according to its preferred embodiments, but it is to be understood that variations and/or modifications may be made by those skilled in the art without departing from the relative scope of protection, as defined by the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| RM2014A000500 | Sep 2014 | IT | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IT2015/000209 | 9/2/2015 | WO | 00 |
