HEAT ACCUMULATION SYSTEM

Abstract: A heat accumulation system has a plurality of chemical heat accumulation units (A, B) arranged in parallel and each incorporating reaction vessels (1, 2, 1', 2') containing, respectively, a chemical heat accumulating material such as zeolite (3, 3') and a reaction medium (4, 4') such as water. Any surplus heat which could not be used in the regeneration of the chemical heat accumulation material in one system is utilized for evaporation of a reaction medium in the other unit. Disclosed also is a method of operating this system.

Description: The present invention relates to a chemical heat accumulation system comprising at least two chemical heat accumulation units, each including a first vessel accommodating a chemical reaction material, a second vessel accommodating a reaction medium, a pipe interconnecting said first and second vessels and a valve provided in said pipe, heat supply means for introducing heat from a heat source into said first vessel of each of said chemical heat accumulation units to heat said chemical reaction material therein, and heat recovery means for recovering, by a first heat medium, the heat generated as a result of heat-generating reaction of said chemical reaction material in said first vessel of each of said chemical heat accumulation units. Such a heat accumulation system in disclosed in US-4 161 211. The system comprises a pair of chemical heat accumulation units, each including a first vessel accommodating a reaction material, a second vessel accommodating a reaction medium, a pipe interconnecting the first and second vessels, and a valve disposed in the pipe. Each of the vessels of each of this prior art chemical heat accumulation units accommodates only a single heat exchanger, which delimits operation and efficiency capabilities. Heat accumulation apparatus employing chemical heat accumulation materials are further disclosed in JP-60-226678 A, 60-263060 A, 61-11574 A, 63-34463 A and 63-34464 A. In these known arts, however, there is no means for an alternating use of a pair of parallel heat accumulation apparatus for the purpose of smooth operation of a system including the heat accumulation apparatus. In consequence, it has been impossible to make an efficient use of the heat energy possessed by a waste gas: namely, heat energy of the waste gas could not be used with high efficency. Accordingly, it is the object of the invention to provide a chemical heat accumulation system of the genaric kind which enables to greatly improve the heat recovery efficiency and to have a smooth and uninterrupted operation. This object is obtained with the chemical heat accumulation system of the generic kind in that said heat supply means comprise heat supply lines respectively extending through said first vessels of said chemical heat accumulation units and including first heat exchangers respectively disposed in said first vessels of said chemical heat accumulation units, in that said heat recovery means comprise heat recovery lines each extending through said second vessel of one of said chemical heat accumulation units and then through said first vessel of the other chemical heat accumulation units and including a second heat exchanger disposed in said second vessel of said one chemical heat accumulation unit and a third heat exchanger disposed in said first vessel of the other chemical heat accumulation unit, the arrangement being such that a second heat medium heated by said heat source is supplied from said heat source through one of said heat supply lines into said first heat exchanger in said first vessel of one of said chemical heat accumulation units and that said first heat medium is supplied through one of said heat recovery lines into said second heat exchanger in said second vessel of said one chemical heat accumulation units and then posses through said third heat exchanger in said first vessel of the other chemical heat accumulation unit, in that said heat supply lines are provided with valves operable to switch over the heat supply by means of the second heat medium from the one chemical heat accumulation unit to the other chemical heat accumulation unit and in that said heat recovery lines are provided with valves operable to switch over the heat recovery by means of the first heat medium from the other chemical heat accumulation unit to the one chemical heat accumulation unit. Thus, the heat accumulation system according to the present invention has at least two chemical heat accumulation units arranged in parallel and each including a first vessel containing a reaction material (chemical heat accumulating material) and a second vessel containing a reaction medium. When two such units are used, any surplus heat which could not be utilized in the regeneration of the reaction material in the first unit is efficiently utilized for the purpose of heating of the reaction medium in the second vessel in the second unit. The gas or vapor produced as a result of the regeneration of the reaction material in the first vessel of the first unit is condensed in the second vessel of the same unit by allowing another heat medium to absorb condensation heat, so that this heat medium is pre-heated. The pre-heated heat medium is brought into heat exchange with the reaction material in the first vessel of the second unit so as to be heated up to a higher temperature through absorption of the reaction heat, whereby heat can be recovered effectively and delivered as a heat output. According to the invention, it is thus possible to make an efficient use of the surplus heat which could not be utilized for regeneration of the reaction material and the condensation heat generated when the gas produced as a result of the regeneration is liquefied. The described operation can be executed alternately with each of the first and second chemical heat accumulation units by switching the operation phases of these units, thereby offering a high rate of utilization of heat energy. As will be understood from the foregoing description, the heat accumulation system of the present invention provides a high heat recovery efficiency when used in an air conditioning or a refrigeration system, as in the cases of other applications. Practically, a cold heat of about - 30°C or so can be obtained in the second vessel, by using an alcohol such as methyl alcohol or ethyl alcohol as the reaction medium and silica-gel as the reaction material. The heat accumulation system of the present invention employs a parallel connection of a plurality of chemical heat accumulation units such that the waste heat remaining in the waste heat carrying medium after regeneration of the reaction material in one of the units is utilized in the evaporation of the reaction medium in the other chemical heat accumulation unit, so that the heat derived from a heat source can be recovered with a high efficiency. The heat accumulation system of the present invention has heat recovery means in which a heat medium used for the purpose of heat recovery is circulated through the second vessel of one of the heat accumulation units so as to absorb condensation heat which is generated in this second vessel as a result of condensation of the gas which has been produced as a result of regeneration of the reaction material, the heat medium being then introduced into the first vessel of the other chemical heat accumulation unit which is in the heat radiating phase. It is therefore possible to further heat the heat medium to a higher temperature, thus offering a higher efficiency of heat recovery. It is also to be noted that the heat accumulation system of the present invention can operate smoothly and continuously because a plurality of chemical heat accumulation units can alternately put into heat radiating operation and regenerating operation such that one of the units discharges heat while the other or another unit regenerates the reaction material. Preferably each of said heat supply lines extends from said first vessel of one of said chemical heat accumulation units into and through said second vessel of the other chemical heat accumulation unit and includes a fourth heat exchanger disposed in said second vessel of said other chemical heat accumulation unit. Advantageously each of said heat supply lines further includes a fifth heat exchanger disposed between said first heat exchanger and said fourth heat exchanger. Conveniently each of said recovery lines further includes a sixth heat exchanger disposed between said second heat exchanger and said third heat exchanger. Furthermore seventh and eighth heat exchangers may be respectively disposed in heat exchanging relationship with said fifth heat exchangers and duct means may be provided in fluid-flow communication with said seventh and eighth heat exchangers to collect heat therefrom. Additionally, ninth and tenth heat exchangers may be respectively disposed in heat exchanging relationship with the sixth heat exchangers and duct means may be provided in fluid-flow communication with said ninth and tenth heat exchangers to collect heat therefrom. It is possible that exhaust duct means for collecting waste heat are derived from said heat supply lines, wherein said heat recovery means has a portion disposed in said duct means so that said first heat medium is supplied through said portion of said heat recovery means and heated by the heat collected by said duct means. The heat source can be a gas turbine and the heat medium can be water, said water being heated as a result of heat recovery to generate steam which is introduced into a combuster of said gas turbine. The first heat medium may be water, said water being heated as a result of the heat recovery to generate steam which is introduced into a steam turbine to drive the same. The invention also relates to a chemical heat accumulation plant comprising a plurality of sets of chemical heat accumulation systems. Preferably in such a plant the heat recovered by the heat recovery means of one of said chemical heat accumulation systems from said first vessels of said one heat accumulation system is introduced into the first heat exchangers in the first vessels of the other heat accumulation system through the heat supply means of said other chemical heat accumulation system. The above features and advantages of the present invention will become clear from the following description of the preferred embodiments when the same is read in conjunction with the accompanying drawings. Fig. 1 is an illustration of an embodiment of the heat accumulation system in accordance with the present invention; and Figs. 2 to 7 are illustrations of modifications of the heat accumulation system of the present invention. Referring to Fig. 1, an embodiment of the heat accumulation system of the present invention is composed mainly of a first chemical heat accumulation unit A and a second chemical heat accumulation unit B. The first chemical heat accumulation unit A includes a first vessel 1 containing a reaction material 3 such as lime, zeolite or the like, a second vessel 2 containing a reaction medium such as water, methanol or the like, a pipe 5 connected between the first and second vessels 1 and 2, and a valve 6 provided at an intermediate portion of the pipe 5. Similarly, the second heat accumulation unit B includes a fist vessel 1′ containing a reaction material 3′, a second vessel 2′ containing a reaction medium 4′, a pipe 5′ connected between the first and second vessels 1′ and 2′,and a valve 6′ provided at an intermediate portion of the pipe 5′. The heat accumulation system is connected to, for example, a heat source H which discharges waste heat by means of a second medium having a comparatively high temperature. The heat source H is, for example, a gas turbine, an internal combustion engine, a fuel cell or the like. Heat produced by a blast furnace, solar heat and heat generated by utilization of midnight power also can be used as the heat from a heat source H. A description will be given of a practical example of application of this system in which the first and second heat accumulation systems are operated alternatingly to recover heat wasted from the heat source H so as to continuously generate heat in the form of a temperature higher than that wasted from the heat source, thereby enabling an efficient use of the wasted heat. It is assumed here that the first chemical heat accumulation unit A is in the heat accumulation phase (regeneration), while the second chemical heat accumulation system B is in the heat discharging phase. The second medium carrying heat wasted from the heat source H is delivered to a first heat exchanger 7 provided in the reaction material 3 in the first vessel 1, through a duct or a pipe 15 via a valve 13. It is to be understood that a corresponding valve 13′ associated with the second heat accumulation unit B is closed in this mode. In consequence, the reaction material 3 is heated so that the reaction medium 4 adsorbed or absorbed on or in the reaction material 3 is evaporated to become a gas which is supplied to the second vessel 2 through the pipe 5. The gas is then cooled and liquefied while giving condensation heat to a heat a first medium which is introduced into the second vessel 2 through a pipe 12. It is assumed here that the reaction material 3 is lime (CaO) and has been changed into slaked lime (Ca(OH)₂) upon absorption of the reaction medium 4. In such a case, vapor of H₂O is separated in the first vessel 1 as a result of heating by the waste heat carried by the second medium, so that the reaction material 3 is progressively changed again into CaO. On the other hand, the vapor of H₂O introduced into the second vessel 2 is effectively used in the following manner. The above-mentioned first medium, which may be water or air, is introduced into a second heat exchanger 9 in the second vessel 2 through the pipe 12 via a valve 11. In consequence, the vapor of H₂O introduced into the second vessel 2 is condensed as a result of delivery of heat to the first medium, so that the first medium is heated to a higher temperature. The thus heated first medium is then introduced into a third heat exchanger 8′ in the first vessel 1′ of the second chemical heat accumulation unit B through a pipe 14. Since the second chemical heat accumulation unit B is in the heat discharging phase, the reaction medium 4′ in the second vessel 2′ is evaporated to become vapor which is introduced through a pipe 5′ into the first vessel 1′ of the second heat accumulation unit B, so that the vapor reacts with the reaction material 3′. The reaction material 3′ has been heated to an extremely high temperature as a result of the reaction, so that the first medium introduced into the third heat exchanger 8′ is heated to a very high temperature by the heat of the reaction material 3′ so as to become superheated gas or superheated steam. The temperature to which the first medium is heated is higher than the temperature of the temperature of the second medium carrying the heat wasted from the heat source H. The first medium thus heated to a high temperature is then delivered through an outlet pipe 16 so that the heat possessed by the first medium is effectively utilized. In this process, the heat required for gasifying the reaction medium 4′ in the second vessel 2′ of the second heat accumulation unit B is derived from the gas wasted from the final stage of the heat source H. Namely, the waste heat carrying second medium carrying the waste heat from the heat source H, introduced into the first heat exchanger 7 for heating the reaction material 3, still possesses heat even after the heating of the reaction material 3. The waste heat carrying second medium is then introduced through a valve 18 and a duct 24 into a forth heat exchanger 10′ in the second vessel 2′ so as to heat the reaction medium 4′. When a large quantity of heat is introduced into the forth heat exchanger 10′, opening of the valve 18 and the opening of a valve 17 in a branching line are suitably controlled so as to allow any surplus heat to be delivered to the outside of the system through another outlet pipe 20 via via the valve 17. When the heat accumulation (regeneration) in the first chemical heat accumulation unit A and the heat discharge from the second chemical heat accumulation unit B are over, the operation phases are switched so that the first A and the second B chemical heat accumulation units become ready for operations in the heat discharging phase and in the heat accumulation phase, respectively. It is therefore possible to continuously operate the system without suspending recovery of the heat. It will be seen that the switching of two chemical heat accumulation units A, B is possible by a suitable valve operation, because both units A, B have the same arrangement. In some cases, it may become necessary that the heat accumulation (regeneration) or the heat discharging operation are temporarily suspended. In order to cope with such a demand, the operator is required only to close the valve 6 in the pipe 5 or the valve 6′ in the pipe 5′. As will be understood from the foregoing description, the heat accumulation system employs a plurality of chemical heat accumulation units A, B which are operated alternately or in a switching manner so that the whole system can smoothly operate without suspension. In addition, both the heat generated through regeneration of the reaction material 3,3′ and the heat which could not be utilized in the heating of the reaction material 3,3′ are effectively recovered and utilized. In consequence, the heat accumulation system provides a high rate of recovery of waste heat energy well reaching 90% or higher, in contrast to conventional systems which could provide a waste heat recovery rate of about 70% or so at the highest. Fig. 2 shows a modification of the embodiment shown in Fig. 1. In this modification, the waste heat carrying second medium from the heat source H is introduced into the first vessel 1 or 1′ and is then introduced into an exhaust duct 21 directly through the pipe 20 or 20′ or via the second vessel 2′ or 2 and the pipe 19′ or 19 so that the heat energy still remaining in the waste heat carrying second medium is effectively recovered in the exhaust duct 21. More specifically, the first heat medium such as water is introduced into a heat exchanger 23 disposed in the exhaust duct 21 via an inlet pipe 22 so that the heat medium is heated by the heat remaining in the waste heat carrying second medium. The thus heated first heat medium is then introduced into the second vessel 2 through the pipe 12 and then into the first vessel 1′ through the pipe 14 so as to become a vapor of high temperature which is delivered through the outlet pipe 16. Alternatively, the first heat medium is introduced into the second vessel 2′ through the pipe 12′ and then into the first vessel 1 through the pipe 14′ so as to become a vapor of high temperature which is delivered through the outlet pipe 16. It will be seen that the modification shown in Fig. 2 provides a higher rate of recovery of the waste heat. Fig. 3 shows another modification of the embodiment of Fig. 1 combined with a power generating gas turbine system. The gas turbine system has a compressor 30, a combustor 31, a gas turbine 32 and a generator 33 for generating electric power. In this case, water is used as the heat medium introduced through the pipe 12 or 12′. The first heat medium is evaporated to become steam as it passes through the heat exchanger 8′ or 8 and is injected into the combustor 31 through a pipe 16b or 16b for the purpose of suppressing generation of nitrogen oxides (NOx). In this modification, gas dampers or change-over valves 34,35 and 35 are used in place of the valves 13, 13′, 17, 17′ and 18, 18′ of Fig. 1, thereby simplifying the construction of the system. Fig. 4 shows a different modification in which the heat accumulation system is connected to a combined power generating system having a power generating gas turbine system and a power generating steam turbine system. This modification is different from that shown in Fig. 3 in that the steam of high temperature and pressure available at the outlet pipe 16a or 16b is introduced into a steam turbine 37 so as to drive a generator 38 thereby increasing the total electric output power of the combined power generating system. It will be clear to those skilled in the art that the modifications of Figs. 3 and 4 may be combined with each other such that the steam of high temperature and pressure available at the outlet pipes 16a and 16b are introduced into the combustor 31 and the steam turbine 37. The invention also may be modified such that a pair of heat accumulation systems, each having a construction as shown in Fig. 1, are combined so as to provide a dual system. Such a dual system includes a pair of first chemical heat accumulation units A of the same type as that shown Fig. 1 arranged in parallel with each other and a pair of the second chemical heat accumulation units B of the same type as that shown in Fig. 1 arranged in parallel with each other. One or both of the units in the respective pairs of units are put into operation according to a change in the heat wasted the heat source H. It is also possible to operate two pairs of heat accumulation units with a suitable time difference so as to smooth the heat output from the system. It is also possible to construct a multiple system by combining three or more heat accumulation systems each having the same construction as that shown in Fig. 1. The arrangement also may be such that a parallel connection of a pair of second chemical heat accumulation units B of a copmparatively small capacity is used in combination with a single first chemical heat accumulation unit A of a comparatively large capacity. Fig. 5 shows a different modification of the heat accumulation system shown in Fig. 1. In this modification, a plurality of heat accumulation systems, each having the same construction as the system shown in Fig. 1, is connected in series so as to provide a multi-staged heating system. Namely, the first heat medium of high temperature delivered from the outlet pipe 16 of the heat accumulation system 100 of the first stage is introduced into the duct or pipe 15′ of the heat accumulation system 200 of the second stage so that the temperature of the heat medium is further elevated. In this modification, a chemical heat accumulation material which exhibits a comparatively low heating temperature, e.g., zeolite, is used in the heat accumulation system 100 of the first stage, whereas the heat accumulation system 200 of the second stage utilizes a chemical heat accumulation material which develops a heating temperature higher than that produced by the material of the first stage, e.g., lime or strontium oxide. For instance, referring to Fig. 5, zeolite is used as the reaction material 3, 3′ in the first vessels 1, 1′ of the first stage and water is used as the reaction medium 4, 4′ in the second vessels 2, 2′. In such a case, steam of about 350°C is obtained from the outlet pipe 16 of the first stage. This steam is supplied into the first vessels 1, 1′ of the heat accumulation system 200 of the second stage through the pipe 15′. If lime (or strontium oxide) and water are used, respectively, as the reaction material 3,3′ in the first vessels 1,1′ and the reaction medium 4,4′ in the second vessels 2,2′ of the second stage heat accumulation system 200, a high steam temperature of 650°C is obtained at the outlet pipe 16′ of the second stage heat accumulation system 200. Fig. 6 shows a different modification of the heat accumulation system of Fig. 1, arranged to further improve the performance. In this embodiment, a duct (or pipe) 50 shunts from the duct (or pipe) 15. A first heat medium flowing through the pipe 14 or 14′ is heated by the heat carried by a first medium flowing through the duct (or pipe) 50, through heat exchange performed in further heat exchangers 57 to 60. At the same time, the the waste heat carrying first medium flowing through the duct 24 or 24′ is heated through heat exchangers 61 to 64 thereby attaining a higher overall heat recovery efficiency. As will be seen from Fig. 6, the first medium flowing through the duct 50 is discharged into an exhaust duct 52 through valves 53 to 56, and heat exchangers 58, 60, 62 and 64. On the other hand, the heat exchangers 57 and 59 which are sixth heat exchangers are provided in the pipes 14 and 14′. The first heat medium flowing through these heat exchangers 57, 59 is heated by a heat exchange through heat exchangers 58 and 60 and is then further heated upon absorption of reaction heat through the third heat exchanger 8′ or 8. The heat exchangers 61 and 63 called fifth heat exchangers are provided in the ducts 24 and 24′, respectively. The waste heat carrying second medium flowing through these heat exchangers 61 and 63 is heated through the above-mentioned heat exchangers 62 and 64, called a seventh and eighth heat exchanges, and is introduced into the forth heat exchangers 10′, 10 so as to heat the reaction medium 4′, 4. The degree of heating of the first heat medium flowing through the sixth heat exchangers 57 and 59 and the degree of heating of the waste heat carrying second medium flowing through the fifth heat exchangers 61 and 63 can be controlled by suitably adjusting the openings of the valves 53, 54, 55, 56 and 51. Fig. 7 shows a different modification in which the heat accumulation system shown in Fig. 1 is applied to a refrigeration system or an air conditioning system. Referring to this figure, the forth heat exchangers 10,10′ are connected to fan-coil units (or coolers) 40, 40′ through pipes 41, 41′. The pipes 19, 19′ shunting from the outlet pipes 20, 20′ in the embodiment shown in Fig. 1 are omitted in this modification. It is assumed that the first chemical heat accumulation system A, composed of first and second vessels 1, 2, pipe 5 and valve 6, is in the regenerating phase for regeneration of the heat accumulation material by the waste heat derived from the heat source H, while the second chemical heat accumulation system B, composed of first and second vessels 1′, 2′, pipe 5′ and valve 6′, is in the heat discharging phase. When the first heat medium introduced through the second heat exchanger 9 and the third heat exchanger 8′, it cools a reaction medium 4, e.g., alcohol or freon, and a reaction material 3′, e.g., silica-gel or zeolite, so that regeneration is promoted in the first chemical heat accumulation system A. In the second chemical heat accumulation system B, the reaction material such as silica-gel absorbs a gas, e.g., alcohol gas, coming from the second vessel 2′, so that the discharge of the heat is promoted. On the other hand, the temperature of the reaction medium 4′ , e.g., alcohol, in the second vessel 2′ is lowered as a result of evaporation thereof. Meanwhile, a refrigerant, e.g., water or freon is circulated in the pipe 41′ by means of a pump (not shown) so as to convey cold heat from the reaction medium 4′ to the fan-coil unit (or cooler) 40′ across the forth heat exchanger 10′, thereby to chill air or to freeze goods. When the first and second chemical heat accumulation units A and B are switched to heat discharging phase and regeneration phase, respectively, the cold heat becomes available at the forth heat exchanger 10, so that the fan-coil unit 10 is put into operation for the purpose of chilling air or freezing goods. It is possible to connect the pipes 41 and 41′ through a change-over valve. In such a case, one of the fan-coil units (or coolers) 40 and 40′ can be omitted. On the other hand, the first heat medium coming from the outlet pipe 16 has been heated to a high temperature so that it can be used for the purpose of heating water to enable a hot water service. It will be clear to those skilled in the art that a multi-stage system can be obtained by arranging a plurality of systems of the type shown in Fig. 7 in a multiple stages as in the case of the modification described in connection with Fig. 5, so that a cold heat of a further lowered temperature can be generated.

Claims: 1. A chemical heat accumulation system comprising at least two chemical heat accumulation units (A, B) each including a first vessel (1, 1′) accommodating a chemical reaction material (3, 3′), a second vessel (2, 2′) accommodating a reaction medium (4, 4′), a pipe (5, 5′) interconnecting said first (1, 1′) and second (2, 2′) vessels and a valve (6, 6′) provided in said pipe (5, 5′); heat supply means for introducing heat from a heat source (H) into said first vessel (1, 1′) of each of said chemical heat accumulation units (A, B) to heat said chemical reaction material (3, 3′) therein, and heat recovery means for recovering, by a first heat medium, the heat generated as a result of heat-generating reaction of said chemical reaction material (3, 3′) in said first vessel (1, 1′) of each of said chemical heat accumulation units (A, B), characterized in that said heat supply means comprise heat supply lines (15, 24; 15, 24′) respectively extending through said first vessels (1, 1′) of said chemical heat accumulation units (A, B) and including first heat exchangers (7, 7′) respectively disposed in said first vessels (1, 1′) of said chemical heat accumulation units (A, B), in that said heat recovery means comprise heat recovery lines (12, 14, 16b; 12′, 14′, 16a) each extending through said second vessel (2, 2′) of one of said chemical heat accumulation units (A, B) and then through said first vessel (1, 1′) of the other chemical heat accumulation units (B, A) and including a second heat exchanger (9, 9′) disposed in said second vessel (2, 2′) of said one chemical heat accumulation unit (A, B) and a third heat exchanger (8′, 8) disposed in said first vessel (1′, 1) of the other chemical heat accumulation unit (B, A), the arrangement being such - that a second heat medium heated by said heat source (H) is supplied from said heat source (H) through one of said heat supply lines (15, 24; 15, 24′) into said first heat exchanger (7, 7′) in said first vessel (1, 1′) of one of said chemical heat accumulation units (A, B) and - that said first heat medium is supplied through one of said heat recovery lines (12, 14, 16b; 12′, 14′, 16a) into said second heat exchanger (9, 9′) in said second vessel (2, 2′) of said one chemical heat accumulation units (A, B) and then passes through said third heat exchanger (8′, 8) in said first vessel (1′, 1) of the other chemical heat accumulation unit (B, A), in that said heat supply lines (15, 24; 15, 24′) are provided with valves (13, 13′) operable to switch over the heat supply by means of the second heat medium from the one chemical heat accumulation unit (A) to the other chemical heat accumulation unit (B) and in that said heat recovery lines (12, 14, 16b; 12′, 14′, 16a) are provided with valves (11, 11′) operable to switch over the heat recovery by means of the first heat medium from the other chemical heat accumulation unit (B) to the one chemical heat accumulation unit (A). 2. A chemical heat accumulation system according to claim 1, characterized in that each of said heat supply lines (15, 24; 15, 24′) extends from said first vessel (1, 1′) of one of said chemical heat accumulation units (A, B) into and through said second vessel (2′, 2) of the other chemical heat accumulation unit (B, A) and includes a fourth heat exchanger (10′, 10) disposed in said second vessel (2′, 2) of said other chemical heat accumulation unit (B, A). 3. A chemical heat accumulation system according to claim 2, characterized in that each of said heat supply lines (15, 24; 15, 24′) further includes a fifth heat exchanger (61, 63) disposed between said first heat exchanger (7, 7′) and said fourth heat exchanger (10′, 10) and by seventh and eighth heat exchangers (62, 64) respectively disposed in heat exchanging relationship with said fifth heat exchanger (61, 63) and duct means (52) provided in fluid-flow communication with said seventh and eighth heat exchangers (62, 64) to collect heat therefrom. 4. A chemical heat accumulation system according to claim 3, characterized in that each of said heat recovery lines (12, 14, 16b; 12′, 14′, 16a) further includes a sixth heat exchanger (57, 59) disposed between said second heat exchanger (9, 9′) and said third heat exchanger (8′, 8) and by ninth and tenth heat exchangers (58, 60) respectively disposed in heat exchanging relationship with the sixth heat exchangers (57, 59) and duct means (52) provided in fluid-flow communication with said ninth and tenth heat exchangers (58 and 60) to collect heat therefrom. 5. A chemical heat accumulation system according to one of the claims 1 to 4, characterized by exhaust duct means (21) for collecting waste heat derived from said heat supply lines (15, 24; 15, 24′), wherein said heat recovery means has a portion (23) disposed in said duct means (21) so that said first heat medium is supplied through said portion (23) of said heat recovery means and heated by the heat collected by said duct means (21). 6. A chemical heat accumulation system according to one of the claims 1 to 5, characterized in that said heat source (H) is a gas turbine (32) and that said first heat medium is water, said water being heated as a result of heat recovery to generate steam which is introduced into a combuster (31) of said gas turbine (32). 7. A chemical heat accumulation system according to one of the claims 1 to 6, characterized in that said first heat medium is water, said water being heated as a result of the heat recovery to generate steam which is introduced into a steam turbine (37) to drive the same. 8. A chemical heat accumulation plant comprising a plurality of sets of chemical heat accumulation systems (100, 200) according to claim 1 or 2. 9. A chemical heat accumulation plant according to claim 8, wherein the heat recovered by the heat recovery means (8, 16a; 8′, 16b; 16) of one (100) of said chemical heat accumulation systems (100, 200) from said first vessels (1, 1′) of said one heat accumulation system (100) is introduced into the first heat exchangers (7, 7′) in the first vessels (1, 1′) of the other heat accumulation system (200) through the heat supply means (15′) of said other chemical heat accumulation system (200).

Inventors: FUKUSHIMA, TOSHIHIKO, KUNUGI, YOSHIFUMI, YANADORI, MICHIO
Applicants: HITACHI, LTD.
Application year: 1989
Main classification: F28D20
IPC codes: F25B30, F25B17, F28D20