LATENT HEAT ACCUMULATOR, MANUFACTURING PROCESS AND USES THEREOF

Abstract: The invention relates to a latent heat accumulator form­ ed of a plurality of sealed cells (c) of small dimensions, filled with a chemical compound having a high latent melting heat. The cells are formed from a plastic thermoformable material, with high thermal conductivity and gasproof as well as steamproof. The cells are produced sealed, so as to prevent any outlet of the chemical compound or of its va­ pours. The heat is stored under form of latent heat and the melting temperature of the chemical compound is selected in function of the average temperature of the heat source being utilized.

Description: "LATENT EAT ACCUMULATOR, NUF4ACTURING PROCESS AND USES OF11 The present invention relates to a heat accumulator and, in particular, to a heat accumulator apt to store considerable amounts of heat at a selected temperature. The problem of making use of the heat available at low temperatures (for instance, at roon temperature or a fe@ tens of Oc higher) has always been difficult to solve. This not so much for lacy; of possible utilization of the heat at this temperature (it is in fact sufficient to think of the' heating of environments, or of the production of hot ater for sanitary use), but rather oozing to the difficulty of accumulating said heat during the periods and in the places there it. is produced, so as to then be able to restore it hen and there necessary. I.t is well shown, in fact, that the residual heat of a large number of industrial processes constitutes, in most cases, a processing "rejection" which has to be eliminated in the air or in water, with consequent heat pollution phenomena. The utilization of this heat for the heating of rooms or of water is often neither possible nor economically convenient, due to the difficulty of conciliating the requirements of consumption and those of heat production and thus, as a matter of fact, due to the unavailability of a satisfactory heat storage system. Even in plants which make use of solar energy - to which the invention specifically, though not exclusively, refers - the fundamental problem, still to be solved, is that concerning the storage of the heat absorbed by the collecting surfaces and not immediately used up. For this purpose, one simply uses at present large insulated reservoirs connected to the circuit of the worldng fluid (generally consisting of ater) and filled by the sane. This system, however, as :ell as talking up considerable space, is usually apt to satisfy only the requirements of storage connected to the day-and-night period, for wllat concerns the production of hot water for sanitary use. Whereas, the problem of producing an accumulator, allowing to store during the summer period an amount of heat such as to enable hot tauter to be delivered during the winter period without resorting to any other sources of energy, still has to be solved, unless one t ere to use reservoirs having such dimensions and characteristics of insulation, as to result extremely costly. Even more so, on account of- the foregoing, it has been impossible up-to-date to make use of solar energy for heating environments during the -nter season. In fact, the solutions proposed - all on an eXperimental level - require appropriately conceived structures, having such costs and structural characteristics as to make it practically unthinlrable for them to be adopted in the normal building industry. The dralfbacks evidenced by the current heat storage devices, namely the incapability to accumulate considerable amounts of heat in a limited- space, are substantially due to the fact that heat is stored therein under form of specific heat. This latter in fact, is given by the product of the heat storage fluid mass multiplied by its specific heat and by the difference in temperature between the heat storage fluid and the enviromment. Consequently, the only variable on which it is normally possible to operate is the heat storage fluid mass, in that the temperature difference is imposed - seen that, as stated, loNr temperature plants are involved - and it is generally rather low (from a fe:: C up to a few tens of CC), ;hile the specific heat is anyhow very low for all the fluids of practical interest (it in fact has its highest value for water ;ith I keal/dn3). In order to overcome these drawbacks, it has been thought to adopt storage systems which store the heat under form of latent heat (in particular, melting heat or heat of crystallization), and not under form of specific heat. The advantages of this choice are evident. The latent heats per unit of volume are in fact far hitler than the corresponding specific heats. r'urthermore, they allor to transfer the heat at a constant temperature, already knosn at the planning stage. The latent heat storage systems, which have so far found some practical application, are confined to the field of temperatures exceeding 900 CIC (for instance, in the heat accumulators adopted in the solar concentration systems, especially in the space field). Various attempts have also been made to obtain heat accumulators using the latent heat of chemical substances having a lower melting temperature (for instance, Glauber salt zVith 32 .40C melting point). In fact, these accumulators appear to be particularly suited for use in the solar plants, wherein no concentration of sun radiations is carried out. Nevertheless, the chemical compounds having a high latent melting heat at these temperatures, combined ith an acceptable cost, evidence features of evaporation and/or. chemical unstability, which alter their physical characteristics already after only 30 or 40 melting and subsequent solidification cycles; they are therefore practically useless for the above mentioned purposes. In consideration of the above, these products have so far found no practical application, in spite of the remaricable advantages which they could on the other hand provide. It will be noted that, so far, only the case of latent melting heat has been intentionally mentioned, as the latent heat of vaporization cannot be conveniently utilized owing to the ide volumetric variations between the liquid phase and the gaseous phase. The object of the present invention is to overcome the aforespecified drawbacks, which have so far strongly limited the utilization of heat sources at low temperature, by providing a latent heat accumulator apt to store into a limited space considerable quantities of heat at a predetermined temperature, and in which the physical characteristics of the substance subject to cyclic changes of state are substantially free from phenomena of decay in the long run, independently of the number of cycles. Another object of the present invention is to indicate a process for the production of the aforespecified heat accumulator. The aforementioned objects are obtained, according to the present invention, by means of a latent heat acciirnulator of the type utilizing a substance .ith a high latent melting heat per unit of volume and -.ith a high thermal conductivity, characterized in that said substance is enclosed in a plurality of sealed cells formed of a material -ith high thermal conductivity and each having dimensions of the order of magnitude of centimeters, and in that said substance has a melting temperature included between OoC and 100 C. According to a main characteristic of the invention, said substance is a chemical compound included in the group consisting of hydrate salts and, in particular, hydrate phosphates, sulphates an4 sulphites, or else in the group constituted by the paraffines. The use of the accumulator according to the present invention becomes particularly convenient, simple and quick, if the accumulator itself -is manufactured according to a preferred process comprising the following stages: - forming a plurality of small cavities into at least one sheet of a thermoformable plastic material; - filling said cavities tith said substance having a high latent melting heat, at the fluid state; - heat sealing said cavities, under partial vacuum, so as to form a plurality of sealed cells, filled sith said substance and practically having no air-locks. The invention ;-ill anyho be described in further detail, sith reference to some preferred embodiments thereof, shorn in the accompanying drawings, in which: Fig. 1 is a diagraseatic vietf showing a machine for the continuous production of the sealed cells forming heat accumulator according to the present invention; Fig. 2 illustrates a method for hanging chains of cells inside a heat storage reservoir (not shown); Fig. 3 shows a single cell as used in mixing with concrete and the like; Fig. 4 schematically shows a concrete slab incorporating a plurality of cells identical to that illustrated in figure 3; ; Fig. 5 is a schematic view shoxiDng another machine for the continuous production of the sealed cells forming the heat accumulator according to the present invention; Fig. 6 sllo^s part of a continuous belt of cells produced with the ;:achine of figure 5; and Fig. 7 is a graph reporting temperature curves in function of the heat exchanged per unit of volume, of one of the chemical substances used in the present invention. The curves illustrate a hypothesis of behaviour of this substance. The accumulator according to the present invention is formed of a plurality of cells C filled ith a substance F having a high latent melting heat. The cells C are formed of a plastic material having the follow- ing characteristics: it is thermoformable, apt to be heat sealed and it has a high coefficient of thermal conductivity. A preferred material is constituted by coextruded, high-density polyethylene. The term "coextruded" is intended for a high-density polyethylene extruded simultaneously .th a thin-film polyethylene, which perfectly adheres to the first, increasing its heat-sealing characteristics (obviously on the side ;here the thin film is applied). The cells C enclose in their inner part a certain quantity of substance F with high latent melting heat, the melting temperature of TAlich is included between 0 C and 100 C. Various chemical compounds are apt to fulfil these conditions. The substance F lill preferably be selected among the chemical compounds belonging to the group comprising hydrate salts, hydrate phosphates, sulphates and sulphites, or else to the group constituted by the paraffines. Anong the indicated products, the following have been tested bith success: decahydrate sodium sulphate m.p. 32. 40C Q1 85 kcalZdm3 dodecahydrate bisodium pilosphate m.p. 36 C Q1 90 kcal/dm3 heptahydrate bisodium phosphate m.p. 48 OC Q1 90 kcal/im3 where m.p. is the melting point of the substance, and Ql is its latent melting heat per unit of volume. All these products have a high latent melting heat per unit of volume (equal to an average of about 80-90 tines the specific heat per unit of volume of water), and they also have melting temperatures included between OOC and 1000C.- The melting temperature of the substance F forms the parameter according to which each chemical compound is preferred for a specific application, as better explained hereinafter. As previously stated, this type of chemical compounds, if subjected to a series of melting cycles and subsequent crystallization, may undergo - due to possible separations of the phases or evaporation of the components - a decay of its physical characteristics, particularly those specified heretofore, which condition the proper working thereof. The Applicant has no been able to establish, surprisingly, that if such chemical compounds are enclosed into sealed cells of small dimensions, the above drawback is substantially eliminated, that is, the decay of the physical characteristics of said chemical compounds occurs only after such a high number of cycles, as not to be felt in the practical uses. In particular, the volume of the cell C lill have to be less than a critical volume equal to about l dim . Preferably, said volume tzitl be far more limited, for istance comprised between 50 and 800 cc. In these conditions, the substance F may perform a very high number of cycles - for instance, up to about 3500 cycles - without undergoing any altering. Since, in current applications such a number of cycles corresponds to a period of time of about a hundred years, it can be understood how the desired working of the substance F is practically unlimited. Increasingly smaller volumes of the cells C involve an increase in the number of cycles, which the substance F can perform without undergoing any altering. On the other hand, a reduction in the size of the cells C involves an increase in the total production costs thereof. It trill thus be necessary to find an economical "optimum" arrangement to determine the ideal size of the cells C, taking also into account the requirements dictated by the various types of uses. The cells C are formed according to a particularly simple process, comprising the folloing stages: - forming a plurality of small cavities into at least one sheet of thermoformable plastic material; - filling said cavities ith said substance-F having a high latent melting heat, at a temperature above the melting point of said substance, so as to keep it at the fluid state during the filling operations; - heat sealing said cavities, under partial vacuum, so as to form a plurality of sealed cells C, filled with said substance F and practically having no air locks. .o different machines, apt to carry out this process, are schematically illustrated in figures 1 and 5. The two machines produce cells C lsith different final shapes, which can be suited for different applications. The machine illustrated in figure 1 substantially comprises a head 1, which provides to pour the substance F inside the sheet 2 of plastic material, having a tubular shape. The head 1 may be constituted by an extruder, apt to extrude the tubular sheet 2 simultaneously ith the feeding of the substance F. The sealing operation of the single cells takes place in 3 and 4, thereby obtaining chains of cells, as illustrated in figure 2. These chains of cells C can have an end tailpiece 5, apt to be folded over. The tailpiece 5 alloys to promptly hang the chains of cells C onto bars 6, or other hooldng means, provided at the top of heat storage reservoirs (not sho;n). The machine illustrated in figure 5 comprises instead a first roll 7 of plastic sheet material, into which are impressed in 3, by thermoforming, a series of cavities 9 of the dimensions desired for the cells C. Said cavities are filled in 10, and subsequently-the whole sheet is covered in 12 Tvith a second sheet of plastic material coming from the roll 11. Finally, the two sheets are reciprocally sealed in 13, in the contact areas surrounding the filled cavities. This allows to obtain a continuous belt of cells C, a portion of which is sho'n in figure 6, positioned upside-don in respect of the position with dich it comes out of the machine for its production. Evidently, the aforedescribed machines are only some possible examples of carrying out the above illustrated process, of which there may obviously be other embodiments, according also to the shape desired for the cells C. The heat accumulator according to the present invention finds its best- use - as already seen in the introductory part - in all those cases in :hich the temperature of the heat source is too lo; to be able to be utilized in any other ':ay. This accumulator, in fact, by making use of the high latent heat of the substance F, allows to store large amounts of heat in a small space, restoring said heat at the most appropriate moment. The accumulators may be placed in direct contact with any heat source, as for example sun radiation, industrial heat excesses, thermal exchange fluids, and the like. In the presence of temperatures higher than the exchange temperature of the substance F (defined hereinafter), this latter absorbs heat and gradually melts. This heat is automatically and promptly restored, by renewed solidification of the substance F, as soon as the temperature drops below said exchange temperature. The amount of heat absorbed per unit of volume is obviously in relation to the value of the latent heat of each single compound forming the substance F. The heretofore specified exchange temperature is the temperature at which the heat bac!cflov between substance F and environment taices place (here and hereinafter it is meant - unless othertfise indicated - that the substance F absorbs or transfers heat exclusively under form of latent heat). If the environment has temperatures below the exchange temperature, heat is transferred from the substance F to the environment through a gradual solidification of the substance itself. Viceversa, if the environment has a temperature which is lligher than the exchange temperature, heat is transferred from the environment to the substance F. The aforementioned characteristics would lead to the conclusion that the exchange temperature should coincide lith the melting temperature of the substance F. Whereas, the Applicant was actually able to ascertain, experimentally, that the exchange temperature is usually below the melting temperature and that it depends, as rell as from this latter, also from the amount of substance F present in the support (slab, all or the like), from the thickness of said support and, finally, from the total coefficient of thermal conductivity K of the support itself. Always experimentally, it has been able to establish, through special temperature probes, that the substance F is apt to absorb heat even at temperatures up to 150-200C lower than the melting temperature, in conditions of slow cooling or heating of the environment, while in fast cooling conditions the substance promptly (within a few seconds) reaches its olm melting temperature. This last characteristic is particularly interesting because, in case of a sudden drop of the external temperature, the substance F reaches its own melting temperature and it is therefore apt to transfer large quantities of heat in a short time (due to the increase in the difference of temperature) restoring in the environment the desired temperature conditions. On account of these characteristics, the accumulator according to the present invention lends itself particularly -11 for use in applications which require the temperature to keep constant around a predetermined value, for instance typically in the conditioning of rooms, lthere it lill be able to perform the double function of producing heat in the winter season and of absorbing the same in the summer season. A possible theoretical hypothesis mll now be given apt to justify the apparently anomalous behaviour of the substance F forming the accumulator according to the present invention, that is, its capability to absorb heat, under form of latent heat, even at temperatures below the melting temperature. Fig. 7 shows a qualitative graph of a heating curve of a typical substance F, itll melting point of 320C. In abscissae are reported the quantities of heat Q in kcal/dm , shill the ordinates indicate the -temperature T in C. The line A-B represents the heating of the substance F at the solid state from T = 0 to T = 320 (melting temperature). The horizontal- line B-C represents the melting at a constant temperature, supplying 85 kcal/dm , and finally, the line C- represents the heating of the substance F completely melted. One assumes the presence of a metastable branch C-X, which appears in conditions of a slow cooling, eventually followed by an equally slow heating. The presence of said branch justifies the fact that latent heat is not exclusively exchanged at the temperature of 320, but in a range of temperatures included between 320 and a tempe rature T , which cannot be exactly defined but which anyhow varies x between 80 and 150. The exchange temperature of the substance F - but only, as said, in slow cooling eventually followed by slow heating conditions - can be set at any point of this range of temperatures, by acting on the parameters already seen heretofore, which can be suitably progra=,red at the planning stage. In the event of the exchange temperature being set at 220C (a typical value for the conditioning of rooms), the working area of the substance F /ill cover the arc of the curve Y-Z. The result is that, in conditions of high isolation during the summer period, any rise of temperature above the exchange temperature will cause a partial melting of the. substance F with conversion of the heat of the atmosphere into latent heat of the substance F. The temperature increase of the substance F, resulting from this melting, is very limited and does not exceed - in the course of a particularly hot day - a few tenths of a degree. It is therefore quite evident how, in this way, it is possible to obtain a perfect conditioning action, in the sense heretofore specified. It should furthermore be noted that this hyfilothesis satisfacto rily explains the behaviour of the substance F in the event of sudden cooling. In fact, in this case (for instance during a strong sum niter storm) the substance F abandons the state of unstable equilibrium relative to the curve C-X, and imaediately moves to the corresponding stable condition W at the temperature of 320C, due to the supply of heat deriving from the simultaneous solidification of a part of said substance F. lEen applied for conditioning rooms, the single cells C (separated the ones from the others, as shown in figure 3) may be mingled directly with concrete, or the like, for casting slabs or walls of buildings to be conditioned (figure 4). Alternatively, the cells C (in the shape shown in figure 6) may constitute a continuous layer positioned between the slab and the finishing mantle of flooring. This arrangement allows to obtain inside the buildings a practically constant temperature value compensating the temperature differences tied to the day-night cycle. Furthermore, this arrangement - in association itch special central storage reservoirs forming large reserves of latent heat - allows to distribute the heat required for heating rooms during the winter season. In such central heat storage reservoirs, the cells C are arranged as illustrated in figure 2, or else in the form of belts (figure 6) placed astride of the bars 6, inside reservoirs filled with a worlcing fluid (for instance water) apt to constitute the heat transmission means between the single cells C of each reservoir, and between these cells and the cells C scattered into the walls of the building. By lay of example, se are giving hereunder the formulas of some preferred types of substances F, indicating - in their order - the melting temperature, the latent heat in kcal/i13, and the exchange temperature in OC. For each formula, the field of application is indicated: a) 32/35/22 and 36/90/36 for the heating of rooms, ';ith positioning of the cells C within the concrete elements forming the buildings to be conditioned (preferably floorings). The first formula is adopted in tIle case of residences, industrial plants and the like. Mle second formula is typically studied for application to greenhouses or other similar constructions having the same heating requirements; b) 48/90/55 for storing hot water for sanitary uses and for heat storage processes and thermomising in general (central heat storage reservoirs). In this case the exchange temperature is controlled by means of a thermostat, tich circulates the hot ater coming from the heat collectors only when its temperature exceeds the exchange temperature. This latter is then determined so as to provide a sufficient temperatures jump in respect of the melting temperature of the substance F. Obviously, other types of substances F, lith different formulas, may be prearranged for applications which require different operative temperatures; for instance, a formula of the type 32/35/lO could be perfectly suited to prevent the forming of ice onto viaducts, or in other similar special applications. From the foregoing, it is undoubted that the present invention has fully attained its intended objects. It in fact provides a heat accumilator which is apt to store, in a limited space large quantities of heat, at a temperature prearranged according to the temperature of the heat source being utilized and according to the requirements of use. Furthermore, as seen, the accumulator has a very long and practically unlimited life. The invention is particularly suited for solar plants without concentration of the radiations, to which it confers a high degree of autonomy, compensating not only the temperature differences connected ith the day-night period, but above all the radiation shortages connected with the autumn-winter periods. The invention has been described kith reference to some preferred embodiments thereof, but it is evident that there may be other embodiments differing from the same, arising from requirements of application, within reach of an expert in the art and thus all falling within the scope of the invention itself.

Claims: CLAIMS I) Latent heat accumulator, of the type using a substance with a high latent melting heat per unit of volume and w-.ith a high thermal conductivity, characterized in that said substance is enclosed in a plurality of sealed cells formed of a material with high thermal conductivity and each having dimensions of the order of magnitude of centimeters, and in that said substance has a melting temperature included between OOC and 1000 C. 2) Accumulator as in claim i), herein said sealed cells are formed of a thermoformable plastic material, apt to be heat sealed. 3) Accumulator as in clain l), wherein said plastic material is coextruded high-density polyethylene. 4) Accumulator as in claim i), wherein said substance with high latent melting heat is a chemical compound included in the group consisting of: hydrate salts and, in particular, hydrate phosphates, sulphates and sulphites. 5) Accumulator as in claim 1), wherein said substance with high latent melting heat is a chemical compound included in the group constituted by the paraffines. 6) Accumulator as in claim l), "wherein said cells form a continuous chain. 7) Accumulator as in claim l), wherein said cells form a continuous belt containing several cells placed crossbjse. ) Accumulator as in claim l), wherein said cells have a volume of less than 1 dm 9) Accumulator as in claim 1 herein said cells have a volume between 50 and 100 cc. to) Process for the production of a latent heat accumulator, of the type using a substance with high latent melting heat per unit of volume and :ith a high thermal conductivity, characteri zed by comprising the stages of: - forming a plurality of small cavities into at least one sheet of a thermoformable plastic material; - filling said cavities ith said substance having a high latent melting heat, at the fluid state; - heat sealing said cavities under partial vacuum, so as to form a plurality of sealed cells, filled with the substance and practically having no air locks. ll) Process as in claim to), for producing a latent heat accumulator as in claim 6), wherein said sheet of plastic material is a tubular sheet and is coextruded simultaneously with the feeding of said substance R high latent melting heat, and said cavities and cells are formed by heat sealing operations on the tubular sheet. 12) Process as in claim to), for producing a latent heat accurulator as in claim 7), wherein said cavities are obtained, by thermoforming, into a first sheet of plastic material and, after the cavities have been filled with said substance having a high latent melting heat, a second sheet of plastic material is applied on the first and sealed thereon in the contact areas surrounding the cavities. 13) Process as in claims to), 11) or 12), wherein said sealed cells are subsequently separated the ones from the others. 14) Use of a latent heat accumulator as in any one of the preceding claims 1) to 9), for hot water production plants making use of solar energy, wherein said cells are arranged as hanging chains or belts, plunged into the fluid of a heat storage reservoir. 15) Use of a latent heat accumulator as in any one of the preceding claims l) to 93, in room conditioning plants malcing use of solar energy, wherein said cells, either singly or in the form of a belt, are incorporated into the concrete of the slabs or of the stalls. 16) Use of a latent heat accumulator as in any one of the preceding claims t) to 93, in heat regeneration plants at temperatures included between OOC and 1000C.

Inventors: STIFFLER, MARIO
Applicants: STIFFLER MARIO, TEA SISTEMI SRL
Application year: 1982
Main classification: C09K5
IPC codes: F28D20, C09K5