TWI868355B - Chemical heat storage material and manufacturing method thereof - Google Patents
Chemical heat storage material and manufacturing method thereof Download PDFInfo
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Abstract
一種化學蓄熱材料,其含有鹼土金屬之氫氧化物及/或氧化物,作為相對於鹼土金屬之氫氧化物之含量,硼及氟之合計含量為10 ppm以上未達1200 ppm。上述化學蓄熱材料進而含有鹼金屬之化合物,且相對於上述鹼土金屬之氫氧化物及/或氧化物,上述鹼金屬之化合物之量較佳為0.1~50 mol%。A chemical thermal storage material contains hydroxide and/or oxide of an alkali earth metal, wherein the total content of boron and fluorine is 10 ppm or more and less than 1200 ppm relative to the content of the hydroxide of the alkali earth metal. The chemical thermal storage material further contains an alkali metal compound, and the amount of the alkali metal compound relative to the hydroxide and/or oxide of the alkali earth metal is preferably 0.1 to 50 mol%.
Description
本發明係關於一種化學蓄熱材料及其製造方法。The present invention relates to a chemical heat storage material and a manufacturing method thereof.
近年來,根據二氧化碳排放規定,要求減少化石燃料之使用,除了於各製程中節省能源以外,還必須推進排熱之利用。作為排熱之利用手段,已知利用水之100℃以下之溫水蓄熱。然而,溫水蓄熱存在如下問題:(1)因存在放熱損失而無法長時間蓄熱;(2)顯熱量較小,因此需要大量水,蓄熱設備難以小型化;以及(3)輸出溫度根據利用量而不穩定,且逐漸降低等。因此,為了推進此種排熱之民生利用,必須開發更高效率之蓄熱技術。In recent years, in accordance with the regulations on carbon dioxide emissions, the use of fossil fuels has been required to be reduced. In addition to saving energy in various processes, it is also necessary to promote the use of waste heat. As a means of utilizing waste heat, it is known to use warm water below 100°C for heat storage. However, warm water heat storage has the following problems: (1) It cannot store heat for a long time due to the existence of heat loss; (2) The sensible heat is small, so a large amount of water is required, and the heat storage equipment is difficult to miniaturize; and (3) The output temperature is unstable and gradually decreases depending on the amount of utilization. Therefore, in order to promote the civilian use of this kind of waste heat, it is necessary to develop more efficient heat storage technology.
作為效率較高之蓄熱技術,可列舉:化學蓄熱法。化學蓄熱法伴隨物質之吸附、水合等化學變化,因此與利用材料本身(水、熔鹽等)之潛熱或顯熱的蓄熱方法相比,每單位質量之蓄熱量較高。作為化學蓄熱法,提出有:利用大氣中之水蒸氣之吸附脫附的水蒸氣吸附脫附法、對於金屬鹽之氨吸收(氨錯合物生成反應)、利用醇等有機物之吸附脫附之反應等。若考慮到對環境之負荷或裝置之簡便性,則水蒸氣吸附脫附法最有利。作為水蒸氣吸附脫附法中使用之化學蓄熱材料,已知為鹼土金屬之氫氧化物的氫氧化鈣或氫氧化鎂。As a heat storage technology with high efficiency, the following can be cited: chemical heat storage method. Chemical heat storage method is accompanied by chemical changes such as adsorption and hydration of substances. Therefore, compared with the heat storage method that utilizes the latent heat or sensible heat of the material itself (water, molten salt, etc.), the heat storage per unit mass is higher. As a chemical heat storage method, there are: water vapor adsorption and desorption method that utilizes the adsorption and desorption of water vapor in the atmosphere, ammonia absorption of metal salts (ammonia complex formation reaction), and adsorption and desorption reactions of organic substances such as alcohols. If the load on the environment or the simplicity of the device is taken into consideration, the water vapor adsorption and desorption method is the most advantageous. As a chemical heat storage material used in the water vapor adsorption desorption method, calcium hydroxide or magnesium hydroxide, which is a hydroxide of an alkali earth metal, is known.
然而,該等氫氧化鈣及氫氧化鎂於100~400℃之低溫區域不會引起有效的脫水反應,因此,存在無法作為實用的蓄熱材發揮機能之問題。However, these calcium hydroxides and magnesium hydroxides do not cause effective dehydration reactions in the low temperature range of 100 to 400° C., and therefore, there is a problem that they cannot function as practical heat storage materials.
為了解決此問題,專利文獻1中提出了如下化學蓄熱材料:其係藉由利用與選自由鎂、鎳、鈷、銅及鋁構成之群中至少1種金屬成分之複合氫氧化物從而可於100~300℃左右進行蓄熱者。To solve this problem, Patent Document 1 proposes the following chemical heat storage material: it is a material that can store heat at about 100 to 300°C by utilizing a composite hydroxide with at least one metal component selected from the group consisting of magnesium, nickel, cobalt, copper and aluminum.
進而,專利文獻2中提出了如下化學蓄熱材料:其係以改善專利文獻1所記載之化學蓄熱材料之蓄熱量為目的,於鎂或鈣之氫氧化物添加氯化鋰等吸濕性金屬鹽而成者。 先前技術文獻 專利文獻Furthermore, Patent Document 2 proposes the following chemical heat storage material: it is formed by adding a hygroscopic metal salt such as lithium chloride to magnesium or calcium hydroxide for the purpose of improving the heat storage capacity of the chemical heat storage material described in Patent Document 1. Prior Art Document Patent Document
專利文獻1:日本特開2007-309561號公報 專利文獻2:日本特開2009-186119號公報Patent document 1: Japanese Patent Publication No. 2007-309561 Patent document 2: Japanese Patent Publication No. 2009-186119
[發明所欲解決之課題][The problem that the invention wants to solve]
根據專利文獻1及2中所揭示之技術,雖然可將蓄熱運作溫度進行某種程度之低溫化,然而,例如於欲將工廠廢熱進行蓄熱時等,工廠廢熱之溫度區域為200~250℃或更低之低溫區域,故其蓄熱運作溫度並不夠低,難以效率良好地利用工廠廢熱,要求追求運作溫度之更進一步的低溫化。進而,將蓄熱運作溫度低溫化亦為提高蓄熱密度與反應效率。擴張工廠排熱之可回收之適用範圍,並提高再生能源活用之經濟性依然是重要的課題。According to the technology disclosed in Patent Documents 1 and 2, although the heat storage operating temperature can be lowered to a certain extent, for example, when the factory waste heat is to be stored, the temperature range of the factory waste heat is 200-250°C or lower, so the heat storage operating temperature is not low enough, and it is difficult to use the factory waste heat efficiently, and it is required to pursue a further lowering of the operating temperature. Furthermore, lowering the heat storage operating temperature is also to improve the heat storage density and reaction efficiency. Expanding the applicable scope of factory waste heat recovery and improving the economic efficiency of renewable energy utilization are still important issues.
有鑑於上述之現狀,本發明之目的在於提供一種化學蓄熱材料及其製造方法,該化學蓄熱材料係進行利用了鹼土金屬之氫氧化物的脫水反應之蓄熱者,顯示更高之反應率,並且可實現更低溫之蓄熱。 [解決課題之技術手段]In view of the above-mentioned current situation, the purpose of the present invention is to provide a chemical heat storage material and a manufacturing method thereof, wherein the chemical heat storage material is a heat storage material that utilizes the dehydration reaction of the hydroxide of an alkali earth metal, exhibits a higher reaction rate, and can achieve heat storage at a lower temperature. [Technical means to solve the problem]
為了解決上述之課題,本發明人等反覆進行各種研究,結果發現:於利用了鹼土金屬之氫氧化物的脫水反應之化學蓄熱材料中,作為相對於鹼土金屬之氫氧化物的含量,將硼及氟之含量設為10 ppm以上未達1200 ppm,藉此,可製造出顯示更高之反應率,且可實現於更低溫之蓄熱的化學蓄熱材料,從而完成本發明。In order to solve the above-mentioned problems, the inventors of the present invention have repeatedly conducted various studies and found that: in a chemical thermal storage material utilizing the dehydration reaction of an alkali earth metal hydroxide, by setting the content of boron and fluorine to 10 ppm or more and less than 1200 ppm relative to the content of the alkali earth metal hydroxide, a chemical thermal storage material showing a higher reaction rate and capable of achieving thermal storage at a lower temperature can be manufactured, thereby completing the present invention.
即,本案之第一發明係有關一種化學蓄熱材料,其係含有鹼土金屬之氫氧化物及/或氧化物者,作為相對於鹼土金屬之氫氧化物之含量,硼及氟之含量為10 ppm以上未達1200 ppm。較佳為,上述鹼土金屬為選自由鈣、鎂、鍶及鋇構成之群中至少1種。 上述化學蓄熱材料可進而含有鹼金屬之化合物,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述鹼金屬之化合物之量可為0.1~50 mol%。較佳為,上述鹼金屬為選自由鋰、鉀及鈉構成之群中至少1種。 上述化學蓄熱材料可進而含有選自由鎳、鈷、銅及鋁構成之群中至少1種之金屬的化合物,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述金屬之量可為0.1~40 mol%。 上述化學蓄熱材料可進而含有金屬之酸鹽,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述金屬之酸鹽的量可為0.05~30 mol%。較佳為,上述金屬之酸鹽為選自由鹼金屬及鹼土金屬構成之群中至少1種之金屬之酸鹽。更佳為,上述選自由鹼金屬及鹼土金屬構成之群中至少1種之金屬之酸鹽為選自由鋰、鈉、鉀、鈣、鎂、鍶及鋇構成之群中至少1種之金屬之酸鹽。又,較佳為,上述金屬之酸鹽為選自由鋁、鐵、鈷、鎳、銅及鋅構成之群中至少1種之金屬之酸鹽。That is, the first invention of this case is related to a chemical thermal storage material, which contains hydroxide and/or oxide of alkali earth metal, and the content of boron and fluorine is 10 ppm or more and less than 1200 ppm relative to the content of hydroxide of alkali earth metal. Preferably, the alkali earth metal is at least one selected from the group consisting of calcium, magnesium, strontium and barium. The chemical thermal storage material may further contain an alkali metal compound, and the amount of the alkali metal compound may be 0.1-50 mol% relative to the hydroxide and/or oxide of alkali earth metal. Preferably, the alkali metal is at least one selected from the group consisting of lithium, potassium and sodium. The chemical thermal storage material may further contain a compound of at least one metal selected from the group consisting of nickel, cobalt, copper and aluminum, and the amount of the metal may be 0.1 to 40 mol% relative to the hydroxide and/or oxide of the alkali earth metal. The chemical thermal storage material may further contain an acid salt of a metal, and the amount of the acid salt of the metal may be 0.05 to 30 mol% relative to the hydroxide and/or oxide of the alkali earth metal. Preferably, the acid salt of the metal is an acid salt of at least one metal selected from the group consisting of alkali metals and alkali earth metals. More preferably, the acid salt of at least one metal selected from the group consisting of alkali metals and alkali earth metals is an acid salt of at least one metal selected from the group consisting of lithium, sodium, potassium, calcium, magnesium, strontium and barium. Furthermore, more preferably, the acid salt of the metal is an acid salt of at least one metal selected from the group consisting of aluminum, iron, cobalt, nickel, copper and zinc.
本案之第二發明係有關一種化學蓄熱材料之製造方法,其包括製備如下化學蓄熱材料之步驟,該化學蓄熱材料含有鹼土金屬之氫氧化物及/或氧化物,且作為相對於鹼土金屬之氫氧化物之含量,硼及氟之合計含量為10 ppm以上未達1200 ppm。 上述方法進而可包括混合鹼土金屬之氫氧化物及/或氧化物與鹼金屬之化合物之步驟,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述鹼金屬之化合物之量可為0.1~50 mol%。 上述方法進而可包括混合鹼土金屬之氫氧化物及/或氧化物與選自由鎳、鈷、銅及鋁構成之群中至少1種之金屬的化合物之步驟,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述金屬之量可為0.1~40 mol%。 上述方法進而可包括混合鹼土金屬之氫氧化物及/或氧化物與金屬之酸鹽之步驟,相對於上述鹼土金屬之氫氧化物及/或氧化物,上述金屬之酸鹽之量可為0.05~30 mol%。 [發明之效果]The second invention of this case is related to a method for manufacturing a chemical heat storage material, which includes the steps of preparing the following chemical heat storage material, wherein the chemical heat storage material contains hydroxide and/or oxide of alkali earth metal, and the total content of boron and fluorine relative to the content of hydroxide of alkali earth metal is more than 10 ppm and less than 1200 ppm. The above method may further include the step of mixing hydroxide and/or oxide of alkali earth metal with a compound of alkali metal, and the amount of the above compound of alkali metal may be 0.1 to 50 mol% relative to the above hydroxide and/or oxide of alkali earth metal. The above method may further include the step of mixing the hydroxide and/or oxide of the alkali earth metal with a compound of at least one metal selected from the group consisting of nickel, cobalt, copper and aluminum, wherein the amount of the above metal may be 0.1 to 40 mol% relative to the hydroxide and/or oxide of the alkali earth metal. The above method may further include the step of mixing the hydroxide and/or oxide of the alkali earth metal with an acid salt of the metal, wherein the amount of the above metal acid salt may be 0.05 to 30 mol% relative to the hydroxide and/or oxide of the alkali earth metal. [Effect of the invention]
依據本發明,可提供如下化學蓄熱材料及其製造方法,該化學蓄熱材料係進行利用了鹼土金屬之氫氧化物的脫水反應的蓄熱之化學蓄熱材料,顯示更高之反應率,且可實現於更低溫之蓄熱者。According to the present invention, a chemical thermal storage material and a method for manufacturing the same can be provided. The chemical thermal storage material is a thermal storage material that utilizes a dehydration reaction of an alkali earth metal hydroxide, exhibits a higher reaction rate, and can achieve thermal storage at a lower temperature.
以下,詳細說明本發明之實施型態。 本發明之化學蓄熱材料係利用以鹼土金屬之氫氧化物及氧化物進行之以下可逆反應者。再者,於以下反應式中,表示使用鈣或鎂作為鹼土金屬之情形。 CaO+H2 OCa(OH)2 ΔH=-109.2 kJ/mol MgO+H2 OMg(OH)2 ΔH=-81.0 kJ/molThe following is a detailed description of the embodiments of the present invention. The chemical thermal storage material of the present invention utilizes the following reversible reaction with hydroxide and oxide of alkali earth metal. In the following reaction formula, calcium or magnesium is used as the alkali earth metal. CaO + H 2 O Ca(OH) 2 ΔH=-109.2 kJ/mol MgO+H 2 O Mg(OH) 2 ΔH=-81.0 kJ/mol
各式中,朝右方向之反應為氧化鈣或氧化鎂之水合放熱反應。反之,朝左方向之反應為氫氧化鈣或氫氧化鎂之脫水吸熱反應。亦即,本發明之化學蓄熱材料可藉由進行氫氧化鈣或氫氧化鎂之脫水反應來蓄熱,又,可藉由進行氧化鈣或氧化鎂之水合反應而將蓄積之熱能進行供給。In each formula, the reaction to the right is the exothermic hydration reaction of calcium oxide or magnesium oxide. Conversely, the reaction to the left is the endothermic dehydration reaction of calcium hydroxide or magnesium hydroxide. That is, the chemical heat storage material of the present invention can store heat by performing the dehydration reaction of calcium hydroxide or magnesium hydroxide, and can also supply the stored heat energy by performing the hydration reaction of calcium oxide or magnesium oxide.
本發明中之化學蓄熱材料可含有鹼土金屬之氫氧化物或鹼土金屬之氧化物中任一者,亦可兩者皆含有。作為上述鹼土金屬,可列舉:鈣、鎂、鍶、鋇。可為僅含有該等之1種者,亦可為含有2種以上之組合者。其中,較佳為鈣及/或鎂,更佳為鎂。作為鹼土金屬之氫氧化物、鹼土金屬之氧化物,較佳可列舉:氫氧化鎂、氫氧化鈣、鎂與鈣之複合氫氧化物、氧化鎂、氧化鈣、鎂與鈣之複合氧化物,可單獨使用該等,亦可混合2種以上使用。The chemical heat storage material in the present invention may contain either hydroxide of alkali earth metal or oxide of alkali earth metal, or both. Examples of the above-mentioned alkali earth metal include calcium, magnesium, strontium, and barium. It may contain only one of these or a combination of two or more of these. Among them, calcium and/or magnesium are preferred, and magnesium is more preferred. Examples of hydroxide of alkali earth metal and oxide of alkali earth metal include magnesium hydroxide, calcium hydroxide, composite hydroxide of magnesium and calcium, magnesium oxide, calcium oxide, and composite oxide of magnesium and calcium. These may be used alone or in combination of two or more.
本發明中之化學蓄熱材料中,作為相對於鹼土金屬之氫氧化物之含量,硼及氟之合計含量為10 ppm以上1200 ppm以下。其中,相對於鹼土金屬之氫氧化物之含量意指:該化學蓄熱材料含有鹼土金屬之氧化物之情形時,將該氧化物之重量換算為氫氧化物之重量,相對於換算後之氫氧化物之重量的含量。若硼及氟之合計含量相較於上述範圍為更多或更少,則難以獲得如下效果:即顯示更高之反應率且實現更低溫之蓄熱。上述合計含量之下限較佳為20 ppm以上,更佳為50 ppm以上,進而較佳為100 ppm以上。上述合計含量之上限較佳為1000 ppm以下,進而較佳為700 ppm以下。In the chemical thermal storage material of the present invention, the total content of boron and fluorine is 10 ppm or more and 1200 ppm or less relative to the content of hydroxide of alkali earth metal. The content relative to the hydroxide of alkali earth metal means: when the chemical thermal storage material contains an oxide of alkali earth metal, the weight of the oxide is converted into the weight of hydroxide, and the content is relative to the weight of the converted hydroxide. If the total content of boron and fluorine is more or less than the above range, it is difficult to obtain the following effects: showing a higher reaction rate and achieving lower temperature heat storage. The lower limit of the above total content is preferably 20 ppm or more, more preferably 50 ppm or more, and further preferably 100 ppm or more. The upper limit of the above-mentioned total content is preferably 1000 ppm or less, and further preferably 700 ppm or less.
雖然硼及氟如何作用於化學蓄熱材料之水合或脫水反應並未完全清楚,然而,可認為硼及氟於化學蓄熱材料之表面附近吸附於鹼土金屬之氫氧化物及/或氧化物或形成不溶性鹽而存在。推測藉由控制該情形,有助於鹼土金屬之氫氧化物及/或氧化物之循環特性(亦即加熱脫水反應及藉由水蒸氣導入之水合反應時之反應性)的提升或安定化。Although it is not completely clear how boron and fluorine act on the hydration or dehydration reaction of the chemical thermal storage material, it is believed that boron and fluorine are adsorbed on the hydroxide and/or oxide of the alkali earth metal near the surface of the chemical thermal storage material or form insoluble salts. It is speculated that by controlling this situation, it is helpful to improve or stabilize the cycle characteristics of the hydroxide and/or oxide of the alkali earth metal (that is, the reactivity during the heating dehydration reaction and the hydration reaction introduced by water vapor).
化學蓄熱材料所含有之硼及/或氟可為「作為雜質而於為化學蓄熱材料之原料之鹼土金屬之氫氧化物及/或氧化物中含有者」,亦可為「對鹼土金屬之氫氧化物及/或氧化物添加者」。被添加時之硼及/或氟之形態可為下述之鹼金屬之化合物、特定之金屬之化合物或金屬之酸鹽,又,亦可為無機酸。The boron and/or fluorine contained in the chemical thermal storage material may be "contained as impurities in the hydroxide and/or oxide of the alkali earth metal which is the raw material of the chemical thermal storage material", or "added to the hydroxide and/or oxide of the alkali earth metal". The form of the boron and/or fluorine when added may be the following alkali metal compound, specific metal compound or metal acid salt, and may also be an inorganic acid.
本發明之化學蓄熱材料除了鹼土金屬之氫氧化物及/或氧化物以外,亦可進而含有鹼金屬之化合物。藉由進而摻合鹼金屬之化合物,可更提高化學蓄熱材料之反應率。The chemical thermal storage material of the present invention may contain not only hydroxides and/or oxides of alkali earth metals, but also alkali metal compounds. By further mixing alkali metal compounds, the reaction rate of the chemical thermal storage material may be further increased.
作為構成鹼金屬之化合物之鹼金屬,可列舉:鋰、鉀、鈉,可為僅含有該等之1種者,亦可為含有組合2種以上者。其中,較佳為鋰、鈉,更佳為鋰。作為鹼金屬之化合物,只要可發揮本發明之效果者,並無特別限定,然而,較佳為具有吸濕性之鹽,且可吸附環境中之水分或生成對應之水合物之鹽。作為該種鹽,例如作為操作容易者可列舉:氟化物、氯化物、溴化物等鹵化物、氫氧化物、硼酸鹽、碳酸鹽、醋酸鹽、硝酸鹽或硫酸鹽等。可單獨使用該等,亦可混合使用2種以上。Alkaline metals constituting the alkali metal compound include lithium, potassium, and sodium. The alkali metal compound may contain only one of these or a combination of two or more of these. Among them, lithium and sodium are preferred, and lithium is more preferred. The alkali metal compound is not particularly limited as long as it can exert the effect of the present invention. However, it is preferably a hygroscopic salt that can absorb moisture in the environment or generate a corresponding hydrate. Such salts include, for example, halides such as fluoride, chloride, and bromide, hydroxides, borates, carbonates, acetates, nitrates, or sulfates that are easy to handle. These may be used alone or in combination of two or more.
更具體而言,作為鋰之鹽,較佳為鹵化鋰及/或氫氧化鋰,更佳為氯化鋰、溴化鋰及/或氫氧化鋰。作為鉀之鹽,較佳為鹵化鉀及/或氫氧化鉀,更佳為氯化鉀、溴化鉀及/或氫氧化鉀。作為鈉之鹽,較佳為鹵化鈉及/或氫氧化鈉,更佳為氯化鈉、溴化鈉及/或氫氧化鈉。More specifically, the lithium salt is preferably lithium halide and/or lithium hydroxide, and more preferably lithium chloride, lithium bromide and/or lithium hydroxide. The potassium salt is preferably potassium halide and/or potassium hydroxide, and more preferably potassium chloride, potassium bromide and/or potassium hydroxide. The sodium salt is preferably sodium halide and/or sodium hydroxide, and more preferably sodium chloride, sodium bromide and/or sodium hydroxide.
作為上述鹼金屬之化合物之使用量,將上述鹼土金屬之氫氧化物及/或氧化物之量設為100 mol%時,鹼金屬之化合物之量較佳為0.1~50 mol%。若鹼金屬之化合物之量相較於上述範圍為更少,則難以達成因鹼金屬之化合物之使用而獲得之反應率提高或蓄熱溫度之低溫化。又,若鹼金屬之化合物之量較上述範圍為多,則有化學蓄熱材料提供之每單位體積或每單位質量之蓄熱量降低之疑慮。上述鹼金屬之化合物之量較佳為0.5~30 mol%,更佳為1.0~20 mol%,進而較佳為2.0~10 mol%。藉由調節該鹼金屬之化合物之量,可控制化學蓄熱材料之脫水吸熱溫度。其中,上述鹼金屬之化合物含有硼或氟之情形下,該鹼金屬之化合物可於滿足上述化學蓄熱材料中之硼及氟之合計含量之範圍內使用。As the usage amount of the above-mentioned alkali metal compound, when the amount of the above-mentioned hydroxide and/or oxide of the alkali earth metal is set to 100 mol%, the amount of the alkali metal compound is preferably 0.1-50 mol%. If the amount of the alkali metal compound is less than the above range, it is difficult to achieve the increase in reaction rate or the lowering of heat storage temperature obtained by the use of the alkali metal compound. In addition, if the amount of the alkali metal compound is more than the above range, there is a concern that the heat storage capacity per unit volume or per unit mass provided by the chemical heat storage material will decrease. The amount of the above-mentioned alkali metal compound is preferably 0.5-30 mol%, more preferably 1.0-20 mol%, and further preferably 2.0-10 mol%. By adjusting the amount of the alkali metal compound, the dehydration endothermic temperature of the chemical thermal storage material can be controlled. Wherein, when the alkali metal compound contains boron or fluorine, the alkali metal compound can be used within the range that satisfies the total content of boron and fluorine in the chemical thermal storage material.
本發明之化學蓄熱材料除了上述鹼土金屬之氫氧化物及/或氧化物與任意成分之上述鹼金屬之化合物以外,亦可進而含有特定之金屬之化合物。藉由進而含有上述特定之金屬之化合物,可更提高化學蓄熱材料之反應率。此時,上述特定之金屬之化合物較佳為與鹼土金屬之氫氧化物及/或氧化物進行化學上之複合化。The chemical thermal storage material of the present invention may further contain a specific metal compound in addition to the above-mentioned hydroxide and/or oxide of the alkali earth metal and the above-mentioned alkali metal compound of any component. By further containing the above-mentioned specific metal compound, the reaction rate of the chemical thermal storage material can be further improved. In this case, the above-mentioned specific metal compound is preferably chemically compounded with the hydroxide and/or oxide of the alkali earth metal.
上述特定之金屬選自由鎳、鈷、銅及鋁構成之群,可為僅含有該等中之1種者,亦可為含有組合2種以上者。其中,較佳為選自由鎳、鈷及鋁構成之群至少1種,更佳為鎳及/或鈷。The specific metal is selected from the group consisting of nickel, cobalt, copper and aluminum, and may contain only one of them or a combination of two or more thereof. Among them, at least one selected from the group consisting of nickel, cobalt and aluminum is preferred, and nickel and/or cobalt is more preferred.
作為上述特定之金屬之化合物並無特別限定,較佳為與鹼土金屬之氫氧化物及/或氧化物複合化者,可列舉氟化物、氯化物、溴化物等之鹵化物、氫氧化物、氧化物、硼酸鹽、碳酸鹽、醋酸鹽、硝酸鹽或硫酸鹽等。可單獨使用該等,亦可混合2種以上而使用。更具體而言,較佳為氫氧化鎳、氫氧化鈷、鎳與鈷之複合氫氧化物、氧化鎳、氧化鈷、及/或鎳與鈷之複合氧化物。The compound of the above-mentioned specific metal is not particularly limited, and preferably is a compound with a hydroxide and/or oxide of an alkali earth metal, and examples thereof include halides such as fluorides, chlorides, and bromides, hydroxides, oxides, borates, carbonates, acetates, nitrates, or sulfates. These may be used alone or in combination of two or more. More specifically, nickel hydroxide, cobalt hydroxide, a composite hydroxide of nickel and cobalt, nickel oxide, cobalt oxide, and/or a composite oxide of nickel and cobalt are preferred.
作為上述特定之金屬之化合物之使用量,較佳為將上述鹼土金屬之氫氧化物及/或氧化物之量設為100 mol%時,上述特定之金屬之量為0.1~40 mol%。若上述特定之金屬之量相較於上述範圍為更少,則難以藉由上述特定之金屬之化合物之使用達成反應率之提高或蓄熱溫度之低溫化。又,若上述特定之金屬之量相較於上述範圍為更多,則有化學蓄熱材料提供之每單位體積或每單位質量之蓄熱量降低之疑慮。上述特定之金屬之量較佳為3~40 mol%,更佳為5~30 mol%,進而較佳為10~25 mol%。藉由調節該特定之金屬之化合物之使用量,可控制化學蓄熱材料之脫水吸熱溫度。其中,上述特定之金屬之化合物含有硼或氟之情形下,該特定之金屬之化合物可於滿足上述化學蓄熱材料中之硼及氟之合計含量之範圍內使用。As for the usage amount of the above-mentioned specific metal compound, it is preferred that when the amount of the above-mentioned hydroxide and/or oxide of the above-mentioned alkali earth metal is set to 100 mol%, the amount of the above-mentioned specific metal is 0.1-40 mol%. If the amount of the above-mentioned specific metal is less than the above-mentioned range, it is difficult to achieve an increase in reaction rate or a lowering of heat storage temperature by using the above-mentioned specific metal compound. Moreover, if the amount of the above-mentioned specific metal is more than the above-mentioned range, there is a concern that the heat storage capacity per unit volume or per unit mass provided by the chemical heat storage material will decrease. The amount of the above-mentioned specific metal is preferably 3-40 mol%, more preferably 5-30 mol%, and further preferably 10-25 mol%. By adjusting the usage amount of the specific metal compound, the dehydration heat absorption temperature of the chemical thermal storage material can be controlled. Wherein, when the specific metal compound contains boron or fluorine, the specific metal compound can be used within the range satisfying the total content of boron and fluorine in the chemical thermal storage material.
本發明中之化學蓄熱材料可為鹼土金屬之氫氧化物及/或氧化物、與依情況之鹼金屬之化合物、與依情況之特定之金屬之化合物單純進行物理上之混合或分散者,但並不限定於此。可為各構成成分之一部份或全部相互化學地複合化而成者,又,亦可為各構成成分之一部份或全部相互化學地反應而生成第三成分者。The chemical thermal storage material of the present invention may be a mixture or dispersion of hydroxide and/or oxide of alkali earth metal, a compound of alkali metal as appropriate, or a compound of specific metal as appropriate, but is not limited thereto. It may be a compound of some or all of the constituents chemically combined with each other, or it may be a compound of some or all of the constituents chemically reacting with each other to generate a third component.
本發明之化學蓄熱材料除了上述鹼土金屬之氫氧化物及/或氧化物、為任意成分之上述鹼金屬之化合物與為任意成分之上述特定之金屬之化合物以外,亦可進而含有金屬之酸鹽。金屬之酸鹽意指:藉由金屬之化合物與酸反應而形成之鹽,尤其,較佳為藉由用酸中和金屬之氫氧化物而形成之鹽。具體而言,例如可列舉:硝酸鎂、醋酸鎂、苯甲酸鎂、檸檬酸鎂、硝酸鈣、醋酸鈣、苯甲酸鈣、檸檬酸鈣、硝酸鋰、醋酸鋰、苯甲酸鋰、檸檬酸鋰等,但並不限定於該等。The chemical thermal storage material of the present invention may further contain metal acid salts in addition to the above-mentioned hydroxides and/or oxides of alkali earth metals, the above-mentioned compounds of alkali metals as arbitrary components, and the above-mentioned compounds of specific metals as arbitrary components. Metal acid salts refer to salts formed by the reaction of metal compounds and acids, and in particular, preferably salts formed by neutralizing metal hydroxides with acids. Specifically, for example, magnesium nitrate, magnesium acetate, magnesium benzoate, magnesium citrate, calcium nitrate, calcium acetate, calcium benzoate, calcium citrate, lithium nitrate, lithium acetate, lithium benzoate, lithium citrate, etc. can be listed, but it is not limited to them.
作為構成上述金屬之酸鹽的金屬,可列舉:鈣、鎂、鍶、鋇等鹼土金屬;鋰、鈉、鉀等鹼金屬;鋁、鐵、鈷、鎳、銅及鋅。可為僅含有該等中之1種者,亦可為含有組合2種以上者。其中,較佳為鈣、鋰及/或鎂,更佳為鈣及/或鎂。構成上述金屬之酸鹽的鹼土金屬可為與上述構成鹼土金屬之氫氧化物及/或氧化物的鹼土金屬為相同者,亦可為相異者,然而,就提高化學蓄熱材料之反應率之觀點而言,較佳為相同者。其中,於本發明使用之金屬之酸鹽為鹼土金屬之酸鹽時,作為該鹼土金屬之酸鹽,較佳為不使用鹼土金屬之碳酸鹽及氯化物。Examples of metals constituting the acid salts of the metals mentioned above include: alkali earth metals such as calcium, magnesium, strontium, and barium; alkali metals such as lithium, sodium, and potassium; aluminum, iron, cobalt, nickel, copper, and zinc. It may contain only one of these or a combination of two or more of these. Among them, calcium, lithium, and/or magnesium are preferred, and calcium and/or magnesium are more preferred. The alkali earth metals constituting the acid salts of the metals mentioned above may be the same as or different from the alkali earth metals constituting the hydroxides and/or oxides of the alkali earth metals mentioned above. However, from the viewpoint of increasing the reaction rate of the chemical thermal storage material, it is preferred that they are the same. Among them, when the metal acid salt used in the present invention is an alkaline earth metal acid salt, it is preferred not to use carbonates and chlorides of alkaline earth metals as the alkaline earth metal acid salt.
作為構成上述金屬之酸鹽的酸並無特別限定,可適當地使用公知之酸,可為無機酸、有機酸之任一者。又,可為水溶性之酸,亦可為於水難溶性或不溶性之酸。又,可僅使用1種,亦可適當組合2種以上而使用。The acid constituting the acid salt of the metal is not particularly limited, and a known acid may be used appropriately, and may be any of an inorganic acid and an organic acid. In addition, it may be a water-soluble acid, or an acid that is poorly soluble or insoluble in water. In addition, only one type may be used, or two or more types may be used in combination appropriately.
作為無機酸,例如可列舉:氫氟酸、鹽酸、氫溴酸、氫碘酸、硼酸、硫酸、硝酸、磷酸、膦酸、磺酸、氫氰酸等。Examples of the inorganic acid include hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, boric acid, sulfuric acid, nitric acid, phosphoric acid, phosphonic acid, sulfonic acid, and hydrocyanic acid.
作為有機酸,例如可列舉:有機磺酸、有機膦酸、脂肪族羥酸(包含二羥酸、三羥酸)、芳香族羥酸(包含二羥酸、三羥酸)、脂肪族羧酸(包含二羧酸、三羧酸)、脂肪族不飽和羧酸(包含二羧酸、三羧酸)、芳香族羧酸(包含二羧酸、三羧酸)、芳香族不飽和羧酸(包含二羧酸、三羧酸)、其他之含氧酸、其他之側氧羧酸、胺基酸、及該等衍生物之酸。Examples of organic acids include organic sulfonic acids, organic phosphonic acids, aliphatic hydroxy acids (including dihydroxy acids and trihydroxy acids), aromatic hydroxy acids (including dihydroxy acids and trihydroxy acids), aliphatic carboxylic acids (including dicarboxylic acids and tricarboxylic acids), aliphatic unsaturated carboxylic acids (including dicarboxylic acids and tricarboxylic acids), aromatic carboxylic acids (including dicarboxylic acids and tricarboxylic acids), aromatic unsaturated carboxylic acids (including dicarboxylic acids and tricarboxylic acids), other oxygen-containing acids, other pendant carboxylic acids, amino acids, and acids of their derivatives.
作為有機磺酸,例如可列舉:甲磺酸、苯磺酸、對甲苯磺酸等。作為有機膦酸,例如可列舉:磷酸二甲酯、苯膦酸等。作為脂肪族羥酸或芳香族羥酸,例如可列舉:乳酸、蘋果酸、檸檬酸、酒石酸等。作為脂肪族羧酸或脂肪族不飽和羧酸,例如可列舉:蟻酸、醋酸、丙酸、酪酸、丙烯酸、山梨酸、丙酮酸、草乙酸、方酸、草酸、丙二酸、琥珀酸、戊二酸、順丁烯二酸、烏頭酸等。作為芳香族羧酸或芳香族不飽和羧酸,例如可列舉:苯甲酸、鄰苯二甲酸、柳酸、莽草酸、沒食子酸、焦蜜石酸等。作為胺基酸,例如可列舉:天門冬胺酸、麩胺酸等。Examples of organic sulfonic acids include methanesulfonic acid, benzenesulfonic acid, p-toluenesulfonic acid, etc. Examples of organic phosphonic acids include dimethyl phosphate, benzenephosphonic acid, etc. Examples of aliphatic hydroxy acids or aromatic hydroxy acids include lactic acid, apple acid, citric acid, tartaric acid, etc. Examples of aliphatic carboxylic acids or aliphatic unsaturated carboxylic acids include fusic acid, acetic acid, propionic acid, butyric acid, acrylic acid, sorbic acid, pyruvic acid, oxalacetic acid, squaric acid, oxalic acid, malonic acid, succinic acid, glutaric acid, citric acid, acetic acid, etc. Examples of aromatic carboxylic acids or aromatic unsaturated carboxylic acids include benzoic acid, phthalic acid, salicylic acid, shikimic acid, gallic acid, pyromelitic acid, etc. Examples of amino acids include aspartic acid and glutamic acid.
作為上述金屬之酸鹽之使用量,將上述鹼土金屬之氫氧化物及/或氧化物之量設為100 mol%時,上述金屬之酸鹽之量較佳為0.05~30 mol%之量。若金屬之酸鹽之使用量相較於上述範圍為更少,則難以藉由該酸鹽之添加達成反應率之提高或蓄熱溫度之低溫化。又,若金屬之酸鹽之使用量相較於上述範圍為更多,則對成為母材料之上述鹼土金屬之氫氧化物及/或氧化物之影響較大,而有化學蓄熱材料提供之每單位體積或每單位質量之蓄熱量降低之疑慮。上述金屬之酸鹽之使用量較佳為0.1~20 mol%,更佳為0.3~15 mol%,進而較佳為0.5~10 mol%,進而再更佳為0.8~8 mol%,尤佳為1~6 mol%。其中,上述金屬之酸鹽含有硼或氟之情形下,該金屬之酸鹽可於滿足上述化學蓄熱材料中之硼及氟之合計含量之範圍內使用。As the usage amount of the above-mentioned metal acid salt, when the amount of the above-mentioned alkali earth metal hydroxide and/or oxide is set to 100 mol%, the amount of the above-mentioned metal acid salt is preferably 0.05 to 30 mol%. If the usage amount of the metal acid salt is less than the above-mentioned range, it is difficult to achieve an increase in reaction rate or a decrease in heat storage temperature by adding the acid salt. In addition, if the usage amount of the metal acid salt is more than the above-mentioned range, the influence on the above-mentioned alkali earth metal hydroxide and/or oxide that becomes the parent material is greater, and there is a concern that the heat storage capacity per unit volume or per unit mass provided by the chemical heat storage material is reduced. The usage amount of the above metal acid salt is preferably 0.1-20 mol%, more preferably 0.3-15 mol%, further preferably 0.5-10 mol%, further more preferably 0.8-8 mol%, and particularly preferably 1-6 mol%. Wherein, in the case where the above metal acid salt contains boron or fluorine, the metal acid salt can be used within the range satisfying the total content of boron and fluorine in the above chemical thermal storage material.
本發明之化學蓄熱材料為利用了鹼土金屬之氫氧化物與鹼土金屬之氧化物所引發之吸熱脫水反應及水合放熱反應者。於該範圍中,本發明之化學蓄熱材料中可含有其他成分,亦可含有於上述已說明之構成成分以外之化學蓄熱成分、未顯示化學蓄熱作用之成分(例如:黏合劑)。其中,於該等其他成分含有硼或氟之情形時,該其他成分可於滿足上述之化學蓄熱材料中之硼及氟之合計含量之範圍內使用。The chemical thermal storage material of the present invention utilizes the endothermic dehydration reaction and the hydration exothermic reaction caused by the hydroxide of alkali earth metal and the oxide of alkali earth metal. Within this range, the chemical thermal storage material of the present invention may contain other components, and may also contain chemical thermal storage components other than the components described above, and components that do not show chemical thermal storage effects (e.g., adhesives). Among them, when these other components contain boron or fluorine, the other components can be used within the range that satisfies the total content of boron and fluorine in the above-mentioned chemical thermal storage material.
本發明之化學蓄熱材料之形狀並無特別限定,例如可為粉末、造粒體、成形體等形狀。於製造形狀為粉末、造粒體、成形體之化學蓄熱材料時,可應用已知之手法。例如:製造粉末之化學蓄熱材料時,可應用篩選、裂解、粉碎步驟。又,製造造粒體之化學蓄熱材料時,可應用擠出造粒、轉動造粒、流化床造粒、噴霧乾燥等造粒步驟。製造成形體之化學蓄熱材料時,可應用利用沖壓成形、射出成形、吹氣成形、真空成形、擠出成形之成形步驟。亦即,只要無損及可實施作為化學蓄熱材料之性狀之程度,可依照需要者之實施型態選擇任意之形狀。The shape of the chemical thermal storage material of the present invention is not particularly limited, for example, it can be in the shape of powder, granules, molded bodies, etc. When manufacturing chemical thermal storage materials in the shape of powder, granules, and molded bodies, known techniques can be applied. For example: when manufacturing chemical thermal storage materials in the form of powder, screening, cracking, and crushing steps can be applied. In addition, when manufacturing chemical thermal storage materials in the form of granules, granulation steps such as extrusion granulation, rotary granulation, fluidized bed granulation, and spray drying can be applied. When manufacturing chemical thermal storage materials in the form of molded bodies, molding steps such as stamping, injection molding, blow molding, vacuum molding, and extrusion molding can be applied. That is, as long as there is no damage and the properties of the chemical thermal storage material can be implemented, any shape can be selected according to the implementation form required.
其次,說明本發明中製造化學蓄熱材料之方法。 本發明中製造化學蓄熱材料之方法並無特別限定,但至少作為相對於鹼土金屬之氫氧化物之含量,硼及氟之含量之合計為10 ppm以上未達1200 ppm,較佳為包含製備含有鹼土金屬之氫氧化物及/或氧化物之化學蓄熱材料之步驟。Next, the method for producing the chemical thermal storage material in the present invention is described. The method for producing the chemical thermal storage material in the present invention is not particularly limited, but at least the total content of boron and fluorine relative to the content of hydroxide of alkali earth metal is 10 ppm or more and less than 1200 ppm, and preferably includes the step of preparing a chemical thermal storage material containing hydroxide and/or oxide of alkali earth metal.
製備化學蓄熱材料時使用之原料的鹼土金屬之氫氧化物及/或氧化物可為純度99.9重量%以上之高純度品,亦可為例如純度為95重量%以上未達99.9重量%之相對低純度者。作為原料,可使用作為工業用之鎂之來源的海水法氧化鎂、天然礦石之燒成氧化鎂、電熔氧化鎂等。The alkali metal hydroxide and/or oxide used as the raw material for preparing the chemical thermal storage material may be a high purity product with a purity of 99.9% by weight or more, or a relatively low purity product with a purity of 95% by weight or more but less than 99.9% by weight. As the raw material, magnesium oxide obtained by seawater method, which is a source of magnesium for industrial use, magnesium oxide calcined from natural ore, fused magnesium oxide, etc. may be used.
於原料之鹼土金屬之氫氧化物及/或氧化物含有多於上述合計含量之範圍的硼及氟之情形時,較佳為實施藉由適當之精製處理降低硼及/或氟之操作。又,亦可於原料之鹼土金屬之氫氧化物及/或氧化物中以滿足上述合計含量之範圍添加含有硼及/或氟之成分而製造本發明之化學蓄熱材料。When the raw material alkali earth metal hydroxide and/or oxide contains more boron and fluorine than the above-mentioned total content range, it is preferred to perform an operation to reduce the boron and/or fluorine by appropriate refining treatment. In addition, the chemical thermal storage material of the present invention can also be manufactured by adding components containing boron and/or fluorine to the raw material alkali earth metal hydroxide and/or oxide to meet the above-mentioned total content range.
說明製造含有上述鹼金屬之化合物、上述特定之金屬之化合物、及/或上述金屬之酸鹽之化學蓄熱材料之方法的一例。首先,使鹼金屬之化合物溶解於離子交換水,製備鹼金屬之化合物之水溶液,於該水溶液中加入鹼土金屬之氫氧化物之粉末並攪拌混合。此時,可一併投入特定之金屬之化合物或金屬之酸鹽。可將所獲得之漿料進行乾燥,作為乾燥粉末製造化學蓄熱材料。攪拌混合之方法無特別限定,只要將溶劑之離子交換水與鹼土金屬之氫氧化物之粉末充分混合即可。An example of a method for producing a chemical thermal storage material containing the above-mentioned alkali metal compound, the above-mentioned specific metal compound, and/or the above-mentioned metal acid salt is described. First, the alkali metal compound is dissolved in ion exchange water to prepare an aqueous solution of the alkali metal compound, and the powder of the hydroxide of the alkali earth metal is added to the aqueous solution and stirred and mixed. At this time, the specific metal compound or the metal acid salt can be added at the same time. The obtained slurry can be dried to produce a chemical thermal storage material as a dry powder. The method of stirring and mixing is not particularly limited, as long as the ion exchange water of the solvent and the powder of the hydroxide of the alkali earth metal are fully mixed.
亦可變更加入各成分之順序。於此情形,例如可如下製造化學蓄熱材料:最初將鹼金屬之化合物、或鹼金屬之化合物與特定之金屬之化合物溶解於離子交換水,於該水溶液中加入金屬之酸鹽,其後,加入鹼土金屬之氫氧化物之粉末而製作漿料,接著使其乾燥而製造化學蓄熱材料。The order of adding the components may also be changed. In this case, for example, the chemical thermal storage material may be manufactured as follows: first, an alkali metal compound or an alkali metal compound and a specific metal compound are dissolved in ion exchange water, a metal acid salt is added to the aqueous solution, and then a powder of an alkali earth metal hydroxide is added to prepare a slurry, which is then dried to manufacture the chemical thermal storage material.
本發明之化學蓄熱材料可藉由對100~400℃左右之熱源(例如來自工廠排熱等之未利用熱)進行吸熱而脫水來進行蓄熱。經脫水後之化學蓄熱材料藉由保持乾燥狀態可容易維持蓄熱狀態,又可一面維持該蓄熱狀態一面搬送至需要之地點。於放熱之情形,可藉由接觸水,較佳為接觸水蒸氣而作為熱能取出水合反應熱(依情況,為水蒸氣吸附熱)。又,亦可於氣密封閉空間內之一側進行水蒸氣吸附,並且於另一側使水蒸發,藉此產生冷熱能。The chemical thermal storage material of the present invention can store heat by absorbing heat from a heat source of about 100 to 400°C (for example, unused heat from factory exhaust heat, etc.) and dehydrating it. The dehydrated chemical thermal storage material can easily maintain the thermal storage state by keeping it dry, and can be transported to the required location while maintaining the thermal storage state. In the case of heat release, the hydration reaction heat (depending on the situation, the water vapor adsorption heat) can be taken out as heat energy by contacting water, preferably contacting water vapor. In addition, water vapor can be adsorbed on one side of the airtight closed space, and water can be evaporated on the other side to generate cold and heat energy.
又,本發明之化學蓄熱材料亦適合於有效利用自引擎或燃料電池等所排出之排氣之熱。例如排氣之熱可活用於:汽車之熱機運轉之縮短、提升乘客之環境舒適度、燃料費用之改善、藉由提高排氣觸媒之活性而降低排氣之有害程度等。尤其,引擎中因運轉所造成之負荷不一定,排氣輸出亦不穩定,因此,來自引擎之排氣熱之直接利用必然沒有效率且伴隨著不便。若利用本發明之化學蓄熱材料,則藉由將來自引擎之排氣熱暫時進行化學上之蓄熱,並視熱之需求輸出熱,藉此,可達到更理想的排氣熱之利用。 [實施例]In addition, the chemical heat storage material of the present invention is also suitable for effectively utilizing the heat of exhaust gas discharged from engines or fuel cells. For example, the heat of exhaust gas can be used to shorten the operation of the thermal engine of the car, improve the environmental comfort of passengers, improve fuel costs, and reduce the harmfulness of exhaust gas by increasing the activity of exhaust catalysts. In particular, the load caused by the operation of the engine is uncertain, and the exhaust gas output is also unstable. Therefore, the direct use of the exhaust heat from the engine is inevitably inefficient and accompanied by inconvenience. If the chemical heat storage material of the present invention is used, the exhaust heat from the engine is temporarily chemically stored and the heat is output according to the heat demand, thereby achieving a more ideal exhaust heat utilization. [Example]
以下舉出實施例進一步詳細說明本發明,但本發明並不限定於該等實施例。The present invention is further described in detail with reference to the following embodiments, but the present invention is not limited to these embodiments.
(評價方法) 對於藉由各實施例及比較例獲得之化學蓄熱材料,使用示差熱、熱重量同時測定裝置(DTG-60,島津製作所公司製造)進行熱評價。具體而言,於升溫速度10℃/min、大氣條件下、常壓條件,將添加了鹼金屬之化合物之化學蓄熱材料之試料加熱至300℃,未添加鹼金屬之化合物之化學蓄熱材料之試料加熱至350℃,此後,將溫度保持一定,經時地測定重量減少量。基於所獲得之重量減少值,計算出作為各化學蓄熱材料中之氫氧化鎂變化為氧化鎂之比率的反應率。(Evaluation method) The chemical thermal storage materials obtained by each embodiment and comparative example were thermally evaluated using a differential thermal and thermogravimetric simultaneous measuring device (DTG-60, manufactured by Shimadzu Corporation). Specifically, the sample of the chemical thermal storage material to which the alkali metal compound was added was heated to 300°C, and the sample of the chemical thermal storage material to which the alkali metal compound was not added was heated to 350°C at a heating rate of 10°C/min, under atmospheric conditions, and under normal pressure conditions. Thereafter, the temperature was kept constant and the weight loss was measured over time. Based on the obtained weight loss value, the reaction rate, which is the ratio of magnesium hydroxide in each chemical thermal storage material to magnesium oxide, was calculated.
反應率之計算係以如下方式進行:為了排除揮發成分等之影響,將升溫至200℃之時間點之化學蓄熱材料之重量作為開始重量並設定為反應率0%,將假設氫氧化鎂全部變化為氧化鎂之情形下之重量減少值設定為反應率100%。The reaction rate is calculated as follows: In order to exclude the influence of volatile components, the weight of the chemical thermal storage material at the time when the temperature is raised to 200°C is set as the starting weight and the reaction rate is set to 0%, and the weight loss value assuming that all magnesium hydroxide is converted into magnesium oxide is set as the reaction rate of 100%.
化學蓄熱材料之性能評價特別是基於如下反應率而進行:將樣品溫度到達200℃之時間點設為0秒,其後,自經過2000秒之時間點的重量減少值所計算出之反應率。結果顯示,該反應率愈高,則吸熱脫水反應愈快速進行,蓄熱量愈大,且可藉由更低溫之熱進行蓄熱。再者,表中之相對反應率之數字並非絕對值,而是表示將各比較例之反應率設為基準之100時之相對值。The performance evaluation of chemical thermal storage materials is based on the following reaction rate: the time point when the sample temperature reaches 200°C is set as 0 seconds, and then the reaction rate is calculated from the weight loss value after 2000 seconds. The results show that the higher the reaction rate, the faster the endothermic dehydration reaction proceeds, the greater the heat storage capacity, and heat storage can be performed by lower temperature heat. In addition, the relative reaction rate numbers in the table are not absolute values, but relative values when the reaction rate of each comparative example is set to the benchmark of 100.
於本實施例及比較例使用之氫氧化鎂係使用本發明者等所製造者。 氫氧化鎂之純度係使用多元素同時螢光X射線分析裝置(Simultix12,Rigaku Corporation製造)測定各種雜質之含量,將成為主要之雜質的Ca、Si、Al、Fe、P、S之氧化物換算後之含量、與Cl含量自100%一併減掉而算出。 硼含量係將試料完全溶解後,使用ICP發光分光分析裝置(Hitachi High-Tech Corporation製造之商品名「PS3520 VDD」)測得。 氟含量係藉由離子電極法(裝置名稱:離子計D-53S,堀場製作所股份有限公司製造)測定「將試料以鹽酸溶解製備而得之溶液中之氟量」。 BET比表面積係使用比表面積測定裝置(Macsorb、Mountech Co. Ltd.製造),以使用氮氣之氣體吸附法(BET法)測得。 體積平均粒徑係使用雷射繞射散射式粒度分布測定裝置(MT3300,日機裝股份有限公司製造)測定。The magnesium hydroxide used in this embodiment and comparative example is produced by the inventors of the present invention. The purity of magnesium hydroxide is determined by measuring the contents of various impurities using a multi-element simultaneous fluorescent X-ray analyzer (Simultix12, manufactured by Rigaku Corporation), and the contents of the oxides of Ca, Si, Al, Fe, P, and S, which are the main impurities, are converted and calculated together with the Cl content from 100%. The boron content is measured by using an ICP emission spectrometer (trade name "PS3520 VDD" manufactured by Hitachi High-Tech Corporation) after the sample is completely dissolved. The fluorine content was measured by the ion electrode method (device name: ion meter D-53S, manufactured by Horiba, Ltd.) to determine the amount of fluorine in a solution prepared by dissolving a sample in hydrochloric acid. The BET specific surface area was measured by a specific surface area measuring device (Macsorb, manufactured by Mountech Co. Ltd.) using a gas adsorption method (BET method) using nitrogen. The volume average particle size was measured by a laser diffraction scattering particle size distribution measuring device (MT3300, manufactured by Nikkiso Co., Ltd.).
(實施例1) 秤量氫氧化鎂(純度約99%,BET比表面積40 m2 /g,體積平均粒徑4.2 μm)5g,進而,秤量相對於該氫氧化鎂硼含量成為440 ppm之量的硼酸(關東化學試藥,特級),進而,秤量相對於該氫氧化鎂氟含量成為10 ppm之量的氟化鎂(關東化學試藥,特級)。 使秤量所得之硼酸與氟化鎂完全溶解於離子交換水50 ml中而獲得水溶液。於該水溶液投入上述所秤量之氫氧化鎂,使用磁攪拌器以300秒、轉數200(rpm)之條件進行攪拌而製作漿料。 將該漿料以乾燥機(Advantech Co., Ltd.製造,DRA430DA)以110℃、乾燥12小時以上去除水分,藉此製造化學蓄熱材料。對所獲得之化學蓄熱材料以上述評價方法確認熱行為並計算出反應率。(Example 1) Weigh 5 g of magnesium hydroxide (purity of about 99%, BET specific surface area of 40 m2 /g, volume average particle size of 4.2 μm), and further weigh boric acid (Kanto Chemical Reagents, special grade) in an amount to make the boron content of the magnesium hydroxide 440 ppm, and further weigh magnesium fluoride (Kanto Chemical Reagents, special grade) in an amount to make the fluorine content of the magnesium hydroxide 10 ppm. The weighed boric acid and magnesium fluoride are completely dissolved in 50 ml of ion exchange water to obtain an aqueous solution. The weighed magnesium hydroxide is added to the aqueous solution, and stirred with a magnetic stirrer for 300 seconds at 200 rpm to prepare a slurry. The slurry was dried in a dryer (Advantech Co., Ltd., DRA430DA) at 110°C for more than 12 hours to remove moisture, thereby manufacturing a chemical thermal storage material. The thermal behavior of the obtained chemical thermal storage material was confirmed by the above-mentioned evaluation method and the reaction rate was calculated.
(實施例2) 除了以使硼之含量成為660 ppm之方式使用硼酸以外,以與實施例1相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Example 2) Except that boric acid was used so that the boron content was 660 ppm, the chemical thermal storage material was manufactured in the same manner as in Example 1, and the reaction rate was calculated in the same manner.
(實施例3) 除了以使硼之含量成為440 ppm、氟之含量成為220 ppm之方式使用硼酸及氟化鎂以外,以與實施例1相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Example 3) Except that boric acid and magnesium fluoride were used so that the boron content was 440 ppm and the fluorine content was 220 ppm, a chemical thermal storage material was manufactured in the same manner as in Example 1, and the reaction rate was calculated in the same manner.
(比較例1) 除了以使硼之含量成為1030 ppm、氟之含量成為800 ppm之方式使用硼酸及氟化鎂以外,以與實施例1相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Comparative Example 1) Except that boric acid and magnesium fluoride were used so that the boron content was 1030 ppm and the fluorine content was 800 ppm, a chemical thermal storage material was produced in the same manner as in Example 1, and the reaction rate was calculated in the same manner.
(實施例4) 秤量氫氧化鎂(與實施例1相同)5g,進而,秤量相對於該氫氧化鎂成為10 mol%之量的氯化鋰・1水合物(關東化學試藥,特級,純度98.0%),進而,秤量相對於該氫氧化鎂硼含量成為400 ppm之量的硼酸(關東化學試藥,特級),進而,秤量相對於該氫氧化鎂氟含量成為10 ppm之量的氟化鎂(關東化學試藥,特級)。 使秤量所得之氯化鋰・1水合物完全溶解於離子交換水50 ml中而獲得水溶液。於該水溶液投入上述所秤量之氫氧化鎂、硼酸及氟化鎂,使用磁攪拌器以300秒、轉數200(rpm)之條件進行攪拌而製作漿料。 將該漿料以乾燥機(Advantech Co., Ltd.製造,DRA430DA)以110℃、乾燥12小時以上去除水分,藉此製造化學蓄熱材料。對所獲得之化學蓄熱材料以上述評價方法確認熱行為並計算出反應率。(Example 4) Weigh 5 g of magnesium hydroxide (same as in Example 1), and further weigh lithium chloride monohydrate (Kanto Chemical Reagents, special grade, purity 98.0%) in an amount of 10 mol% relative to the magnesium hydroxide, and further weigh boric acid (Kanto Chemical Reagents, special grade) in an amount of 400 ppm relative to the boron content of the magnesium hydroxide, and further weigh magnesium fluoride (Kanto Chemical Reagents, special grade) in an amount of 10 ppm relative to the fluorine content of the magnesium hydroxide. The weighed lithium chloride monohydrate is completely dissolved in 50 ml of ion exchange water to obtain an aqueous solution. The above-weighed magnesium hydroxide, boric acid and magnesium fluoride were added to the aqueous solution, and stirred with a magnetic stirrer at 200 rpm for 300 seconds to prepare a slurry. The slurry was dried in a dryer (manufactured by Advantech Co., Ltd., DRA430DA) at 110°C for more than 12 hours to remove moisture, thereby preparing a chemical thermal storage material. The thermal behavior of the obtained chemical thermal storage material was confirmed by the above-mentioned evaluation method and the reaction rate was calculated.
(實施例5) 除了以使硼之含量成為600 ppm之方式使用硼酸以外,以與實施例4相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Example 5) Except that boric acid was used so that the boron content was 600 ppm, the chemical thermal storage material was manufactured in the same manner as in Example 4, and the reaction rate was calculated in the same manner.
(實施例6) 除了以使硼之含量成為440 ppm、氟之含量成為200 ppm之方式使用硼酸及氟化鎂以外,以與實施例4相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Example 6) Except that boric acid and magnesium fluoride were used so that the boron content was 440 ppm and the fluorine content was 200 ppm, a chemical thermal storage material was manufactured in the same manner as in Example 4, and the reaction rate was calculated in the same manner.
(實施例7) 除了以使硼之含量成為1030 ppm、氟之含量成為10 ppm之方式使用硼酸及氟化鎂以外,以與實施例4相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Example 7) Except that boric acid and magnesium fluoride were used in such a way that the boron content was 1030 ppm and the fluorine content was 10 ppm, a chemical thermal storage material was manufactured in the same manner as in Example 4, and the reaction rate was calculated in the same manner.
(比較例2) 除了以使硼之含量成為1060 ppm、氟之含量成為800 ppm之方式使用硼酸及氟化鎂以外,以與實施例4相同之方法製造化學蓄熱材料,並同樣計算出反應率。(Comparative Example 2) Except that boric acid and magnesium fluoride were used so that the boron content was 1060 ppm and the fluorine content was 800 ppm, a chemical thermal storage material was produced in the same manner as in Example 4, and the reaction rate was calculated in the same manner.
將結果表示於表1及表2。表1中,將以比較例1所獲得之化學蓄熱材料之反應率設為基準之100,並表示將各實施例所獲得之反應率轉換為相對反應率而得到之數字。表2中,則將以比較例2所獲得之化學蓄熱材料之反應率設為基準之100,並表示將各實施例所獲得之反應率轉換為相對反應率而得到之數字。The results are shown in Tables 1 and 2. In Table 1, the reaction rate of the chemical thermal storage material obtained in Comparative Example 1 is set as 100 as the standard, and the reaction rates obtained in each embodiment are converted into relative reaction rates. In Table 2, the reaction rate of the chemical thermal storage material obtained in Comparative Example 2 is set as 100 as the standard, and the reaction rates obtained in each embodiment are converted into relative reaction rates.
[表1]
(氫氧化鎂系)
[表2]
(氯化鋰添加系)
根據表1,可確認硼及氟之合計含量為10 ppm以上未達1200 ppm之範圍內之實施例1~3之化學蓄熱材料與比較例1於相同評價條件下,相較於比較例1,吸熱脫水反應更迅速地進行。由此可知,實施例1~3之化學蓄熱材料相較於比較例1之化學蓄熱材料蓄熱量較大,又,可以更低溫之熱進行蓄熱。According to Table 1, it can be confirmed that the chemical thermal storage materials of Examples 1 to 3, whose total content of boron and fluorine is within the range of 10 ppm or more and less than 1200 ppm, and Comparative Example 1, under the same evaluation conditions, have a faster endothermic dehydration reaction than Comparative Example 1. It can be seen that the chemical thermal storage materials of Examples 1 to 3 have a larger heat storage capacity than the chemical thermal storage material of Comparative Example 1, and can store heat at a lower temperature.
根據表2,可確認於氫氧化鎂添加氯化鋰10 mol%,且硼及氟之合計含量為10 ppm以上未達1200 ppm之範圍內之實施例4~7之化學蓄熱材料與比較例2於相同評價條件下,相較於比較例2,吸熱脫水反應更迅速地進行。由此可知,實施例4~7之化學蓄熱材料相較於比較例2之化學蓄熱材料蓄熱量較大,又,可以更低溫之熱進行蓄熱。According to Table 2, it can be confirmed that the chemical thermal storage materials of Examples 4 to 7 in which 10 mol% of lithium chloride is added to magnesium hydroxide and the total content of boron and fluorine is within the range of 10 ppm or more and less than 1200 ppm and Comparative Example 2, under the same evaluation conditions, the endothermic dehydration reaction proceeds more rapidly than that of Comparative Example 2. It can be seen that the chemical thermal storage materials of Examples 4 to 7 have a larger heat storage capacity than the chemical thermal storage material of Comparative Example 2, and can store heat at a lower temperature.
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