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WO2023053859A1 - Heat storage structure and heat storage system - Google Patents

Heat storage structure and heat storage system Download PDF

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Publication number
WO2023053859A1
WO2023053859A1 PCT/JP2022/033360 JP2022033360W WO2023053859A1 WO 2023053859 A1 WO2023053859 A1 WO 2023053859A1 JP 2022033360 W JP2022033360 W JP 2022033360W WO 2023053859 A1 WO2023053859 A1 WO 2023053859A1
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WIPO (PCT)
Prior art keywords
heat storage
heat
sealed container
storage material
storage structure
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.)
Ceased
Application number
PCT/JP2022/033360
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French (fr)
Japanese (ja)
Inventor
俊彦 赤塚
直之 河目
弘文 会田
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Canon Optron Inc
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Canon Optron Inc
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Filing date
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Priority claimed from JP2022108927A external-priority patent/JP2023051731A/en
Application filed by Canon Optron Inc filed Critical Canon Optron Inc
Priority to CN202280046682.2A priority Critical patent/CN117580928A/en
Publication of WO2023053859A1 publication Critical patent/WO2023053859A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/16Materials undergoing chemical reactions when used
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00

Definitions

  • the present disclosure relates to heat storage structures and heat storage systems.
  • heat storage technology There are generally three types of heat storage technology: sensible heat storage that uses the specific heat of substances, latent heat storage that uses changes in the state of substances, and chemical heat storage that uses chemical changes in substances.
  • the heat storage material reacts with a specific reaction medium such as water or ammonia to generate heat.
  • Chemical heat storage is suitable for long-term heat storage because it can maintain a heat storage state (a state where heat can be generated if there is a reaction medium) unless a reaction medium is supplied.
  • Chemical heat storage must create a stable mechanism for heat storage and heat generation after considering a series of phenomena accompanying chemical reactions, and has various problems. For example, when an exothermic reaction is caused by a reaction medium, the particles of the heat storage material agglomerate in an attempt to reduce the surface energy of each particle of the heat storage material. There was a problem.
  • the heat storage material is covered with a second compound having pores through which water molecules can pass, thereby suppressing the aggregation of the heat storage material and reducing the decrease in reactivity.
  • a heat-absorbing and heat-absorbing material is disclosed.
  • the heat storage material is an aggregate of fine particles, so if the reaction medium is liquid, there is a risk that it will be washed away. Also, if the reaction medium is a gas, the heat storage material tends to dance and may be blown away. Thus, the heat storage material may be washed away by the reaction medium. In addition, in the step of covering the heat storage material with the second compound, it is necessary to adjust the materials used and the process, and a simpler method is desired.
  • the present disclosure provides a heat storage structure that prevents the outflow of the chemical heat storage material due to the chemical heat storage material being swept away or blown away by the reaction medium, and capable of stably storing heat or exothermic reaction.
  • the present disclosure is a heat storage structure having a sealed container and a chemical heat storage material sealed in the sealed container,
  • the sealed container includes at least a portion of a water vapor permeable member
  • the chemical heat storage material is A group consisting of magnesium oxide, magnesium hydroxide, and at least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead.
  • the chemical heat storage material is a substance that generates heat by a hydration reaction and/or stores heat by a dehydration reaction
  • the heat storage structure is characterized in that the moisture permeability of the water vapor permeable member is 200 to 10000 g/(m 2 ⁇ 24 h).
  • the present disclosure is a heat storage system comprising a steam supplier for performing a hydration reaction, a heat supplier for performing a dehydration reaction, and a heat accumulator, wherein the heat storage device comprises the heat storage structure of the present disclosure; heat is sent to the heat accumulator by the heat supplier; The chemical heat storage material contained in the heat storage structure undergoes a dehydration reaction with the heat sent to the heat accumulator, whereby heat is stored in the chemical heat storage material, Further, steam is sent to the heat accumulator by the steam supplier, The heat stored in the chemical heat storage material is extracted by a hydration reaction of the chemical heat storage material contained in the heat storage structure. It relates to a heat storage system.
  • FIG. 1 shows a schematic diagram showing the configuration of one embodiment of the heat storage structure.
  • the heat storage structure is formed from a chemical heat storage material 1 and a sealed container 2 that seals the chemical heat storage material.
  • the sealed container has a property of impermeable to liquid water but permeable to water vapor (such property is hereinafter referred to as "moisture permeability".
  • moisture permeability The degree to which a substance having moisture permeability allows water vapor to pass is referred to as "moisture permeability”.
  • the sealed container 2 may include at least a portion of the water vapor permeable member.
  • the sealed container 2 may be entirely made of a water vapor permeable member. In the heat storage structure of FIG. 1, the sealed container 2 is made of a water vapor permeable member.
  • the chemical heat storage material 1 is a substance that generates heat by hydration reaction and/or stores heat by dehydration reaction, and is composed of magnesium oxide, magnesium hydroxide, alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, and copper. , at least one inorganic salt selected from the group consisting of zinc and lead, at least one selected from the group consisting of organic salts and halides. Among them, those having a dehydration reaction temperature of 200° C. or less are preferable. Since the temperature at which the dehydration reaction occurs is 200° C. or less, unused heat in the factory can be used as a heat source, leading to effective utilization of heat.
  • the chemical heat storage material particularly preferably contains at least one selected from the group consisting of magnesium oxide and magnesium sulfate from the viewpoint of having a large heat storage amount per mass.
  • At least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead that can be contained in the chemical heat storage material include hydrated It is not particularly limited as long as it generates heat by the reaction and/or accumulates heat by the dehydration reaction.
  • alkali metals refer to lithium, sodium, potassium, rubidium, cesium and francium.
  • Alkaline earth metals refer to beryllium, magnesium, calcium, strontium, barium and radium.
  • Preferred alkali metals are lithium and sodium, and preferred alkaline earth metals are magnesium and calcium.
  • Examples of at least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include carbonates such as calcium carbonate and barium carbonate; Phosphates include magnesium phosphate and sodium phosphate, sulfates include sodium sulfate and magnesium sulfate, nitrates include magnesium nitrate and aluminum nitrate, and silicates include magnesium silicate and calcium silicate. be done.
  • Examples of at least one organic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include formates, acetates, octylates and the like.
  • Examples include fatty acid salts, aromatic carboxylic acid salts such as phthalates and benzoates, and sulfonates such as p-toluenesulfonates and ethanesulfonates.
  • acetate is preferred.
  • Acetates include sodium acetate, calcium acetate, magnesium acetate, nickel acetate, copper acetate, zinc acetate, lead acetate and the like.
  • Examples of at least one halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include fluorides such as magnesium fluoride and calcium fluoride , chlorides such as magnesium chloride and calcium chloride, bromides such as magnesium bromide and calcium bromide, and iodides such as magnesium iodide and calcium iodide. Among them, magnesium chloride or calcium chloride is preferred.
  • a chemical heat storage material that stores heat by a hydration reaction is classified into a chemical heat storage material that forms a hydroxide by a hydration reaction and a chemical heat storage material that forms a hydrate.
  • a chemical heat storage material that forms a hydroxide for example, generates heat by a hydration reaction as shown in formula (1) and stores heat by a dehydration reaction as shown in formula (2).
  • a chemical heat storage material that forms a hydrate for example, generates heat by a hydration reaction as shown in formula (3) and stores heat by a dehydration reaction as shown in formula (4).
  • heat may be generated by a reaction that increases the hydration number from 1 to 6, or heat may be accumulated by a reaction that reduces the hydration number from 4 to 2.
  • Some chemical heat storage materials have high solubility in water and dissolve during the process of hydration reaction or dehydration reaction.
  • the dissolution during the hydration reaction is caused by the water added for the hydration reaction, and the dissolution during the dehydration reaction is caused by the moisture desorbed from the chemical heat storage material itself.
  • Examples of such substances include MgSO4.7H2O , potassium alum KAl ( SO4 ) 2.12H2O , sodium thiosulfate Na2S2O3.5H2O , sodium carbonate Na2CO3 . 10H2O can be mentioned.
  • the chemical heat storage material dissolves into a chemical heat storage material aqueous solution
  • the chemical heat storage material is sealed in a sealed container, and the sealed container is permeable to water vapor having a predetermined moisture permeability. Since the member is included in at least a part thereof, the chemical heat storage medium aqueous solution does not flow out of the sealed container, so the present disclosure is particularly effective in such a case.
  • the form of the chemical heat storage material is not particularly limited as long as the chemical heat storage material can undergo a hydration reaction. Quality is more preferred.
  • the moisture applied for the hydration reaction may be liquid water or water vapor.
  • the sealed container has a water vapor permeable member at least in part, so the sealed container may have a structure that cannot be opened and closed. It is preferable to have a structure that can be opened and closed.
  • a part of the sealed container is opened, liquid water is poured into the chemical heat storage material in the heat storage state sealed in the sealed container, and the sealed container is immediately sealed. Close the stop container. Heat generation due to hydration reaction begins when water is poured.
  • the chemical heat storage material does not flow out even after the reaction, it can be used repeatedly if the chemical heat storage material is dehydrated and returned to the heat storage state.
  • steam when steam is used, steam is supplied from the outside of the sealed container to cause the chemical heat storage material to generate heat due to a hydration reaction. Since the chemical heat storage material does not flow out even after the reaction, it can be used repeatedly if it is dehydrated and returned to the heat storage state. Even when water vapor is used, a part of the sealed container may have a structure that can be opened and closed as long as it is sealed during hydration and dehydration. Other methods of use include, for example, liquid water and water vapor. Heat generation from the chemical heat storage material can be repeated regardless of the reaction medium, but it may be used only once.
  • the dehydration reaction of the chemical heat storage material is not particularly limited as long as it can apply heat to the chemical heat storage material, but the temperature of the dehydration reaction is preferably 200° C. or less. Since the temperature of the dehydration reaction is 200° C. or less, unused heat in the factory can be used as a heat source, which leads to effective utilization of heat.
  • the dehydration reaction may be performed with the chemical heat storage material sealed in a sealed container, or only the chemical heat storage material may be dehydrated and then sealed in the sealed container.
  • the sealed container 2 seals the chemical heat storage material.
  • an effect is obtained that the chemical heat storage material does not flow out of the sealed container.
  • sealing the chemical heat storage material in the sealed container means that the chemical heat storage material is surrounded by the sealed container, the chemical heat storage material does not flow out of the sealed container, and water outside the sealed container It refers to making it impossible to enter the inside of the sealed container. Of course, this does not preclude providing the sealed container with a mechanism capable of releasing the seal.
  • the material of the sealed container is not particularly limited, but a material that can withstand the operating temperature is desirable. There are two types of working temperatures: the maximum temperature reached during hydration and the dehydration temperature of the chemical heat storage material. If the chemical heat storage material is used only once, it should be able to withstand only the maximum temperature reached during hydration if it is dehydrated before being sealed in the sealed container. When the sealed container is used repeatedly, the sealed container is required to have heat resistance corresponding to the dehydration temperature of the chemical heat storage material.
  • the heat resistance temperature of the sealed container is preferably 70° C. or higher, more preferably 100° C. or higher. Also, it is preferably 900° C. or lower, more preferably 700° C. or lower.
  • the heat resistant temperature of the sealed container refers to the melting point of the sealed container, and the melting point of the sealed container can be measured by a known method. For example, the melting point of the sealed container can be measured by subjecting a portion of the sealed container to thermal analysis such as differential scanning calorimetry (DSC) or differential thermal analysis (DTA). Moreover, the heat-resistant temperature of the sealed container can be adjusted by changing the material of the sealed container.
  • the material of the sealed container is preferably resin, porous metal, or porous ceramic.
  • a ceramic porous body is preferred.
  • the sealed container is preferably a film.
  • the thickness of the film is not particularly limited, it is preferably 1 ⁇ m or more, more preferably 10 ⁇ m or more. Moreover, it is preferably 1 mm or less, and more preferably 250 ⁇ m or less.
  • the sealed container includes at least a portion of the water vapor permeable member.
  • the entire sealed container may be a water vapor permeable member, and FIG. 1 is an example thereof, and the entire sealed container functions as a water vapor permeable member.
  • the water vapor permeable member has moisture permeability.
  • the water vapor permeable member has moisture permeability in order to cause a hydration and/or dehydration reaction while retaining the chemical heat storage material. be.
  • the moisture permeability of the water vapor permeable member is within the above range, the effect of the water vapor permeable member not permeating liquid water but permeating water vapor can be obtained. Therefore, even when water is used as the reaction medium, an effect is obtained that the chemical heat storage material does not flow out.
  • the chemical heat storage material is not blown off by water vapor. Furthermore, even if the chemical heat storage material, which is highly soluble in water, dissolves in the sealed container during the process of hydration reaction or dehydration reaction, it will not flow out of the sealed container. . If the moisture permeability of the water vapor permeable member is less than 200 g/(m 2 ⁇ 24 h), the water vapor generated from the heat storage material during dehydration cannot escape outside the sealed container, and the pressure inside the sealed container increases, resulting in sealing. The container seal is easily broken.
  • the water vapor permeability of the water vapor permeable member is higher than 10000 g/(m 2 ⁇ 24 h)
  • the water pressure resistance of the water vapor permeable member becomes low, and there is a risk that the liquefied heat storage material will seep out onto the surface of the water vapor permeable member.
  • the moisture permeability of the water vapor permeable member is preferably 2000 to 9800 g/(m 2 ⁇ 24 h) so that water vapor generated during dehydration can be smoothly discharged to the outside of the sealed container. As a result, it is possible to obtain the effect of preventing the sealing of the sealed container from breaking due to an increase in the internal pressure of the sealed container. Furthermore, it is more preferably 5000 to 9600 g/(m 2 ⁇ 24 h) so as to increase the intake of water vapor and promote the hydration reaction.
  • the method for adjusting the moisture permeability of the water vapor permeable member is not particularly limited, for example, the water vapor permeable member may have pores 3 .
  • the diameter of the pores 3 of the water vapor permeable member is not particularly limited as long as the water vapor permeability of the water vapor permeable member is within the above range. Since the size of gaseous water molecules is 0.38 nm and the size of liquid water particles is 100 ⁇ m to 3000 ⁇ m, from the viewpoint of permeation of gaseous water molecules and not permeation of liquid water molecules, It is preferably 0.38 nm or more, and preferably 100 ⁇ m or less. However, this is not the case because the appropriate pore size differs depending on the water repellency and water pressure resistance of the surface of the water vapor permeable member.
  • the material of the water vapor permeable member is not particularly limited as long as it satisfies the above moisture permeability, but it is preferable that the water vapor permeable member contains a resin so that the heat storage structure can be in a flexible state.
  • the resin is preferably a polyolefin resin such as polyethylene (PE) or polypropylene (PP), or a flexible resin such as a urethane resin such as thermoplastic polyurethane (TPU), more preferably perfluoroalkoxy, which has a high heat resistance temperature.
  • Fluorine resins such as alkane (PFA) resins and polytetrafluoroethylene (PTFE) resins, polyimides (PI) such as polyamideimide and polyetherimide, polydimethylsiloxane (PDMS), silicone resins such as silicone rubber, polyetheretherketone (PEEK) resin, polyphenylene sulfide (PPS) resin such as linear polyphenylene sulfide and crosslinked polyphenylene sulfide, polyester (PEs) resin, more preferably polytetrafluoroethylene having high chemical resistance and high corrosion resistance. (PTFE) resin.
  • the water vapor permeable member may be a combination of resin such as fluorine-coated glass cloth and other materials such as inorganic substances.
  • the “water vapor transmission rate” is the amount of water vapor that passes through a unit area of film-like material for a certain period of time, and is measured according to JIS Z 0208 in the present disclosure. Specifically, 35 g to 40 g of anhydrous calcium chloride of JIS K 8123 (which passes through a standard sieve of 2380 ⁇ m but does not pass through a standard sieve of 590 ⁇ m) was placed flat in a JIS L 1099 moisture permeable cup of ⁇ 60 mm as a moisture absorbent. Thereafter, a thin piece cut out from the sealed container was attached to a moisture-permeable cup and sealed using an oil compound as a sealing wax to prepare a sample.
  • JIS Z 0208 JIS Z 0208
  • a blank cup was produced by carrying out the same operation without adding the moisture absorbent to the moisture permeable cup.
  • the sample and blank cup obtained above are placed in a constant temperature and humidity apparatus at a temperature of 40 ⁇ 0.5 ° C., a relative humidity of 90 ⁇ 2%, and a wind speed of 0.5 to 2.5 m / s for a certain period of time. It was removed at intervals and weighed to determine the weight gain.
  • the weight increase of the sample is the sum of the weight increase of the moisture absorbent and the weight increase of the moisture permeable cup containing the flakes due to the absorption of water by the moisture absorbent, so it was corrected by the weight increase of the blank cup.
  • JIS Z 0208 states that "the measurement must be completed before the mass of the moisture absorbent increases by 10% or more.” This is because if the mass increase of the moisture absorbent is 10% or more, the reactivity of the moisture absorbent decreases, and there is a possibility that accurate measurement cannot be performed. Since the present disclosure includes a water vapor permeable member with high moisture vapor transmission rate, the weight gain over a short period of time was evaluated so that the weight gain of the absorbent material did not exceed 10%. In addition, in order to confirm that the mass increase is constant, the mass increase for 1 hour up to 1 hour after standing in the constant temperature and humidity device, and 1 hour from 1 hour to 2 hours after standing still.
  • the moisture permeability was calculated by the following formula (6) based on the mass increase for 1 hour from 1 hour to 2 hours after standing.
  • Moisture permeability (g/( m2 ⁇ 24h)) 240 ⁇ m/(t ⁇ s) (6)
  • s Moisture permeable area (cm 2 )
  • t sum of the time (h) of the last two weighing intervals in which the measurements were made. 1 hour for this disclosure.
  • m sum of mass increments (mg) over the last two weighing intervals in which the measurement was made. Mass gained in 1 hour from 1 hour to 2 hours in the present disclosure.
  • the heat storage structure of the present disclosure can prevent the chemical heat storage material from flowing out of the sealed container during hydration and/or dehydration, it can theoretically be used repeatedly any number of times.
  • the generated heat is transmitted to the sealed container and warms the sealed container. In addition to contact heating, there are other ways of warming. If the moisture added for the hydration reaction is liquid water, the hydration rate with the chemical heat storage material is faster than steam, and heat is generated rapidly. Steam can be used to heat objects. When the moisture added for the hydration reaction is water vapor, the water vapor is warmed by the reaction with the chemical heat storage material, and the water vapor functions as warm air. can be done.
  • FIG. 2 is a schematic diagram showing the configuration of another embodiment of the heat storage structure of the present disclosure.
  • the sealed container is composed of the chemical heat storage material 4 of the present disclosure, the sealed container main body 5 and the water vapor permeable member 6 described above.
  • the sealed container can also be configured to partially include the water vapor permeable member. It can be used as a heat storage structure by allowing water vapor to flow in and out of the water vapor permeable member.
  • the sealed container main body may be a member impermeable to water vapor, but may be a water vapor permeable member.
  • FIG. 3 is a schematic diagram showing the configuration of one embodiment of the heat storage system of the present disclosure.
  • the present embodiment includes a heat storage device 13 having the heat storage structure of the present disclosure described above, a blower 7 and a water storage tank 8 as a water vapor supplier for performing a hydration reaction, water 9, and heat supply for performing a dehydration reaction. It is composed of a hot air generator 10 as a machine, a heating chamber 11 using heat generated from a heat accumulator, and a hot air outlet 12 .
  • the procedure for generating heat in FIG. 3 is, for example, as follows.
  • the heat accumulator 13 includes a heat storage structure having a chemical heat storage material in a heat storage state in a form capable of supplying steam sent from a steam supply device to the chemical heat storage material.
  • the heat storage device 13 may be newly provided with a heat storage structure having a chemical heat storage material in a heat storage state, or a heat storage structure having a chemical heat storage material in a state in which heat has already been generated (hereinafter referred to as a non-heat storage state). may be brought into a heat storage state in a heat storage procedure described later.
  • the procedure for heat storage in FIG. 3 is, for example, as follows.
  • the heat accumulator 13 is provided with a heat storage structure having a chemical heat storage material in an unstored state so that the heat sent from the heat supply device can be supplied to the chemical heat storage material.
  • the heat accumulator 13 may be newly provided with a heat storage structure having a chemical heat storage material in a non-heat-storing state, or the heat storage structure having a chemical heat storage material in a heat-storing state may be subjected to the above-described heat generation procedure to obtain a chemical heat storage material. may be set to an unheated state. After that, hot air is generated by the hot air generator 10 and sent to the heat accumulator 13 .
  • the chemical heat storage material in the heat storage structure of the heat accumulator 13 undergoes a dehydration reaction.
  • the dehydration reaction brings the chemical heat storage material into a heat storage state.
  • the water vapor generated by the dehydration reaction may be condensed in a water tank and used for the hydration reaction. Using unused heat from the factory as the heat source for dehydration leads to effective utilization of heat.
  • Example 1 (Preparation of heat storage structure) A heat storage structure was produced by putting 0.200 g of the chemical heat storage material MgSO 4 .7H 2 O into a PTFE three-sided bag of 23 mm ⁇ 23 mm ⁇ t 0.1 mm as a sealed container, and sealing the opening by welding a PFA film. .
  • the outflow prevention effect of the chemical heat storage material of the produced heat storage structure was evaluated by performing the above-described dehydration and hydration. As evaluation indexes, the sealing state of the sealed container and the seepage of water from the surface of the sealed container were used. Each evaluation criterion was defined as follows. Confirmation of the sealed state of the sealed container was an evaluation of whether or not the water vapor generated from the chemical heat storage material during dehydration could be discharged out of the sealed container. The confirmation of the seepage of water was determined by the color of the cobalt chloride paper when the heat storage structure was taken out from the thermo-hygrostat and the cobalt chloride paper was brought into contact with the surface of the sealed container.
  • Examples 2 to 47 0.200 g of the chemical heat storage material listed in Table 1-1 or Table 1-2 is placed in a three-sided bag of 23 mm ⁇ 23 mm (thickness varies depending on material and moisture permeability) as a sealed container, and the opening is thermocompression bonded.
  • a heat storage structure was produced by sealing with a hot-melt agent or a heat-resistant adhesive tape (API-214A from Chuko Kasei Kogyo Co., Ltd.).
  • the moisture-permeable film made of the materials listed in Table 1-1 or Table 1-2 was used, and even if the material was the same, the moisture permeability was adjusted by adjusting the thickness and pore size.
  • the material is crystalline resin, it is produced by the biaxial stretching method, and each raw material is made into a paste at a temperature above the glass transition point and below the melting point, and after extrusion molding, it is stretched perpendicular to the extrusion direction to create a water vapor permeable member. was made. The thickness and pore size were controlled by controlling the stretching temperature and stretching ratio.
  • non-crystalline resin such as PI
  • PI non-crystalline resin
  • a paste that is a mixture of each raw material and fine particles such as silica is applied and molded into a film.
  • a water vapor-permeable member was produced by removing the fine particles.
  • the thickness of the water vapor permeable member was adjusted according to the thickness of the molded body, and the porosity was adjusted according to the size and addition rate of the fine particles to be removed.
  • the fabricated heat storage structure is dehydrated in an electric furnace at a temperature higher than the dehydration temperature of water in the heat storage material and lower than the heat resistance temperature of the sealed container, and then a hydration reaction is performed under hydration conditions suitable for each chemical heat storage material. , evaluated the outflow prevention effect of the chemical heat storage material. The results are shown in Tables 1-1 and 1-2.
  • PTFE is polytetrafluoroethylene resin
  • PI is polyimide resin
  • PP is polypropylene resin
  • PE is polyethylene resin
  • TPU is thermoplastic polyurethane resin
  • PEEK is polyether.
  • a heat storage structure having a sealed container and a chemical heat storage material sealed in the sealed container,
  • the sealed container includes at least a portion of a water vapor permeable member
  • the chemical heat storage material is A group consisting of magnesium oxide, magnesium hydroxide, and at least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead.
  • the chemical heat storage material is a substance that generates heat by a hydration reaction and/or stores heat by a dehydration reaction
  • a heat storage structure wherein the moisture permeability of the water vapor permeable member is 200 to 10000 g/(m 2 ⁇ 24 h).
  • Configuration 2 The heat storage structure according to configuration 1, wherein the heat resistant temperature of the sealed container is 70°C or higher and 700°C or lower.
  • Composition 3 The heat storage structure according to configuration 1 or 2, wherein the water vapor permeable member comprises a resin.
  • composition 4 The heat storage structure according to configuration 3, wherein the resin includes at least one selected from the group consisting of fluororesin, polyimide resin, silicone resin, polyetheretherketone resin, polyphenylene sulfide resin and polyester resin.
  • Composition 5 A heat storage structure according to configuration 3 or 4, wherein the resin comprises polytetrafluoroethylene resin.
  • Composition 6) The heat storage structure according to any one of configurations 1 to 5, wherein the sealed container is a film.
  • composition 7 At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead is carbonate, phosphate, sulfate, nitrate and silicate
  • the heat storage structure according to any one of configurations 1 to 6, comprising at least one selected from the group consisting of salts.
  • a heat storage structure according to claim 1.
  • Composition 9 A heat storage system comprising a steam supplier for performing a hydration reaction, a heat supplier for performing a dehydration reaction, and a heat accumulator,
  • the heat storage device has a heat storage structure according to any one of configurations 1 to 8, heat is sent to the heat accumulator by the heat supplier;
  • the chemical heat storage material contained in the heat storage structure undergoes a dehydration reaction with the heat sent to the heat accumulator, whereby heat is stored in the chemical heat storage material, Further, steam is sent to the heat accumulator by the steam supplier,
  • the heat stored in the chemical heat storage material is extracted by a hydration reaction of the chemical heat storage material contained in the heat storage structure. heat storage system.

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Abstract

Provided is a heat storage structure with which it is possible to prevent outflow of a chemical heat storage material due to the chemical heat storage material being flushed away or blown away by a reaction medium, and with which heat storage or an exothermic reaction can be stably carried out. This heat storage structure has a sealed container and a chemical heat storage material sealed in the sealed container, and is characterized in that: the sealed container includes a water vapor-permeable member in at least a part thereof; the chemical heat storage material contains magnesium oxide, magnesium hydroxide and at least one type of substance selected from the group consisting of at least a halide, an organic salt, or an inorganic salt selected from the group consisting of an alkali metal, an alkaline earth metal, aluminum, manganese, iron, nickel, copper, zinc and lead; this substance generates heat through a hydration reaction and/or stores heat through a dehydration reaction; and the moisture permeability of the water vapor-permeable member is 200-10,000 g/(m2·24h).

Description

蓄熱構造体、および蓄熱システムThermal storage structure and thermal storage system

 本開示は蓄熱構造体、および蓄熱システムに関する。 The present disclosure relates to heat storage structures and heat storage systems.

 地球温暖化対策として省資源、省エネルギー化が求められており、近年では工場から排出される排熱(排ガス熱量)に注目した未利用熱活用技術の開発・導入が活発化している。未利用熱活用技術の一つとして、蓄熱技術は、未利用熱を蓄えることによって熱を必要とする時間や場所を選んで発熱することができるため、エネルギーの有効利用に大きく貢献できると期待されている。  There is a demand for resource saving and energy saving as a countermeasure against global warming, and in recent years, the development and introduction of unused heat utilization technology focusing on the waste heat (exhaust gas heat quantity) emitted from factories has become active. As one of the unused heat utilization technologies, heat storage technology is expected to contribute greatly to the effective use of energy because it can store unused heat and select the time and place where heat is required. ing.

 蓄熱技術は一般的に、物質の比熱を利用した顕熱蓄熱、物質の状態変化を利用した潜熱蓄熱、物質の化学変化を利用した化学蓄熱、の3つがある。なかでも化学蓄熱は、蓄熱材が水やアンモニアなどの特定の反応媒体と反応して熱を発生し、熱の発生後は加熱されることによって反応媒体が脱離して、元の蓄熱材に戻るという特性を利用しており、この特性から反応媒体を供給しない限り蓄熱状態(反応媒体があれば発熱可能な状態)を維持できるため、化学蓄熱は長期間の蓄熱に適している。 There are generally three types of heat storage technology: sensible heat storage that uses the specific heat of substances, latent heat storage that uses changes in the state of substances, and chemical heat storage that uses chemical changes in substances. Among them, in chemical heat storage, the heat storage material reacts with a specific reaction medium such as water or ammonia to generate heat. Chemical heat storage is suitable for long-term heat storage because it can maintain a heat storage state (a state where heat can be generated if there is a reaction medium) unless a reaction medium is supplied.

特開2007-302844号公報JP 2007-302844 A

 化学蓄熱は化学反応に伴う一連の現象を加味した上で蓄熱および発熱の安定した仕組みを作らなければならず、様々な課題を抱えている。例えば、反応媒体によって発熱反応を起こすと、各蓄熱材粒子の表面エネルギーを減少させようとして蓄熱材粒子同士が凝集し、それに伴って反応媒体との接触面積が減少するため、反応性が低下するという課題があった。
 上記の課題に対して、特許文献1では、水分子が透過可能な細孔を有した第2の化合物で蓄熱材料を覆うことによって、蓄熱材同士の凝集を抑制し、反応性の低下を少なくする吸放熱材料が開示されている。
Chemical heat storage must create a stable mechanism for heat storage and heat generation after considering a series of phenomena accompanying chemical reactions, and has various problems. For example, when an exothermic reaction is caused by a reaction medium, the particles of the heat storage material agglomerate in an attempt to reduce the surface energy of each particle of the heat storage material. There was a problem.
In order to address the above problem, in Patent Document 1, the heat storage material is covered with a second compound having pores through which water molecules can pass, thereby suppressing the aggregation of the heat storage material and reducing the decrease in reactivity. A heat-absorbing and heat-absorbing material is disclosed.

 しかしながら、特許文献1に記載された解決手段では、蓄熱材料が微小粒子の集合体であるために、反応媒体が液体であれば流されてしまう恐れがある。また、反応媒体が気体であれば蓄熱材料が舞いやすく吹き飛ばされてしまう恐れがある。このように、蓄熱材料が反応媒体によって流出してしまう恐れがある。また、蓄熱材料を第2の化合物で覆う工程では使用する材料や工程の調整が必要となり、より簡便な方法が望まれている。 However, in the solution described in Patent Document 1, the heat storage material is an aggregate of fine particles, so if the reaction medium is liquid, there is a risk that it will be washed away. Also, if the reaction medium is a gas, the heat storage material tends to dance and may be blown away. Thus, the heat storage material may be washed away by the reaction medium. In addition, in the step of covering the heat storage material with the second compound, it is necessary to adjust the materials used and the process, and a simpler method is desired.

 本開示は、化学蓄熱材が反応媒体によって流されることや、吹き飛ばされることなどによる化学蓄熱材の流出を防ぎ、蓄熱または発熱反応を安定して行える蓄熱構造体を提供するものである。 The present disclosure provides a heat storage structure that prevents the outflow of the chemical heat storage material due to the chemical heat storage material being swept away or blown away by the reaction medium, and capable of stably storing heat or exothermic reaction.

 本開示は、封止容器及び前記封止容器に封止された化学蓄熱材を有する蓄熱構造体であって、
 前記封止容器は、水蒸気透過部材を少なくとも一部に含み、
 前記化学蓄熱材は、
  酸化マグネシウム、水酸化マグネシウム、並びに
  アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩、有機塩及びハロゲン化物
 からなる群から選択される少なくとも一を含み、
 前記化学蓄熱材は水和反応により発熱し、および/または脱水反応により蓄熱する物質であり、
 前記水蒸気透過部材の透湿度が、200~10000g/(m・24h)であることを特徴とする、蓄熱構造体に関する。
The present disclosure is a heat storage structure having a sealed container and a chemical heat storage material sealed in the sealed container,
The sealed container includes at least a portion of a water vapor permeable member,
The chemical heat storage material is
A group consisting of magnesium oxide, magnesium hydroxide, and at least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead. including at least one selected from
The chemical heat storage material is a substance that generates heat by a hydration reaction and/or stores heat by a dehydration reaction,
The heat storage structure is characterized in that the moisture permeability of the water vapor permeable member is 200 to 10000 g/(m 2 ·24 h).

 また、本開示は、水和反応を行うための水蒸気供給機、脱水反応を行うための熱供給機、及び蓄熱器を備える蓄熱システムであって、
 前記蓄熱器が、本開示の蓄熱構造体を有し、
 前記熱供給機によって、前記蓄熱器に熱が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が、前記蓄熱器に送られた熱によって脱水反応を行うことで前記化学蓄熱材に蓄熱が行われ、
 また、前記水蒸気供給機によって、前記蓄熱器に水蒸気が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が水和反応を行うことによって化学蓄熱材に蓄熱された熱が取り出される、
 蓄熱システムに関する。
Further, the present disclosure is a heat storage system comprising a steam supplier for performing a hydration reaction, a heat supplier for performing a dehydration reaction, and a heat accumulator,
wherein the heat storage device comprises the heat storage structure of the present disclosure;
heat is sent to the heat accumulator by the heat supplier;
The chemical heat storage material contained in the heat storage structure undergoes a dehydration reaction with the heat sent to the heat accumulator, whereby heat is stored in the chemical heat storage material,
Further, steam is sent to the heat accumulator by the steam supplier,
The heat stored in the chemical heat storage material is extracted by a hydration reaction of the chemical heat storage material contained in the heat storage structure.
It relates to a heat storage system.

 本開示によれば、化学蓄熱材が反応媒体によって流出することを防ぎ、蓄熱または発熱反応を安定して行える蓄熱構造体を提供することができる。 According to the present disclosure, it is possible to provide a heat storage structure that can prevent the chemical heat storage material from flowing out due to the reaction medium and stably store heat or generate heat.

蓄熱構造体の一実施形態における構成を示す概略図Schematic diagram showing the configuration in one embodiment of the heat storage structure 蓄熱構造体の一実施形態における構成を示す概略図Schematic diagram showing the configuration in one embodiment of the heat storage structure 蓄熱システムの一実施形態における構成を示す概略図Schematic diagram showing the configuration in one embodiment of the heat storage system

 以下、好適な実施の形態を挙げて、本開示にかかる蓄熱構造体、及び蓄熱システムの実施形態を説明する。また、本開示は下記実施形態に限定されるわけではない。
 また、本開示において、数値範囲を表す「X以上Y以下」や「X~Y」の記載は、特に断りのない限り、端点である下限及び上限を含む数値範囲を意味する。数値範囲が段階的に記載されている場合、各数値範囲の上限及び下限は任意に組み合わせることができる。
 さらに、本開示の化学蓄熱材において、「酸化マグネシウム」や「無機塩」などの記載は、特に断りのない限り、無水物および任意の水和数を有する水和物を指すものとする。
Hereinafter, embodiments of a heat storage structure and a heat storage system according to the present disclosure will be described with reference to preferred embodiments. Moreover, the present disclosure is not limited to the following embodiments.
Further, in the present disclosure, unless otherwise specified, the descriptions of “X or more and Y or less” or “X to Y” representing a numerical range mean a numerical range including the lower limit and the upper limit, which are endpoints. When numerical ranges are stated stepwise, the upper and lower limits of each numerical range can be combined arbitrarily.
Furthermore, in the chemical heat storage material of the present disclosure, descriptions such as “magnesium oxide” and “inorganic salt” refer to anhydrides and hydrates having arbitrary hydration numbers unless otherwise specified.

 図1は、蓄熱構造体の一実施形態における構成を示す概略図を示している。蓄熱構造体は、化学蓄熱材1と、化学蓄熱材を封止する封止容器2から形成される。該封止容器は、液体の水は通さないが水蒸気は通す性質(以下、このような性質を「透湿性」という。また、透湿性を持つ物質が水蒸気を通す度合いを「透湿度」という。)を有する水蒸気透過部材を少なくとも一部に含む。封止容器2は、水蒸気透過部材を少なくとも一部に含んでいればよい。封止容器2は、全体が水蒸気透過部材により形成されていてもよい。図1の蓄熱構造体は、封止容器2が水蒸気透過部材で形成されている。 FIG. 1 shows a schematic diagram showing the configuration of one embodiment of the heat storage structure. The heat storage structure is formed from a chemical heat storage material 1 and a sealed container 2 that seals the chemical heat storage material. The sealed container has a property of impermeable to liquid water but permeable to water vapor (such property is hereinafter referred to as "moisture permeability". The degree to which a substance having moisture permeability allows water vapor to pass is referred to as "moisture permeability". ) at least in part. The sealed container 2 may include at least a portion of the water vapor permeable member. The sealed container 2 may be entirely made of a water vapor permeable member. In the heat storage structure of FIG. 1, the sealed container 2 is made of a water vapor permeable member.

 化学蓄熱材1は、水和反応により発熱し、および/または脱水反応により蓄熱する物質であり、酸化マグネシウム、水酸化マグネシウム、並びにアルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩、有機塩及びハロゲン化物からなる群から選択される少なくとも一を含む。中でも、脱水反応を起こす温度が200℃以下であるものが好ましい。脱水反応を起こす温度が200℃以下であることで、工場の未利用熱を熱源として用いることができ、熱の有効利用に繋げることができる。
 化学蓄熱材は、質量あたりの蓄熱量が多いという観点から、酸化マグネシウム、硫酸マグネシウムからなる群から選択される少なくとも一を含むことが特に好ましい。
The chemical heat storage material 1 is a substance that generates heat by hydration reaction and/or stores heat by dehydration reaction, and is composed of magnesium oxide, magnesium hydroxide, alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, and copper. , at least one inorganic salt selected from the group consisting of zinc and lead, at least one selected from the group consisting of organic salts and halides. Among them, those having a dehydration reaction temperature of 200° C. or less are preferable. Since the temperature at which the dehydration reaction occurs is 200° C. or less, unused heat in the factory can be used as a heat source, leading to effective utilization of heat.
The chemical heat storage material particularly preferably contains at least one selected from the group consisting of magnesium oxide and magnesium sulfate from the viewpoint of having a large heat storage amount per mass.

 化学蓄熱材が含みうるアルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩、有機塩及びハロゲン化物としては、水和反応により発熱し、および/または脱水反応により蓄熱するものであれば特に限定されるものではない。
 ここで、アルカリ金属とは、リチウム、ナトリウム、カリウム、ルビジウム、セシウム及びフランシウムを指す。また、アルカリ土類金属とは、ベリリウム、マグネシウム、カルシウム、ストロンチウム、バリウム及びラジウムを指す。アルカリ金属としては、リチウム及びナトリウムが好ましく、アルカリ土類金属としては、マグネシウム及びカルシウムが好ましい。
At least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead that can be contained in the chemical heat storage material include hydrated It is not particularly limited as long as it generates heat by the reaction and/or accumulates heat by the dehydration reaction.
Here, alkali metals refer to lithium, sodium, potassium, rubidium, cesium and francium. Alkaline earth metals refer to beryllium, magnesium, calcium, strontium, barium and radium. Preferred alkali metals are lithium and sodium, and preferred alkaline earth metals are magnesium and calcium.

 アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩としては、炭酸塩、リン酸塩、硫酸塩、硝酸塩、ケイ酸塩からなる群から選択される少なくとも一を含むことが好ましい。また、NaCO・xHO(x=0~10)、NaPO・yHO(y=0~12)及びMgSO・zHO(z=0~7)からなる群から選択される少なくとも一を含むことがより好ましい。 At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead includes carbonates, phosphates, sulfates, nitrates, silicates It preferably contains at least one selected from the group consisting of salts. and the group consisting of Na 2 CO 3.xH 2 O (x=0-10), Na 3 PO 4.yH 2 O (y=0-12) and MgSO 4.zH 2 O (z=0-7). It is more preferable to include at least one selected from

 前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩の例としては、炭酸塩としては炭酸カルシウムや炭酸バリウムなど、リン酸塩としてはリン酸マグネシウムやリン酸ナトリウムなど、硫酸塩としては硫酸ナトリウムや硫酸マグネシウムなど、硝酸塩としては硝酸マグネシウムや硝酸アルミニウムなど、ケイ酸塩としてはケイ酸マグネシウムやケイ酸カルシウムなどが挙げられる。
 前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の有機塩の例としては、ギ酸塩、酢酸塩、オクチル酸塩などの脂肪酸塩、フタル酸塩や安息香酸塩などの芳香族カルボン酸塩、p-トルエンスルホン酸塩、エタンスルホン酸塩などのスルホン酸塩などが挙げられる。中でも、酢酸塩が好ましい。酢酸塩としては、酢酸ナトリウム、酢酸カルシウム、酢酸マグネシウム、酢酸ニッケル、酢酸銅、酢酸亜鉛、酢酸鉛などが挙げられる。
 前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一のハロゲン化物の例としては、フッ化マグネシウム、フッ化カルシウムなどのフッ化物、塩化マグネシウム、塩化カルシウムなどの塩化物、臭化マグネシウム、臭化カルシウムなどの臭化物、ヨウ化マグネシウム、ヨウ化カルシウムなどのヨウ化物が挙げられる。中でも、塩化マグネシウムまたは塩化カルシウムが好ましい。
Examples of at least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include carbonates such as calcium carbonate and barium carbonate; Phosphates include magnesium phosphate and sodium phosphate, sulfates include sodium sulfate and magnesium sulfate, nitrates include magnesium nitrate and aluminum nitrate, and silicates include magnesium silicate and calcium silicate. be done.
Examples of at least one organic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include formates, acetates, octylates and the like. Examples include fatty acid salts, aromatic carboxylic acid salts such as phthalates and benzoates, and sulfonates such as p-toluenesulfonates and ethanesulfonates. Among them, acetate is preferred. Acetates include sodium acetate, calcium acetate, magnesium acetate, nickel acetate, copper acetate, zinc acetate, lead acetate and the like.
Examples of at least one halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead include fluorides such as magnesium fluoride and calcium fluoride , chlorides such as magnesium chloride and calcium chloride, bromides such as magnesium bromide and calcium bromide, and iodides such as magnesium iodide and calcium iodide. Among them, magnesium chloride or calcium chloride is preferred.

 水和反応によって蓄熱する化学蓄熱材は、水和反応によって水酸化物を形成する化学蓄熱材と、水和物を形成する化学蓄熱材の2つに分けられる。水酸化物を形成する化学蓄熱材では、例えば、式(1)に示すような水和反応によって発熱し、式(2)に示すような脱水反応によって蓄熱する。
MgO + HO →Mg(OH)         (1)
Mg(OH) →MgO + HO         (2)
A chemical heat storage material that stores heat by a hydration reaction is classified into a chemical heat storage material that forms a hydroxide by a hydration reaction and a chemical heat storage material that forms a hydrate. A chemical heat storage material that forms a hydroxide, for example, generates heat by a hydration reaction as shown in formula (1) and stores heat by a dehydration reaction as shown in formula (2).
MgO+ H2O →Mg(OH) 2 (1)
Mg(OH) 2 →MgO+ H2O (2)

 水和物を形成する化学蓄熱材では、例えば、式(3)に示すような水和反応によって発熱し、式(4)に示すような脱水反応によって蓄熱する。ただし、特定の水和数間での反応に限定されるものではない。例えば、水和数1から水和数6に増える反応によって発熱してもよいし、水和数4から水和数2に減る反応によって蓄熱してもよい。
MgSO + 7HO →MgSO・7HO       (3)
MgSO・7HO →MgSO + 7HO       (4)
A chemical heat storage material that forms a hydrate, for example, generates heat by a hydration reaction as shown in formula (3) and stores heat by a dehydration reaction as shown in formula (4). However, it is not limited to reactions between specific hydration numbers. For example, heat may be generated by a reaction that increases the hydration number from 1 to 6, or heat may be accumulated by a reaction that reduces the hydration number from 4 to 2.
MgSO4 + 7H2OMgSO4.7H2O (3 )
MgSO4.7H2OMgSO4 + 7H2O ( 4)

 化学蓄熱材の中には水への溶解度が高く、水和反応を行う過程や脱水反応を行う過程で溶解してしまう物質もある。水和反応中の溶解は水和反応のために付与した水に起因し、脱水反応中の溶解は化学蓄熱材自身から脱離した水分によって発生する。そのような物質としては、例えば、MgSO・7HOやカリウムミョウバンKAl(SO・12HO、チオ硫酸ナトリウムNa・5HO、炭酸ナトリウムNaCO・10HOが挙げられる。化学蓄熱材が溶解して化学蓄熱材水溶液になる場合に、本開示の蓄熱構造体では化学蓄熱材が封止容器に封止されており、かつ封止容器は所定の透湿度を有する水蒸気透過部材を少なくとも一部に含むことから、化学蓄熱材水溶液が封止容器から流出することはないため、本開示はそのような場合に特に有効である。 Some chemical heat storage materials have high solubility in water and dissolve during the process of hydration reaction or dehydration reaction. The dissolution during the hydration reaction is caused by the water added for the hydration reaction, and the dissolution during the dehydration reaction is caused by the moisture desorbed from the chemical heat storage material itself. Examples of such substances include MgSO4.7H2O , potassium alum KAl ( SO4 ) 2.12H2O , sodium thiosulfate Na2S2O3.5H2O , sodium carbonate Na2CO3 . 10H2O can be mentioned. When the chemical heat storage material dissolves into a chemical heat storage material aqueous solution, in the heat storage structure of the present disclosure, the chemical heat storage material is sealed in a sealed container, and the sealed container is permeable to water vapor having a predetermined moisture permeability. Since the member is included in at least a part thereof, the chemical heat storage medium aqueous solution does not flow out of the sealed container, so the present disclosure is particularly effective in such a case.

 化学蓄熱材の形態については、化学蓄熱材が水和反応することができれば特に限定はされないが、水分との反応性が高くなるように表面積の大きい粉状、顆粒状であることが好ましく、多孔質であることがより好ましい。 The form of the chemical heat storage material is not particularly limited as long as the chemical heat storage material can undergo a hydration reaction. Quality is more preferred.

 化学蓄熱材の水和反応について、水和反応のために付与する水分は液体の水でもよいし、水蒸気でもよい。ただし、水蒸気を用いる場合には、封止容器が水蒸気透過部材を少なくとも一部に有するため、封止容器が開閉できない構造でもよく、液体の水を用いる場合には、封止容器の一部が開閉できる構造になっていることが好ましい。
 本実施形態の蓄熱構造体の使用方法の一例として、封止容器に封止された蓄熱状態の化学蓄熱材に対し、封止容器の一部を開封して液体の水を注ぎ、すぐに封止容器を閉じる。水を注ぐと水和反応による発熱が始まる。また、反応後も化学蓄熱材が流出しないため、化学蓄熱材を脱水して蓄熱状態に戻せば繰り返し使用が可能である。
 他の使用方法の一例として、水蒸気を用いる場合では、封止容器の外から水蒸気を供給して化学蓄熱材に水和反応による発熱をさせる。反応後も化学蓄熱材が流出しないため、脱水して蓄熱状態に戻せば繰り返し使用が可能である。水蒸気を用いる場合でも、水和および脱水時に封止されていれば封止容器の一部が開閉可能な構造を有していてもよい。
 他の使用方法としては、例えば液体の水と水蒸気を併用してもよい。
 反応媒体に関わらず、化学蓄熱材からの発熱は繰り返しできるが、1度きりで使っても構わない。
Regarding the hydration reaction of the chemical heat storage material, the moisture applied for the hydration reaction may be liquid water or water vapor. However, when using water vapor, the sealed container has a water vapor permeable member at least in part, so the sealed container may have a structure that cannot be opened and closed. It is preferable to have a structure that can be opened and closed.
As an example of a method of using the heat storage structure of the present embodiment, a part of the sealed container is opened, liquid water is poured into the chemical heat storage material in the heat storage state sealed in the sealed container, and the sealed container is immediately sealed. Close the stop container. Heat generation due to hydration reaction begins when water is poured. In addition, since the chemical heat storage material does not flow out even after the reaction, it can be used repeatedly if the chemical heat storage material is dehydrated and returned to the heat storage state.
As an example of another usage method, when steam is used, steam is supplied from the outside of the sealed container to cause the chemical heat storage material to generate heat due to a hydration reaction. Since the chemical heat storage material does not flow out even after the reaction, it can be used repeatedly if it is dehydrated and returned to the heat storage state. Even when water vapor is used, a part of the sealed container may have a structure that can be opened and closed as long as it is sealed during hydration and dehydration.
Other methods of use include, for example, liquid water and water vapor.
Heat generation from the chemical heat storage material can be repeated regardless of the reaction medium, but it may be used only once.

 化学蓄熱材の脱水反応について、化学蓄熱材に熱を加えられる方法であれば特に限定されるものではないが、脱水反応の温度を200℃以下とすることが好ましい。脱水反応の温度が200℃以下であることで、工場の未利用熱を熱源として用いることができ、熱の有効利用に繋げることができる。
 脱水反応は化学蓄熱材を封止容器に封止した状態で行ってもよいし、化学蓄熱材のみを脱水した後に封止容器に封止してもよい。
The dehydration reaction of the chemical heat storage material is not particularly limited as long as it can apply heat to the chemical heat storage material, but the temperature of the dehydration reaction is preferably 200° C. or less. Since the temperature of the dehydration reaction is 200° C. or less, unused heat in the factory can be used as a heat source, which leads to effective utilization of heat.
The dehydration reaction may be performed with the chemical heat storage material sealed in a sealed container, or only the chemical heat storage material may be dehydrated and then sealed in the sealed container.

 封止容器2は化学蓄熱材を封止する。封止容器に化学蓄熱材を封止することによって、化学蓄熱材が封止容器から流出しないという効果が得られる。ここで、「封止容器に化学蓄熱材を封止する」とは、化学蓄熱材の周囲を封止容器で囲い、化学蓄熱材が封止容器から流出せず、封止容器外部の水が封止容器内部に侵入することができない状態にすることをいう。もちろん、封止容器に封止を解除することができるような機構を設けることを妨げるものではない。 The sealed container 2 seals the chemical heat storage material. By sealing the chemical heat storage material in the sealed container, an effect is obtained that the chemical heat storage material does not flow out of the sealed container. Here, "sealing the chemical heat storage material in the sealed container" means that the chemical heat storage material is surrounded by the sealed container, the chemical heat storage material does not flow out of the sealed container, and water outside the sealed container It refers to making it impossible to enter the inside of the sealed container. Of course, this does not preclude providing the sealed container with a mechanism capable of releasing the seal.

 封止容器の材質は特に限定されるものではないが、使用温度に耐えられる材質が望ましい。使用温度には、水和時に到達する最高温度と、化学蓄熱材の脱水温度、の2種類がある。化学蓄熱材を1度きりで使用する場合は、封止容器に封止する前に化学蓄熱材を脱水しておけば水和時に到達する最高温度のみに耐えられればよいが、封止容器に封止したままの状態で繰り返し使用する場合は、化学蓄熱材の脱水温度に応じた耐熱性が封止容器に求められる。 The material of the sealed container is not particularly limited, but a material that can withstand the operating temperature is desirable. There are two types of working temperatures: the maximum temperature reached during hydration and the dehydration temperature of the chemical heat storage material. If the chemical heat storage material is used only once, it should be able to withstand only the maximum temperature reached during hydration if it is dehydrated before being sealed in the sealed container. When the sealed container is used repeatedly, the sealed container is required to have heat resistance corresponding to the dehydration temperature of the chemical heat storage material.

 このような観点から、封止容器の耐熱温度は70℃以上であることが好ましく、100℃以上であることがより好ましい。また、900℃以下であることが好ましく、700℃以下であることがより好ましい。
 なお、封止容器の耐熱温度は、封止容器の融点を指し、封止容器の融点は公知の方法で測定することができる。例えば、示差走査熱量測定(DSC)や示差熱分析(DTA)などの熱分析を封止容器の一部に行うことで、封止容器の融点を測定することができる。また、封止容器の耐熱温度は、封止容器の材質を変更することによって調節することができる。
From this point of view, the heat resistance temperature of the sealed container is preferably 70° C. or higher, more preferably 100° C. or higher. Also, it is preferably 900° C. or lower, more preferably 700° C. or lower.
The heat resistant temperature of the sealed container refers to the melting point of the sealed container, and the melting point of the sealed container can be measured by a known method. For example, the melting point of the sealed container can be measured by subjecting a portion of the sealed container to thermal analysis such as differential scanning calorimetry (DSC) or differential thermal analysis (DTA). Moreover, the heat-resistant temperature of the sealed container can be adjusted by changing the material of the sealed container.

 また、化学蓄熱材の脱水温度が400℃未満の場合、封止容器の材質は樹脂、金属の多孔体、セラミックの多孔体であることが好ましく、400℃以上の場合、耐熱性の高い金属やセラミックの多孔体であることが好ましい。 When the dehydration temperature of the chemical heat storage material is less than 400°C, the material of the sealed container is preferably resin, porous metal, or porous ceramic. A ceramic porous body is preferred.

 封止容器はフィルムであることが好ましい。フィルムの厚さとしては特に限定されないが、1μm以上であることが好ましく、10μm以上であることがより好ましい。また、1mm以下であることが好ましく、250μm以下であることがより好ましい。 The sealed container is preferably a film. Although the thickness of the film is not particularly limited, it is preferably 1 μm or more, more preferably 10 μm or more. Moreover, it is preferably 1 mm or less, and more preferably 250 μm or less.

 封止容器は、水蒸気透過部材を少なくとも一部に含む。封止容器全体が水蒸気透過部材でもよく、図1はその例であり、封止容器全体が水蒸気透過部材として機能している。水蒸気透過部材は、透湿性を有する。
 水蒸気透過部材は、化学蓄熱材を保持しつつ水和および/または脱水反応を起こすために、透湿性を有するものであり、水蒸気透過部材の透湿度は200~10000g/(m・24h)である。
 水蒸気透過部材の透湿度が上記範囲になるような透湿性を有していることで、水蒸気透過部材が液体の水を透過させず、水蒸気を透過させる効果が得られる。そのため、反応媒体として水を用いる場合にも、化学蓄熱材が流出することがないという効果が得られる。また、反応媒体として水蒸気を用いることができる。加えて、水蒸気によって化学蓄熱材が吹き飛ばされることがない。さらに、水への溶解度が高い化学蓄熱材が、水和反応を行う過程や脱水反応を行う過程で、封止容器の中で溶解してしまっても封止容器の外に流出することがない。
 水蒸気透過部材の透湿度が200g/(m・24h)未満であると、脱水時に蓄熱材から発生する水蒸気が封止容器の外に逃げられず、封止容器内の圧力が高くなり封止容器の封止が破れやすくなる。
 また、水蒸気透過部材の透湿度が10000g/(m・24h)より高いと水蒸気透過部材の耐水圧が低くなり、液化した蓄熱材が水蒸気透過部材の表面に染み出してくる恐れがある。
The sealed container includes at least a portion of the water vapor permeable member. The entire sealed container may be a water vapor permeable member, and FIG. 1 is an example thereof, and the entire sealed container functions as a water vapor permeable member. The water vapor permeable member has moisture permeability.
The water vapor permeable member has moisture permeability in order to cause a hydration and/or dehydration reaction while retaining the chemical heat storage material. be.
When the moisture permeability of the water vapor permeable member is within the above range, the effect of the water vapor permeable member not permeating liquid water but permeating water vapor can be obtained. Therefore, even when water is used as the reaction medium, an effect is obtained that the chemical heat storage material does not flow out. Steam can also be used as the reaction medium. In addition, the chemical heat storage material is not blown off by water vapor. Furthermore, even if the chemical heat storage material, which is highly soluble in water, dissolves in the sealed container during the process of hydration reaction or dehydration reaction, it will not flow out of the sealed container. .
If the moisture permeability of the water vapor permeable member is less than 200 g/(m 2 ·24 h), the water vapor generated from the heat storage material during dehydration cannot escape outside the sealed container, and the pressure inside the sealed container increases, resulting in sealing. The container seal is easily broken.
Further, if the water vapor permeability of the water vapor permeable member is higher than 10000 g/(m 2 ·24 h), the water pressure resistance of the water vapor permeable member becomes low, and there is a risk that the liquefied heat storage material will seep out onto the surface of the water vapor permeable member.

 水蒸気透過部材の透湿度は、脱水時に発生した水蒸気を円滑に封止容器の外へ排出できるように2000~9800g/(m・24h)が好ましい。これによって、封止容器の内圧上昇に伴う封止容器の封止破れを防ぐ効果が得られる。さらに、水蒸気の取り込み量を多くして水和反応を促進するように5000~9600g/(m・24h)がより好ましい。
 水蒸気透過部材の透湿性を調整する方法は特に限定されないが、例えば、水蒸気透過部材に細孔3を有させてもよい。
The moisture permeability of the water vapor permeable member is preferably 2000 to 9800 g/(m 2 ·24 h) so that water vapor generated during dehydration can be smoothly discharged to the outside of the sealed container. As a result, it is possible to obtain the effect of preventing the sealing of the sealed container from breaking due to an increase in the internal pressure of the sealed container. Furthermore, it is more preferably 5000 to 9600 g/(m 2 ·24 h) so as to increase the intake of water vapor and promote the hydration reaction.
Although the method for adjusting the moisture permeability of the water vapor permeable member is not particularly limited, for example, the water vapor permeable member may have pores 3 .

 水蒸気透過部材の細孔3の直径は、水蒸気透過部材の透湿度が上記の範囲になれば特に限定されるものではない。気体状の水分子の大きさが0.38nm、液体状の水粒子の大きさが100μm~3000μmであるため、気体状の水分子を透過し、液体状の水分子を透過させないという観点から、0.38nm以上であることが好ましく、100μm以下であることが好ましい。なお、水蒸気透過部材表面の撥水性や耐水圧によって適切な細孔のサイズは異なるため、この限りではない。 The diameter of the pores 3 of the water vapor permeable member is not particularly limited as long as the water vapor permeability of the water vapor permeable member is within the above range. Since the size of gaseous water molecules is 0.38 nm and the size of liquid water particles is 100 μm to 3000 μm, from the viewpoint of permeation of gaseous water molecules and not permeation of liquid water molecules, It is preferably 0.38 nm or more, and preferably 100 μm or less. However, this is not the case because the appropriate pore size differs depending on the water repellency and water pressure resistance of the surface of the water vapor permeable member.

 水蒸気透過部材の材質は、上記透湿度を満たしていれば特に限定されるものではないが、蓄熱構造体がフレキシブルな状態となるように、水蒸気透過部材が、樹脂を含むことが好ましい。樹脂としてはポリエチレン(PE)やポリプロピレン(PP)などのポリオレフィン樹脂や、熱可塑性ポリウレタン(TPU)のようなウレタン樹脂などの可撓性を持つ樹脂が好ましく、より好ましくは耐熱温度が高いパーフルオロアルコキシアルカン(PFA)樹脂やポリテトラフルオロエチレン(PTFE)樹脂などのフッ素樹脂、ポリアミドイミド、ポリエーテルイミドなどのポリイミド(PI)、ポリジメチルシロキサン(PDMS)、シリコーンゴムなどのシリコーン樹脂、ポリエーテルエーテルケトン(PEEK)樹脂、直鎖型ポリフェニレンスルフィド、架橋型ポリフェニレンスルフィドなどのポリフェニレンスルフィド(PPS)樹脂、ポリエステル(PEs)樹脂であり、更に好ましくは高耐薬品性、高耐腐食性を有するポリテトラフルオロエチレン(PTFE)樹脂である。また、水蒸気透過部材は、フッ素コートガラスクロスのような、樹脂と、無機物などのその他の材料とを組み合わせたものであってもよい。 The material of the water vapor permeable member is not particularly limited as long as it satisfies the above moisture permeability, but it is preferable that the water vapor permeable member contains a resin so that the heat storage structure can be in a flexible state. The resin is preferably a polyolefin resin such as polyethylene (PE) or polypropylene (PP), or a flexible resin such as a urethane resin such as thermoplastic polyurethane (TPU), more preferably perfluoroalkoxy, which has a high heat resistance temperature. Fluorine resins such as alkane (PFA) resins and polytetrafluoroethylene (PTFE) resins, polyimides (PI) such as polyamideimide and polyetherimide, polydimethylsiloxane (PDMS), silicone resins such as silicone rubber, polyetheretherketone (PEEK) resin, polyphenylene sulfide (PPS) resin such as linear polyphenylene sulfide and crosslinked polyphenylene sulfide, polyester (PEs) resin, more preferably polytetrafluoroethylene having high chemical resistance and high corrosion resistance. (PTFE) resin. Also, the water vapor permeable member may be a combination of resin such as fluorine-coated glass cloth and other materials such as inorganic substances.

 「透湿度」は、一定時間に単位面積の膜状物質を通過する水蒸気量のことであり、本開示ではJIS Z 0208に準じて測定されたものである。
 具体的には、JIS L 1099の透湿カップφ60mmに、吸湿剤としてJIS K 8123の無水塩化カルシウム(標準ふるい2380μmを通過し、標準ふるい590μmを通過しないもの)35g~40gを平らに入れた。その後、封止容器から切り出した薄片を透湿カップに取り付け、封ろう剤としてオイルコンパウンドを用いて封かんし、サンプルを作製した。また、吸湿剤を透湿カップに入れないで同様の操作を行い、ブランクカップを作製した。
 上記で得られたサンプルとブランクカップを温度40±0.5℃、相対湿度90±2%、風速0.5~2.5m/sの恒温恒湿装置内に静置して、一定の時間間隔で取り出して秤量し、質量増加を測定した。サンプルの質量増加は、吸湿剤が水分を吸収したことによる吸湿剤の質量増加と薄片を含む透湿カップの質量増加の合計であるため、ブランクカップの質量増加で補正した。
 なお、JIS Z 0208では「吸湿剤の質量が10%以上増加する前に測定を終了する必要があり」と記載されている。これは、吸湿剤の質量増加が10%以上になると吸湿剤の反応性が低下し、正確な測定が行えない恐れがあるためである。
 本開示には、透湿度の高い水蒸気透過部材が含まれているため、吸湿材の質量増加が10%を超えないように短時間での質量増加を評価した。また、質量増加が一定であることを確認するため、恒温恒湿装置に静置してから1時間後までの1時間の質量増加と、静置後1時間後から2時間後までの1時間の質量増加が5%以内であることを確認して、静置後1時間後から2時間後までの1時間の質量増加を基に、下記式(6)にて透湿度を算出した。
 透湿度(g/(m・24h))=240×m/(t・s)      (6)
s:透湿面積(cm
t:測定を行った最後の二つの秤量間隔の時間の合計(h)。本開示では1時間。
m:測定を行った最後の二つの秤量間隔の増加質量の合計(mg)。本開示では1時間後から2時間後の1時間で増加した質量。
The “water vapor transmission rate” is the amount of water vapor that passes through a unit area of film-like material for a certain period of time, and is measured according to JIS Z 0208 in the present disclosure.
Specifically, 35 g to 40 g of anhydrous calcium chloride of JIS K 8123 (which passes through a standard sieve of 2380 μm but does not pass through a standard sieve of 590 μm) was placed flat in a JIS L 1099 moisture permeable cup of φ60 mm as a moisture absorbent. Thereafter, a thin piece cut out from the sealed container was attached to a moisture-permeable cup and sealed using an oil compound as a sealing wax to prepare a sample. Also, a blank cup was produced by carrying out the same operation without adding the moisture absorbent to the moisture permeable cup.
The sample and blank cup obtained above are placed in a constant temperature and humidity apparatus at a temperature of 40 ± 0.5 ° C., a relative humidity of 90 ± 2%, and a wind speed of 0.5 to 2.5 m / s for a certain period of time. It was removed at intervals and weighed to determine the weight gain. The weight increase of the sample is the sum of the weight increase of the moisture absorbent and the weight increase of the moisture permeable cup containing the flakes due to the absorption of water by the moisture absorbent, so it was corrected by the weight increase of the blank cup.
JIS Z 0208 states that "the measurement must be completed before the mass of the moisture absorbent increases by 10% or more." This is because if the mass increase of the moisture absorbent is 10% or more, the reactivity of the moisture absorbent decreases, and there is a possibility that accurate measurement cannot be performed.
Since the present disclosure includes a water vapor permeable member with high moisture vapor transmission rate, the weight gain over a short period of time was evaluated so that the weight gain of the absorbent material did not exceed 10%. In addition, in order to confirm that the mass increase is constant, the mass increase for 1 hour up to 1 hour after standing in the constant temperature and humidity device, and 1 hour from 1 hour to 2 hours after standing still. After confirming that the mass increase was within 5%, the moisture permeability was calculated by the following formula (6) based on the mass increase for 1 hour from 1 hour to 2 hours after standing.
Moisture permeability (g/( m2・24h))=240×m/(t・s) (6)
s: Moisture permeable area (cm 2 )
t: sum of the time (h) of the last two weighing intervals in which the measurements were made. 1 hour for this disclosure.
m: sum of mass increments (mg) over the last two weighing intervals in which the measurement was made. Mass gained in 1 hour from 1 hour to 2 hours in the present disclosure.

 本開示の蓄熱構造体は、水和および/または脱水の際に化学蓄熱材が封止容器の外に流出することを抑制できるので、理論上何度でも繰り返し使用が可能である。
 化学蓄熱材から発生した熱の使い方として、発生した熱は封止容器に伝わって封止容器が温められるため、封止容器に加熱対象を接触させれば温めることができる。また、接触加熱だけでなく、他の温め方もある。水和反応のために付与した水分が液体の水の場合、化学蓄熱材との水和速度が水蒸気より早く、急速に熱を発生するため、付与した水が沸騰して高温の水蒸気となり、その水蒸気を使って加熱対象を温めることができる。水和反応のために付与した水分が水蒸気の場合、化学蓄熱材との反応によって水蒸気が温められ、水蒸気が温風として機能するため、水蒸気透過部材を透過した水蒸気を使って加熱対象を温めることができる。
Since the heat storage structure of the present disclosure can prevent the chemical heat storage material from flowing out of the sealed container during hydration and/or dehydration, it can theoretically be used repeatedly any number of times.
As for how to use the heat generated from the chemical heat storage material, the generated heat is transmitted to the sealed container and warms the sealed container. In addition to contact heating, there are other ways of warming. If the moisture added for the hydration reaction is liquid water, the hydration rate with the chemical heat storage material is faster than steam, and heat is generated rapidly. Steam can be used to heat objects. When the moisture added for the hydration reaction is water vapor, the water vapor is warmed by the reaction with the chemical heat storage material, and the water vapor functions as warm air. can be done.

 図2は本開示の蓄熱構造体の別の一実施形態における構成を示す概略図である。本実施形態において、封止容器は、上述した本開示の化学蓄熱材4、封止容器本体5及び水蒸気透過部材6とから構成されている。このように、封止容器がその一部に水蒸気透過部材を含む構成とすることもできる。水蒸気を水蒸気透過部材から出し入れすることによって、蓄熱構造体として用いることができる。図2においては、封止容器本体は、水蒸気を透過しない部材であってもよいが、水蒸気透過部材であってもよい。 FIG. 2 is a schematic diagram showing the configuration of another embodiment of the heat storage structure of the present disclosure. In this embodiment, the sealed container is composed of the chemical heat storage material 4 of the present disclosure, the sealed container main body 5 and the water vapor permeable member 6 described above. In this way, the sealed container can also be configured to partially include the water vapor permeable member. It can be used as a heat storage structure by allowing water vapor to flow in and out of the water vapor permeable member. In FIG. 2, the sealed container main body may be a member impermeable to water vapor, but may be a water vapor permeable member.

 図3は本開示の蓄熱システムの一実施形態における構成を示す概略図である。本実施形態は、上述した本開示の蓄熱構造体を有する蓄熱器13と、水和反応を行う水蒸気供給機としての送風機7及び貯水槽8と、水9と、脱水反応を行うための熱供給機としての熱風発生機10と、蓄熱器から発生した熱を利用する加熱室11と、熱風出口12とから構成されている。 FIG. 3 is a schematic diagram showing the configuration of one embodiment of the heat storage system of the present disclosure. The present embodiment includes a heat storage device 13 having the heat storage structure of the present disclosure described above, a blower 7 and a water storage tank 8 as a water vapor supplier for performing a hydration reaction, water 9, and heat supply for performing a dehydration reaction. It is composed of a hot air generator 10 as a machine, a heating chamber 11 using heat generated from a heat accumulator, and a hot air outlet 12 .

 図3において発熱が行われる手順は、例えば以下の通りである。
 蓄熱器13は、蓄熱状態の化学蓄熱材を有する蓄熱構造体を、水蒸気供給機から送られた水蒸気を化学蓄熱材に供給可能な形態で備える。この時、蓄熱器13に新たに蓄熱状態の化学蓄熱材を有する蓄熱構造体を備えてもよいし、既に発熱した状態(以下、未蓄熱状態と呼ぶ。)の化学蓄熱材を有する蓄熱構造体を、後述の蓄熱手順で蓄熱状態としてもよい。
 その後、送風機7によって送風を行い、水9が貯められている貯水槽8から蓄熱器13に水蒸気が送られる。蓄熱器13に水蒸気が送られることによって、蓄熱器13が有する蓄熱構造体中の化学蓄熱材が、水和反応を行う。水和反応によって生じた熱によって蓄熱器13が温められると共に、加熱室11に水和反応によって生じた熱が送られる。その結果、加熱室11で熱が利用可能になる。この時、加熱室11に温める対象を設置してもよいし、蓄熱器13に温める対象を設置してもよい。
The procedure for generating heat in FIG. 3 is, for example, as follows.
The heat accumulator 13 includes a heat storage structure having a chemical heat storage material in a heat storage state in a form capable of supplying steam sent from a steam supply device to the chemical heat storage material. At this time, the heat storage device 13 may be newly provided with a heat storage structure having a chemical heat storage material in a heat storage state, or a heat storage structure having a chemical heat storage material in a state in which heat has already been generated (hereinafter referred to as a non-heat storage state). may be brought into a heat storage state in a heat storage procedure described later.
After that, air is blown by the blower 7, and steam is sent from the water tank 8 in which the water 9 is stored to the heat accumulator 13. - 特許庁By sending water vapor to the heat accumulator 13, the chemical heat storage material in the heat storage structure of the heat accumulator 13 undergoes a hydration reaction. The heat generated by the hydration reaction warms the heat accumulator 13 and the heat generated by the hydration reaction is sent to the heating chamber 11 . As a result, heat becomes available in the heating chamber 11 . At this time, the object to be warmed may be placed in the heating chamber 11 or the object to be warmed may be placed in the heat accumulator 13 .

 図3において蓄熱が行われる手順は、例えば以下の通りである。
 蓄熱器13に、未蓄熱状態の化学蓄熱材を有する蓄熱構造体を、熱供給機から送られた熱を化学蓄熱材に供給可能に備える。この時、蓄熱器13に新たに未蓄熱状態の化学蓄熱材を有する蓄熱構造体を備えてもよいし、蓄熱状態の化学蓄熱材を有する蓄熱構造体に前述の発熱手順を行い、化学蓄熱材を未蓄熱状態としてもよい。
 その後、熱風発生機10によって熱風を発生させ、蓄熱器13に熱風が送られる。蓄熱器13に熱風が送られることによって、蓄熱器13が有する蓄熱構造体中の化学蓄熱材が、脱水反応を行う。脱水反応によって化学蓄熱材が蓄熱状態となる。
 なお、脱水反応で発生した水蒸気は貯水槽で凝縮させて水和反応に使用してもよい。脱水に使う熱源は、工場の未利用熱を用いると、熱の有効利用に繋がる。
The procedure for heat storage in FIG. 3 is, for example, as follows.
The heat accumulator 13 is provided with a heat storage structure having a chemical heat storage material in an unstored state so that the heat sent from the heat supply device can be supplied to the chemical heat storage material. At this time, the heat accumulator 13 may be newly provided with a heat storage structure having a chemical heat storage material in a non-heat-storing state, or the heat storage structure having a chemical heat storage material in a heat-storing state may be subjected to the above-described heat generation procedure to obtain a chemical heat storage material. may be set to an unheated state.
After that, hot air is generated by the hot air generator 10 and sent to the heat accumulator 13 . By sending hot air to the heat accumulator 13, the chemical heat storage material in the heat storage structure of the heat accumulator 13 undergoes a dehydration reaction. The dehydration reaction brings the chemical heat storage material into a heat storage state.
Incidentally, the water vapor generated by the dehydration reaction may be condensed in a water tank and used for the hydration reaction. Using unused heat from the factory as the heat source for dehydration leads to effective utilization of heat.

以下に実施例を挙げて本開示をより具体的に説明するが、本開示は、以下の実施例により限定されるものではない。 EXAMPLES The present disclosure will be described more specifically below with reference to examples, but the present disclosure is not limited to the following examples.

[実施例1]
(蓄熱構造体の作製)
 封止容器としてのPTFE製三方袋23mm×23mm×t0.1mmに化学蓄熱材MgSO・7HOを0.200g入れ、開口部をPFAフィルムの溶着によって封止して蓄熱構造体を作製した。
[Example 1]
(Preparation of heat storage structure)
A heat storage structure was produced by putting 0.200 g of the chemical heat storage material MgSO 4 .7H 2 O into a PTFE three-sided bag of 23 mm × 23 mm × t 0.1 mm as a sealed container, and sealing the opening by welding a PFA film. .

(蓄熱構造体の脱水)
 作製した蓄熱構造体を秤量した後、電気炉内で加熱し、質量減少しなくなるまで脱水を行った。加熱温度は化学蓄熱材から水が脱離する温度以上かつ封止容器の耐熱温度以下で行った。脱水の確認として、蓄熱構造体から化学蓄熱材を取り出し、株式会社リガク製X線回折装置SmartLabを使用して構造解析を行い、一部または全部の水が抜けた構造に変化したことを確認した。
(Dehydration of heat storage structure)
After weighing the produced heat storage structure, it was heated in an electric furnace and dehydrated until the mass did not decrease. The heating temperature was higher than the temperature at which water is desorbed from the chemical heat storage material and lower than the heat resistance temperature of the sealed container. To confirm dehydration, the chemical heat storage material was taken out from the heat storage structure and structural analysis was performed using an X-ray diffraction device SmartLab manufactured by Rigaku Co., Ltd. It was confirmed that the structure changed to a structure in which some or all of the water was removed. .

(蓄熱構造体の水和)
 脱水した蓄熱構造体を恒温恒湿装置中に静置し、定期的に秤量して質量増加が止まるまで水和反応を行った。水和の確認として、脱水と同様に株式会社リガク製X線回折装置SmartLabを使用して構造解析を行い、化学蓄熱材が元の構造に戻っていることを確認した。
(Hydration of heat storage structure)
The dehydrated heat storage structure was placed in a constant temperature and humidity apparatus, weighed periodically, and hydrated until the mass stopped increasing. As confirmation of hydration, structural analysis was performed using an X-ray diffractometer SmartLab manufactured by Rigaku Corporation in the same manner as dehydration, and it was confirmed that the chemical heat storage material had returned to its original structure.

(流出防止の評価)
 作製した蓄熱構造体の化学蓄熱材の流出防止効果を、上述の脱水と水和を行って評価した。評価指標として封止容器の封止状態と封止容器表面からの水の染み出しを用いた。それぞれの評価基準は以下のように定めた。
 封止容器の封止状態の確認は、脱水時に化学蓄熱材から発生する水蒸気を封止容器の外へ排出できたかの評価であり、封止の破れがないかを目視で行った。水の染み出し確認は、蓄熱構造体を恒温恒湿槽から取り出し、封止容器の表面に塩化コバルト紙を接触させた際の塩化コバルト紙の色によって判断した。塩化コバルト紙が赤色に変色しなかった場合、封止容器表面から水が染み出しておらず、赤色に変色した場合、封止容器表面から水が染み出したと判断した。評価結果を表1-1に示す。
〔封止容器の封止状態〕
A:脱水中に封止容器の封止が破れなかった。
B:脱水中に封止容器の封止が破れた。
〔封止容器表面からの水の染み出し〕
A:水和中に封止容器表面からの水の染み出しが起きなかった。
B:水和中に封止容器表面からの水の染み出しが起きた。
〔流出防止効果〕
 評価指標である封止容器の封止状態、及び封止容器表面からの水の染み出しが、いずれも評価Aの場合に、封止容器から化学蓄熱材が流出しなかった。
 封止容器の封止状態、及び封止容器表面からの水の染み出しのいずれかが評価Bの場合には、封止容器から化学蓄熱材が流出した。
(Evaluation of outflow prevention)
The outflow prevention effect of the chemical heat storage material of the produced heat storage structure was evaluated by performing the above-described dehydration and hydration. As evaluation indexes, the sealing state of the sealed container and the seepage of water from the surface of the sealed container were used. Each evaluation criterion was defined as follows.
Confirmation of the sealed state of the sealed container was an evaluation of whether or not the water vapor generated from the chemical heat storage material during dehydration could be discharged out of the sealed container. The confirmation of the seepage of water was determined by the color of the cobalt chloride paper when the heat storage structure was taken out from the thermo-hygrostat and the cobalt chloride paper was brought into contact with the surface of the sealed container. When the cobalt chloride paper did not turn red, it was determined that water had not oozed out from the surface of the sealed container, and when it turned red, water had oozed out from the surface of the sealed container. Evaluation results are shown in Table 1-1.
[Sealed State of Sealed Container]
A: The sealing of the sealed container was not broken during dehydration.
B: Sealing of the sealed container was broken during dehydration.
[Water oozes out from the surface of the sealed container]
A: Water did not seep out from the surface of the sealed container during hydration.
B: Water seeped out from the surface of the sealed container during hydration.
[Outflow prevention effect]
When the sealed state of the sealed container, which is an evaluation index, and the seepage of water from the surface of the sealed container, which are evaluation indexes, were evaluated A, the chemical heat storage material did not flow out from the sealed container.
When either the sealed state of the sealed container or the seepage of water from the surface of the sealed container was evaluated as B, the chemical heat storage material flowed out of the sealed container.

[実施例2~47]
 表1-1又は表1-2に記載された化学蓄熱材0.200gを封止容器としての23mm×23mm(厚みは材質、透湿度によって異なる)の三方袋に入れ、開口部を熱圧着、ホットメルト剤の溶着、もしくは耐熱性の粘着テープ(中興化成工業株式会社API-214A)によって封止して蓄熱構造体を作製した。三方袋は市販品、もしくは表1-1又は表1-2に記載された材質の透湿性フィルムを加工した物を使用し、同一の材質であっても厚みや細孔径によって透湿度を調整した。材質が結晶性樹脂の場合は二軸延伸法で作製しており、各原材料をガラス転移点以上融点以下の温度でペースト状にし、押し出し成形後、押し出し方向と垂直に延伸することで水蒸気透過部材を作製した。延伸温度や延伸倍率を制御することによって厚みや細孔径をコントロールした。また、非結晶性樹脂のPIなどの場合は、相分離法で作製しており、各原材料とシリカなどの微粒子を混合したペーストをフィルム状に塗布成形し、加熱固化後、フッ化水素水などで微粒子を除去することによって水蒸気透過部材を作製した。成形体の厚みによって水蒸気透過部材の厚みを、除去する微粒子の大きさや添加率によって気孔率を調整した。作製した蓄熱構造体は、電気炉内で蓄熱材の水の脱水温度以上かつ封止容器の耐熱温度以下で脱水し、その後、各化学蓄熱材に合わせた水和条件で水和反応を行って、化学蓄熱材の流出防止効果を評価した。結果を表1-1及び表1-2に示す。
[Examples 2 to 47]
0.200 g of the chemical heat storage material listed in Table 1-1 or Table 1-2 is placed in a three-sided bag of 23 mm × 23 mm (thickness varies depending on material and moisture permeability) as a sealed container, and the opening is thermocompression bonded. A heat storage structure was produced by sealing with a hot-melt agent or a heat-resistant adhesive tape (API-214A from Chuko Kasei Kogyo Co., Ltd.). For the three-sided bag, a commercially available product or a product processed with a moisture-permeable film made of the materials listed in Table 1-1 or Table 1-2 was used, and even if the material was the same, the moisture permeability was adjusted by adjusting the thickness and pore size. . When the material is crystalline resin, it is produced by the biaxial stretching method, and each raw material is made into a paste at a temperature above the glass transition point and below the melting point, and after extrusion molding, it is stretched perpendicular to the extrusion direction to create a water vapor permeable member. was made. The thickness and pore size were controlled by controlling the stretching temperature and stretching ratio. In addition, in the case of non-crystalline resin such as PI, it is produced by the phase separation method, and a paste that is a mixture of each raw material and fine particles such as silica is applied and molded into a film. A water vapor-permeable member was produced by removing the fine particles. The thickness of the water vapor permeable member was adjusted according to the thickness of the molded body, and the porosity was adjusted according to the size and addition rate of the fine particles to be removed. The fabricated heat storage structure is dehydrated in an electric furnace at a temperature higher than the dehydration temperature of water in the heat storage material and lower than the heat resistance temperature of the sealed container, and then a hydration reaction is performed under hydration conditions suitable for each chemical heat storage material. , evaluated the outflow prevention effect of the chemical heat storage material. The results are shown in Tables 1-1 and 1-2.

[比較例1~2]
 実施例と同様の方法で蓄熱構造体を作製し、実施例と同様の方法で流出防止効果を評価した。
[Comparative Examples 1 and 2]
A heat storage structure was produced in the same manner as in the example, and the outflow prevention effect was evaluated in the same manner as in the example.

Figure JPOXMLDOC01-appb-T000001

Figure JPOXMLDOC01-appb-T000002

 表1-1及び表1-2中のPTFEはポリテトラフルオロエチレン樹脂を、PIはポリイミド樹脂を、PPはポリプロピレン樹脂を、PEはポリエチレン樹脂を、TPUは熱可塑性ポリウレタン樹脂を、PEEKはポリエーテルエーテルケトン樹脂を、PPSはポリフェニレンスルフィド樹脂を、PEsはポリエステル樹脂を、それぞれ示す。
Figure JPOXMLDOC01-appb-T000001

Figure JPOXMLDOC01-appb-T000002

In Tables 1-1 and 1-2, PTFE is polytetrafluoroethylene resin, PI is polyimide resin, PP is polypropylene resin, PE is polyethylene resin, TPU is thermoplastic polyurethane resin, and PEEK is polyether. An ether ketone resin, PPS, a polyphenylene sulfide resin, and PEs, a polyester resin, respectively.

 本開示は、以下の構成に関する。
(構成1)
 封止容器及び前記封止容器に封止された化学蓄熱材を有する蓄熱構造体であって、
 前記封止容器は、水蒸気透過部材を少なくとも一部に含み、
 前記化学蓄熱材は、
  酸化マグネシウム、水酸化マグネシウム、並びに
  アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩、有機塩及びハロゲン化物
 からなる群から選択される少なくとも一を含み、
 前記化学蓄熱材は水和反応により発熱し、および/または脱水反応により蓄熱する物質であり、
 前記水蒸気透過部材の透湿度が、200~10000g/(m・24h)であることを特徴とする、蓄熱構造体。
(構成2)
 前記封止容器の耐熱温度が、70℃以上700℃以下である、構成1に記載の蓄熱構造体。
(構成3)
 前記水蒸気透過部材が、樹脂を含む、構成1または2に記載の蓄熱構造体。
(構成4)
 前記樹脂が、フッ素樹脂、ポリイミド樹脂、シリコーン樹脂、ポリエーテルエーテルケトン樹脂、ポリフェニレンスルフィド樹脂及びポリエステル樹脂からなる群から選択される少なくとも一を含む、構成3に記載の蓄熱構造体。
(構成5)
 前記樹脂が、ポリテトラフルオロエチレン樹脂を含む、構成3または4に記載の蓄熱構造体。
(構成6)
 前記封止容器が、フィルムである、構成1~5のいずれか一項に記載の蓄熱構造体。
(構成7)
 前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩が、炭酸塩、リン酸塩、硫酸塩、硝酸塩及びケイ酸塩からなる群から選択される少なくとも一を含む、構成1~6のいずれか一項に記載の蓄熱構造体。
(構成8)
 前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩が、NaCO・xHO(x=0~10)、NaPO・yHO(y=0~12)及びMgSO・zHO(z=0~7)からなる群から選択される少なくとも一を含む、構成1~7のいずれか一項に記載の蓄熱構造体。
(構成9)
 水和反応を行うための水蒸気供給機、脱水反応を行うための熱供給機、及び蓄熱器を備える蓄熱システムであって、
 前記蓄熱器が、構成1~8のいずれか一項に記載の蓄熱構造体を有し、
 前記熱供給機によって、前記蓄熱器に熱が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が、前記蓄熱器に送られた熱によって脱水反応を行うことで前記化学蓄熱材に蓄熱が行われ、
 また、前記水蒸気供給機によって、前記蓄熱器に水蒸気が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が水和反応を行うことによって化学蓄熱材に蓄熱された熱が取り出される、
 蓄熱システム。
The present disclosure relates to the following configurations.
(Configuration 1)
A heat storage structure having a sealed container and a chemical heat storage material sealed in the sealed container,
The sealed container includes at least a portion of a water vapor permeable member,
The chemical heat storage material is
A group consisting of magnesium oxide, magnesium hydroxide, and at least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead. including at least one selected from
The chemical heat storage material is a substance that generates heat by a hydration reaction and/or stores heat by a dehydration reaction,
A heat storage structure, wherein the moisture permeability of the water vapor permeable member is 200 to 10000 g/(m 2 ·24 h).
(Configuration 2)
The heat storage structure according to configuration 1, wherein the heat resistant temperature of the sealed container is 70°C or higher and 700°C or lower.
(Composition 3)
The heat storage structure according to configuration 1 or 2, wherein the water vapor permeable member comprises a resin.
(Composition 4)
The heat storage structure according to configuration 3, wherein the resin includes at least one selected from the group consisting of fluororesin, polyimide resin, silicone resin, polyetheretherketone resin, polyphenylene sulfide resin and polyester resin.
(Composition 5)
A heat storage structure according to configuration 3 or 4, wherein the resin comprises polytetrafluoroethylene resin.
(Composition 6)
The heat storage structure according to any one of configurations 1 to 5, wherein the sealed container is a film.
(Composition 7)
At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead is carbonate, phosphate, sulfate, nitrate and silicate The heat storage structure according to any one of configurations 1 to 6, comprising at least one selected from the group consisting of salts.
(Composition 8)
At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead is Na 2 CO 3.xH 2 O (x=0 to 10 ), Na 3 PO 4.yH 2 O (y=0 to 12), and MgSO 4.zH 2 O (z=0 to 7). A heat storage structure according to claim 1.
(Composition 9)
A heat storage system comprising a steam supplier for performing a hydration reaction, a heat supplier for performing a dehydration reaction, and a heat accumulator,
The heat storage device has a heat storage structure according to any one of configurations 1 to 8,
heat is sent to the heat accumulator by the heat supplier;
The chemical heat storage material contained in the heat storage structure undergoes a dehydration reaction with the heat sent to the heat accumulator, whereby heat is stored in the chemical heat storage material,
Further, steam is sent to the heat accumulator by the steam supplier,
The heat stored in the chemical heat storage material is extracted by a hydration reaction of the chemical heat storage material contained in the heat storage structure.
heat storage system.

1 化学蓄熱材、2 封止容器、3 細孔、4 化学蓄熱材、5 封止容器本体、6 水蒸気透過部材、7 送風機、8 貯水槽、9 水、10 熱風発生機、11 加熱室、12 熱風出口、13 蓄熱器 1 Chemical heat storage material, 2 Sealed container, 3 Pores, 4 Chemical heat storage material, 5 Sealed container body, 6 Water vapor transmission member, 7 Blower, 8 Water tank, 9 Water, 10 Hot air generator, 11 Heating chamber, 12 Hot air outlet, 13 heat accumulator

Claims (9)

 封止容器及び前記封止容器に封止された化学蓄熱材を有する蓄熱構造体であって、
 前記封止容器は、水蒸気透過部材を少なくとも一部に含み、
 前記化学蓄熱材は、
  酸化マグネシウム、水酸化マグネシウム、並びに
  アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩、有機塩及びハロゲン化物
 からなる群から選択される少なくとも一を含み、
 前記化学蓄熱材は水和反応により発熱し、および/または脱水反応により蓄熱する物質であり、
 前記水蒸気透過部材の透湿度が、200~10000g/(m・24h)であることを特徴とする、蓄熱構造体。
A heat storage structure having a sealed container and a chemical heat storage material sealed in the sealed container,
The sealed container includes at least a portion of a water vapor permeable member,
The chemical heat storage material is
A group consisting of magnesium oxide, magnesium hydroxide, and at least one inorganic salt, organic salt and halide selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead. including at least one selected from
The chemical heat storage material is a substance that generates heat by a hydration reaction and/or stores heat by a dehydration reaction,
A heat storage structure, wherein the moisture permeability of the water vapor permeable member is 200 to 10000 g/(m 2 ·24 h).
 前記封止容器の耐熱温度が、70℃以上700℃以下である、請求項1に記載の蓄熱構造体。 The heat storage structure according to claim 1, wherein the heat resistant temperature of the sealed container is 70°C or higher and 700°C or lower.  前記水蒸気透過部材が、樹脂を含む、請求項1または2に記載の蓄熱構造体。 The heat storage structure according to claim 1 or 2, wherein the water vapor permeable member contains resin.  前記樹脂が、フッ素樹脂、ポリイミド樹脂、シリコーン樹脂、ポリエーテルエーテルケトン樹脂、ポリフェニレンスルフィド樹脂及びポリエステル樹脂からなる群から選択される少なくとも一を含む、請求項3に記載の蓄熱構造体。 The heat storage structure according to claim 3, wherein the resin contains at least one selected from the group consisting of fluororesin, polyimide resin, silicone resin, polyetheretherketone resin, polyphenylene sulfide resin and polyester resin.  前記樹脂が、ポリテトラフルオロエチレン樹脂を含む、請求項3または4に記載の蓄熱構造体。 The heat storage structure according to claim 3 or 4, wherein the resin contains polytetrafluoroethylene resin.  前記封止容器が、フィルムである、請求項1~5のいずれか一項に記載の蓄熱構造体。 The heat storage structure according to any one of claims 1 to 5, wherein the sealed container is a film.  前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩が、炭酸塩、リン酸塩、硫酸塩、硝酸塩及びケイ酸塩からなる群から選択される少なくとも一を含む、請求項1~6のいずれか一項に記載の蓄熱構造体。 At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead is carbonate, phosphate, sulfate, nitrate and silicate The heat storage structure according to any one of claims 1 to 6, comprising at least one selected from the group consisting of salts.  前記アルカリ金属、アルカリ土類金属、アルミニウム、マンガン、鉄、ニッケル、銅、亜鉛及び鉛からなる群から選択される少なくとも一の無機塩が、NaCO・xHO(x=0~10)、NaPO・yHO(y=0~12)及びMgSO・zHO(z=0~7)からなる群から選択される少なくとも一を含む、請求項1~7のいずれか一項に記載の蓄熱構造体。 At least one inorganic salt selected from the group consisting of alkali metals, alkaline earth metals, aluminum, manganese, iron, nickel, copper, zinc and lead is Na 2 CO 3.xH 2 O (x=0 to 10 ), Na 3 PO 4.yH 2 O (y=0 to 12) and MgSO 4.zH 2 O (z=0 to 7). or the heat storage structure according to claim 1.  水和反応を行うための水蒸気供給機、脱水反応を行うための熱供給機、及び蓄熱器を備える蓄熱システムであって、
 前記蓄熱器が、請求項1~8のいずれか一項に記載の蓄熱構造体を有し、
 前記熱供給機によって、前記蓄熱器に熱が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が、前記蓄熱器に送られた熱によって脱水反応を行うことで前記化学蓄熱材に蓄熱が行われ、
 また、前記水蒸気供給機によって、前記蓄熱器に水蒸気が送られ、
 前記蓄熱構造体に含まれた化学蓄熱材が水和反応を行うことによって化学蓄熱材に蓄熱された熱が取り出される、
 蓄熱システム。
A heat storage system comprising a steam supplier for performing a hydration reaction, a heat supplier for performing a dehydration reaction, and a heat accumulator,
The heat storage device has the heat storage structure according to any one of claims 1 to 8,
heat is sent to the heat accumulator by the heat supplier;
The chemical heat storage material contained in the heat storage structure undergoes a dehydration reaction with the heat sent to the heat accumulator, whereby heat is stored in the chemical heat storage material,
Further, steam is sent to the heat accumulator by the steam supplier,
The heat stored in the chemical heat storage material is extracted by a hydration reaction of the chemical heat storage material contained in the heat storage structure.
heat storage system.
PCT/JP2022/033360 2021-09-30 2022-09-06 Heat storage structure and heat storage system Ceased WO2023053859A1 (en)

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