JP2008179709A - Heat storage material - Google Patents
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- JP2008179709A JP2008179709A JP2007014650A JP2007014650A JP2008179709A JP 2008179709 A JP2008179709 A JP 2008179709A JP 2007014650 A JP2007014650 A JP 2007014650A JP 2007014650 A JP2007014650 A JP 2007014650A JP 2008179709 A JP2008179709 A JP 2008179709A
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- potassium dititanate
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- 238000005338 heat storage Methods 0.000 title claims abstract description 68
- 239000011232 storage material Substances 0.000 title claims abstract description 43
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 30
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 30
- 239000011591 potassium Substances 0.000 claims abstract description 30
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 claims 1
- 239000004615 ingredient Substances 0.000 claims 1
- 230000036571 hydration Effects 0.000 abstract description 20
- 238000006703 hydration reaction Methods 0.000 abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000010410 layer Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 11
- 239000002918 waste heat Substances 0.000 description 11
- 230000008859 change Effects 0.000 description 8
- 229910001414 potassium ion Inorganic materials 0.000 description 8
- 239000010936 titanium Substances 0.000 description 8
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 8
- 239000013078 crystal Substances 0.000 description 7
- 230000017525 heat dissipation Effects 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 230000018044 dehydration Effects 0.000 description 6
- 238000006297 dehydration reaction Methods 0.000 description 6
- 239000011777 magnesium Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 230000007704 transition Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- -1 salt hydrates Chemical class 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000005968 1-Decanol Substances 0.000 description 1
- 241000172160 Caloria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910013803 LiOH—NaOH Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005496 eutectics Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- HBTFASPVVFSRRI-UHFFFAOYSA-N manganese(2+);dinitrate;hydrate Chemical compound O.[Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O HBTFASPVVFSRRI-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- LTUDISCZKZHRMJ-UHFFFAOYSA-N potassium;hydrate Chemical compound O.[K] LTUDISCZKZHRMJ-UHFFFAOYSA-N 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
本発明は、ボイラー、冷暖房機器、給湯機器などからの廃熱や太陽熱を貯蔵し、適時熱源として有効活用できる蓄熱材料に関する。 The present invention relates to a heat storage material that can store waste heat and solar heat from boilers, air conditioning equipment, hot water supply equipment, and the like and can be effectively used as a timely heat source.
近年、快適な居住空間あるいは工業製品の生産現場において、ボイラー、冷暖房機器、給湯機器などの冷温熱機器は必要不可欠であり、これらの機器によるエネルギー消費量の増大は、石油消費量の増加を引き起こすだけでなく、多大な環境負荷をもたらすため、エネルギー消費量削減に向けた種々の取り組みが活発におこなわれている。
日本で消費される全一次エネルギーの約66%は廃熱で未利用であるという統計があるが、これら廃熱は温度が低く、少なくとも200℃以下の廃熱は利用が難しいという課題を有している。
In recent years, cooling and heating equipment such as boilers, air conditioning equipment, and hot water supply equipment are indispensable in comfortable living spaces or industrial product production sites, and the increase in energy consumption by these equipment causes an increase in oil consumption. In addition, in order to bring about a great environmental load, various efforts for reducing energy consumption are being actively carried out.
There is a statistic that about 66% of the total primary energy consumed in Japan is unused in waste heat, but these waste heat is low in temperature and has the problem that waste heat of at least 200 ° C is difficult to use. ing.
蓄熱材料による廃熱回収は、比較的安価な材料を使用し、簡単な設備で廃熱の回収が可能で、蓄えた熱を適時、熱として取り出すことが可能である。蓄熱材料は、その熱を蓄える機構の違いから主として顕熱蓄熱材料と潜熱蓄熱材料とに分類される。 Waste heat recovery using a heat storage material uses a relatively inexpensive material, enables the recovery of waste heat with simple equipment, and allows the stored heat to be taken out as heat in a timely manner. Thermal storage materials are mainly classified into sensible heat storage materials and latent heat storage materials based on the difference in mechanisms for storing the heat.
顕熱蓄熱材料は、物質の温度変化を伴って熱を蓄える材料である。低温TLの物質に熱エネルギーが流入し、温度THになった時、その物質の蓄熱量QS(J)は、その物質の比熱をC、密度をρ、体積をVとすると、次式で表される。ただし、比熱Cは一定と仮定する。
QS =CρV(TH−TL)・・・・・・・・・(1)
The sensible heat storage material is a material that stores heat with a temperature change of a substance. Thermal energy flows into material of the low-temperature T L, when it becomes the temperature T H, the amount of heat stored material Q S (J) is the specific heat of the material C, and the density [rho, when the volume is V, the following It is expressed by a formula. However, it is assumed that the specific heat C is constant.
Q S = CρV (T H -T L) ········· (1)
すなわち、物質の温度を上昇させる過程が蓄熱であり、温度を下げる過程が放熱である。温度が変動する廃熱に対しては、その温度変化に連動して蓄熱または放熱が起こる。蓄熱量QSは温度差(TH−TL)および物質の熱容量CρVに比例して変化するので、大きな温度差をつけるか、もしくは大きな熱容量の蓄熱材料を使用すれば蓄えられる熱量は増加する。 That is, the process of increasing the temperature of the substance is heat storage, and the process of decreasing the temperature is heat dissipation. For waste heat whose temperature fluctuates, heat storage or heat dissipation occurs in conjunction with the temperature change. Since the heat storage amount Q S changes in proportion to the temperature difference (T H −T L ) and the heat capacity CρV of the substance, the amount of stored heat increases if a large temperature difference is provided or a heat storage material having a large heat capacity is used. .
顕熱蓄熱材料としては、288K付近で水(比熱4.18J/gK)、カロリアHT43(エクソン社製、比熱2.77J/gK)、サーミノールT66(モンサント社製、比熱2.77J/gK)、シルサーム800(ダウコーニング社製、比熱2.10J/gK)、コンクリートブロック(比熱0.88J/gK)、砂利(比熱0.88J/gK)、マグネシアレンガ(比熱0.88J/gK)などが知られている。 As the sensible heat storage material, water (specific heat 4.18 J / gK), calorie HT43 (Exxon, specific heat 2.77 J / gK), Therminol T66 (Monsanto, specific heat 2.77 J / gK), around 288 K, Siltherm 800 (Dow Corning, specific heat 2.10 J / gK), concrete block (specific heat 0.88 J / gK), gravel (specific heat 0.88 J / gK), magnesia brick (specific heat 0.88 J / gK), etc. are known. It has been.
水は化学的に安定で、比熱も大きいため、非常に優れた顕熱蓄熱材料であるが、沸点が低いため大気開放下において100℃以上の廃熱では使用できない。それに対しカロリアHT43など有機熱媒体は、沸点が高いため200℃付近の廃熱にも使用できるが、比熱が水に比べて小さいため、より比熱の大きな材料の開発が熱望されている。さらに、マグネシアレンガなどは耐熱性に優れており、温度差を500℃以上とれば蓄熱量は大きくなるが、200℃以下の低品位廃熱に対しては比熱が非常に小さいことから蓄熱量が小さく、有望な材料とは言えない。 Although water is chemically stable and has a large specific heat, it is a very excellent sensible heat storage material. However, since it has a low boiling point, it cannot be used with waste heat of 100 ° C. or higher in the open atmosphere. On the other hand, an organic heat medium such as Caloria HT43 has a high boiling point and can be used for waste heat around 200 ° C. However, since the specific heat is smaller than that of water, development of a material having a larger specific heat is eagerly desired. Furthermore, magnesia bricks and the like are excellent in heat resistance, and if the temperature difference is 500 ° C. or more, the heat storage amount becomes large, but the heat storage amount is low because the specific heat is very small for low-grade waste heat of 200 ° C. or less. It is a small and promising material.
一方の潜熱蓄熱材料は、物質の相変化または転移に伴う潜熱を利用して熱を蓄える材料で、主として材料固有の融点または転移点で蓄熱および放熱が行われる。したがって、潜熱蓄熱材料の融点または転移点以上にならないと大きな蓄熱量は得られず、逆に蓄えられた熱は融点または転移点未満にならないと放熱が行われることはない。廃熱の温度が変動する場合には、数種類の潜熱蓄熱材料を併用するなどの方法があるが、化学的性質や物理的性質が一致しないなどの問題があり、効率的な蓄熱システムの構築ができなかった。しかし最近では、融点が簡便な方法で変えられる潜熱蓄熱材料として硝酸マンガン水和物が提案されている(特許文献1参照)。 One latent heat storage material is a material that stores heat using latent heat associated with phase change or transition of a substance, and heat storage and heat dissipation are mainly performed at a melting point or a transition point unique to the material. Therefore, a large amount of heat storage cannot be obtained unless the melting point or transition point of the latent heat storage material is exceeded, and conversely, heat is not released unless the stored heat is less than the melting point or transition point. When the temperature of waste heat fluctuates, there are methods such as using several types of latent heat storage materials in combination, but there are problems such as inconsistencies in chemical properties and physical properties, and an efficient heat storage system can be constructed. could not. Recently, however, manganese nitrate hydrate has been proposed as a latent heat storage material whose melting point can be changed by a simple method (see Patent Document 1).
潜熱が大きい材料の例を挙げると、融点または転移点が2℃〜94℃においては、炭化水素類で1−デカノール(潜熱206J/g)、C16パラフィン(潜熱200J/g)などがあり、無機塩水和物ではSr(OH)2・8H2O(潜熱351J/g)、Ba(OH)2・8H2O(潜熱293J/g)、Na2SO4・10H2O(潜熱200J/g)、Na2CH3COO・3H2O(潜熱251J/g)などがある。さらに133℃〜250℃ではペンタエリスリトール(潜熱322J/g)、LiOH−NaOH共晶塩(潜熱362J/g)、尿素(潜熱251J/g)などがある(非特許文献1〜3、特許文献2参照)。
潜熱が大きい材料は、融解、凝固、または転移を繰り返すため物質の分解、変質などが起こりやすく、可燃物または劇物あるいは腐食性を有する物質が多いことが欠点である。
Examples of materials having a large latent heat include hydrocarbons such as 1-decanol (latent heat 206 J / g), C16 paraffin (latent heat 200 J / g), and the like at inorganic or inorganic transition temperatures of 2 ° C. to 94 ° C. For salt hydrates, Sr (OH) 2 .8H 2 O (latent heat 351 J / g), Ba (OH) 2 .8H 2 O (latent heat 293 J / g), Na 2 SO 4 .10H 2 O (latent heat 200 J / g) Na 2 CH 3 COO.3H 2 O (latent heat 251 J / g). Further, at 133 ° C. to 250 ° C., there are pentaerythritol (latent heat 322 J / g), LiOH-NaOH eutectic salt (latent heat 362 J / g), urea (latent heat 251 J / g), and the like (
A material having a large latent heat is likely to be decomposed or altered due to repeated melting, solidification, or transition, and is disadvantageous in that there are many combustible or deleterious substances or corrosive substances.
前記の欠点を解消できるものとして、見かけ比重が0.5〜1.1である酸化アルミニウムを含む蓄熱材料が提案されている。この蓄熱材料の蓄熱、放熱は従来の機構と異なり、酸化アルミニウムへの水分の吸着、脱離を利用している。基本原理は活性アルミナに吸着した水分子の脱離による蓄熱と水分子の再吸着による放熱を利用しているため、化学的に安定で、蓄熱量は150℃の加熱による水分子の脱離で282J/g程度が得られている(特許文献3参照)。しかし、見掛け比重が0.5〜1.1であるため、体積当たりの蓄熱量は小さい。 In order to eliminate the above-described drawbacks, a heat storage material containing aluminum oxide having an apparent specific gravity of 0.5 to 1.1 has been proposed. Unlike the conventional mechanism, the heat storage and heat dissipation of this heat storage material utilizes the adsorption and desorption of moisture to aluminum oxide. Since the basic principle uses heat storage by desorption of water molecules adsorbed on activated alumina and heat release by re-adsorption of water molecules, it is chemically stable and the amount of heat storage is desorption of water molecules by heating at 150 ° C. About 282 J / g is obtained (see Patent Document 3). However, since the apparent specific gravity is 0.5 to 1.1, the heat storage amount per volume is small.
そして最近では、体積当たりの蓄熱量を向上させた蓄熱材料として、一般式K2Ti2O5−x・nH2O(0≦x≦1、0≦n≦2.7)で表記される二チタン酸カリウム水和物を主成分とする蓄熱材料が提案されている。この蓄熱材料はTiO5三角両錘体が連鎖した層状構造を有し、層間に配置されたK+イオンの水和による放熱と脱水和による蓄熱を利用しており、その蓄熱量は306J/g(780J/cm3)と非常に大きな値を示す(特許文献4参照)。また、「H2O量を示すnは、理論的データではないが、実験から求めた最大値は2.7である。」と記載されている(特許文献4第5頁段落0016)。
しかしながら、上記特許文献4に記載の一般式K2Ti2O5−x・nH2O(0≦x≦1、0≦n≦2.7)で表記される二チタン酸カリウム水和物を主成分とする蓄熱材料もコスト対効果の観点から評価すると蓄熱量は十分とは言えず、改善の余地があった。蓄熱量の更なる増加のための新規蓄熱材料の開発または従来の蓄熱材料の改良が要望されている。
However, potassium dititanate hydrate represented by the general formula K 2 Ti 2 O 5-x · nH 2 O (0 ≦ x ≦ 1, 0 ≦ n ≦ 2.7) described in
本発明の目的は、従来技術の上記問題点を解決し、蓄熱、放熱が容易で、大きな蓄熱量を有する蓄熱材料を提供することである。 An object of the present invention is to solve the above-mentioned problems of the prior art, and to provide a heat storage material that is easy to store and release heat and has a large amount of stored heat.
本発明によれば、一般式K2−yMg(y/2)Ti2O5−x・nH2O(0≦x≦1、0<y<0.5)で表記される二チタン酸カリウム塩水和物を主成分とすることを特徴とする蓄熱材料であって、前記二チタン酸カリウム塩水和物を水和させたときの前記nの最大値が2.7を超える値であることを特徴とする蓄熱材料が提供される。 According to the present invention, dititanate indicated by the general formula K 2-y Mg (y / 2) Ti 2 O 5-x · nH 2 O (0 ≦ x ≦ 1,0 <y <0.5) A heat storage material comprising potassium salt hydrate as a main component, wherein the maximum value of n exceeds 2.7 when the potassium dititanate hydrate is hydrated A heat storage material characterized by the above is provided.
本発明によれば、蓄熱、放熱が容易で、大きな蓄熱量を有する蓄熱材料が提供される。 ADVANTAGE OF THE INVENTION According to this invention, heat storage and heat dissipation are easy, and the thermal storage material which has a big thermal storage amount is provided.
本発明における二チタン酸カリウムの一般式は、通常K2Ti2O5と表記されるが正確にはK2Ti2O5−xであり、xは合成温度および合成雰囲気中の酸素分圧によって変化する。
合成温度が低いほど、また合成雰囲気中の酸素分圧が高いほどxは0に近づく。
また、xを1以下とすることにより、二チタン酸カリウムとしての結晶構造を取ることができ、本発明の目的を達する物性とすることができる。なお、xを1より大きくするには強力な還元雰囲気で合成する必要がある。
The general formula of potassium dititanate in the present invention is usually expressed as K 2 Ti 2 O 5 , but is exactly K 2 Ti 2 O 5-x , where x is the synthesis temperature and oxygen partial pressure in the synthesis atmosphere. It depends on.
As the synthesis temperature is lower and the oxygen partial pressure in the synthesis atmosphere is higher, x approaches 0.
Further, by setting x to 1 or less, a crystal structure as potassium dititanate can be obtained, and physical properties that can achieve the object of the present invention can be achieved. In order to make x larger than 1, it is necessary to synthesize in a strong reducing atmosphere.
二チタン酸カリウムの結晶構造は、TiO5三角両錘体が連鎖した層状構造を有し、TiO5三角両錘体からなる層と層との間にK+イオンが配置されていると考えられている。結晶構造から推察すると、xは0に近いほど格子欠陥の少ない安定な状態と考えられ、本発明の蓄熱材料に最も適している。 The crystal structure of potassium dititanate has a layered structure in which TiO 5 triangular pyramidal bodies are linked, and it is considered that K + ions are arranged between the layers made of TiO 5 triangular pyramidal bodies. ing. Inferring from the crystal structure, x is considered to be a stable state with fewer lattice defects as it is closer to 0, and is most suitable for the heat storage material of the present invention.
このような層状構造結晶は、層間に配置されたK+イオンが容易に水和され、一般式としてK2Ti2O5−x・nH2Oで表記される二チタン酸カリウム水和物となる。このとき、H2O分子は、K+イオンに誘導されるようにTiO5三角両錘体からなる層間にゲストとして侵入する。H2O分子が侵入するとTiO5三角両錘体からなる層と層との間隔は膨張するが、結晶構造は変化しない。 In such a layered structure crystal, K + ions arranged between the layers are easily hydrated, and potassium dititanate hydrate represented by the general formula K 2 Ti 2 O 5-x · nH 2 O Become. At this time, H 2 O molecules enter as a guest between the layers made of TiO 5 triangular pyramidal bodies so as to be induced by K + ions. When H 2 O molecules enter, the distance between the layers composed of TiO 5 triangular pyramidal bodies expands, but the crystal structure does not change.
さらに、上記の二チタン酸カリウム水和物を加熱するとTiO5三角両錘体からなる層間にゲストとして侵入していたH2O分子は層間から脱離し、膨張したTiO5三角両錘体からなる層間は収縮し元の状態に戻る。
この反応は、一種のトポケミカルな反応と考えられ、結晶構造の変化を伴わないため、二チタン酸カリウム水和物は、水和、脱水和の繰り返しに対して極めて安定である。
すなわち、放熱と吸熱の繰り返しに対して安定で、安全な蓄熱材料ができる。
Further, when the above potassium dititanate hydrate is heated, the H 2 O molecules that have invaded as a guest between the layers composed of the TiO 5 triangular pyramidal bodies are desorbed from the layers, and are composed of the expanded TiO 5 triangular pyramidal bodies. The interlayer shrinks and returns to its original state.
This reaction is considered to be a kind of topochemical reaction and is not accompanied by a change in crystal structure. Therefore, potassium dititanate hydrate is extremely stable against repeated hydration and dehydration.
That is, a heat storage material that is stable and safe against repeated heat dissipation and heat absorption can be obtained.
本発明における二チタン酸カリウム水和物の水和量nは、水和、脱水和に伴ってその値が変化する。
脱水和させたときのnの最小値は、0より大きい値であることが好ましい。こうすることにより、脱水和状態でも、H2O分子がTiO5三角両錘体からなる層間に残留することで層間が広がり、それによって層間に配置されたK+イオンの水和速度が遅くなるのを防げる。さらに、脱水和させたときのnの最小値は、1.3以上の値であることがより好ましい。こうすることにより、水和速度がより速くなる。
水和させたときのnの最大値は、2.7より大きい値であることが好ましい。こうすることにより従来の蓄熱材料よりも大きな蓄熱量を得ることができる。さらに、水和させたときのnの最大値は、3.5より大きい値であることがより好ましい。こうすることにより、さらに大きな蓄熱量が得られる。
The hydration amount n of potassium dititanate hydrate in the present invention varies with hydration and dehydration.
The minimum value of n when dehydrated is preferably a value greater than zero. By doing so, even in the dehydrated state, the H 2 O molecule remains between the layers made of TiO 5 triangular pyramidal bodies, so that the layers are expanded, thereby slowing the hydration rate of K + ions arranged between the layers. Can be prevented. Furthermore, the minimum value of n when dehydrated is more preferably a value of 1.3 or more. By doing this, the hydration rate is faster.
The maximum value of n when hydrated is preferably greater than 2.7. By doing so, it is possible to obtain a larger amount of heat storage than conventional heat storage materials. Furthermore, the maximum value of n when hydrated is more preferably a value greater than 3.5. By doing so, a larger amount of heat storage can be obtained.
さらに層間に配置されたK+イオンの一部は、アルカリ土類金属の中でイオン半径が最も近いMg2+イオンと置換が可能である。Mg2+イオンの水和エネルギーは、K+イオンの水和エネルギーより約18%大きいため、二チタン酸カリウム水和物の結晶構造が維持できる組成範囲で置換すると蓄熱量が増大する。 Furthermore, some of the K + ions arranged between the layers can be replaced with Mg 2+ ions having the closest ionic radius among the alkaline earth metals. Since the hydration energy of Mg 2+ ions is approximately 18% greater than the hydration energy of K + ions, the amount of heat storage increases when substitution is made within a composition range in which the crystal structure of potassium dititanate hydrate can be maintained.
本発明における一般式K2−yMg(y/2)Ti2O5−x・nH2Oにおいて、yは好ましくは0より大きくする。こうすることにより、K+イオンがMg2+イオンに置換されて、蓄熱量が増大する。
また、yは好ましくは0.5より小さくする。こうすることにより、二チタン酸カリウム水和物にMgTiO3が混入し、蓄熱量は急激に低下するのを防げる。
In the general formula K 2-y Mg (y / 2) Ti 2 O 5-x · nH 2 O in the present invention, y is preferably larger than 0. By doing so, K + ions are replaced with Mg 2+ ions, and the amount of heat storage is increased.
Moreover, y is preferably smaller than 0.5. By doing so, it is possible to prevent MgTiO 3 from being mixed into the potassium dititanate hydrate and the heat storage amount to rapidly decrease.
二チタン酸カリウム塩には、熱伝導性を高めるために金属フィラー、黒鉛粒子などを混合し使用してもよく、さらには付着水による二チタン酸カリウム塩の分解を抑制するためにテフロン(登録商標)微粉末と混練した状態で使用しても構わない。 In order to increase thermal conductivity, potassium dititanate may be mixed with metal fillers, graphite particles, etc., and Teflon (registered to prevent decomposition of potassium dititanate by adhering water) (Trademark) You may use it in the state kneaded with fine powder.
本発明における蓄熱材料は、蓄熱、放熱の繰り返しによる分解や変質がなく、安全に使用ができる。特に30℃から200℃付近の温度域において蓄熱、放熱が容易である。
さらに、家屋におけるボイラー、冷暖房機器あるいは給湯機器などから排出される低品位熱エネルギーを回収し、再利用するコジェネレーションシステムに好適であるだけでなく、太陽熱エネルギーを回収し、昼間の冷房、夜間の暖房に利用するなどにも有効である。
The heat storage material in the present invention does not decompose or change due to repeated heat storage and heat dissipation, and can be used safely. In particular, it is easy to store and dissipate heat in the temperature range from 30 ° C. to 200 ° C.
Furthermore, not only is it suitable for a cogeneration system that collects and reuses low-grade thermal energy discharged from boilers, air-conditioning equipment, or hot-water equipment in homes, but it also collects solar thermal energy for daytime cooling and nighttime use. It is also effective for use in heating.
なお、本発明は前述の実施形態に限定されるものではなく、本発明の目的を達成できる範囲での変形、改良等は本発明に含まれるものである。 It should be noted that the present invention is not limited to the above-described embodiments, and modifications, improvements, and the like within the scope that can achieve the object of the present invention are included in the present invention.
以下、本発明を実施例に基づいて説明するが、本発明はこれに限定されるものではない。また、二チタン酸カリウム塩水和物に基づいて説明するが、二チタン酸カリウム塩水和物を主成分とする蓄熱材料であってもよい。
二チタン酸カリウム塩水和物はたとえば次のようにして作製される。
一般式K2−yMg(y/2)Ti2O5−x・nH2Oにおいて、y=0.0、0.1、0.2、0.4、0.5および1.0となるように炭酸カリウム(K2CO3)、炭酸マグネシウム(MgCO3)および酸化チタン(TiO2)を秤量し、これら粉末をメノウ乳鉢でよく混合、粉砕した。得られた混合粉末を白金坩堝に入れ、マッフル炉を用いて、気温20℃、相対湿度50%(水蒸気圧約1.2kPa)の空気中で30℃から950℃まで10℃/分で昇温後、950℃で48時間保持することで二チタン酸カリウム塩を合成した。
水和と脱水和を繰り返す処理を行なうため、上記のようにして合成された二チタン酸カリウム塩を恒温恒湿器に移し、水蒸気圧を1.2kPaに制御した空気中に30℃で24時間放置した後、恒温恒湿器を昇温し300℃で0.5時間放置し、降温した。この温度プログラムに従った処理を1回とし、この処理を3回繰り返し実施することにより、蓄熱材料としての二チタン酸カリウム塩水和物が得られた。
EXAMPLES Hereinafter, although this invention is demonstrated based on an Example, this invention is not limited to this. Moreover, although demonstrated based on potassium dititanate salt hydrate, the heat storage material which has potassium dititanate hydrate as a main component may be sufficient.
Potassium dititanate hydrate is prepared, for example, as follows.
In the general formula K 2-y Mg (y / 2) Ti 2 O 5-x · nH 2 O, and y = 0.0,0.1,0.2,0.4,0.5 and 1.0 Thus, potassium carbonate (K 2 CO 3 ), magnesium carbonate (MgCO 3 ) and titanium oxide (TiO 2 ) were weighed, and these powders were thoroughly mixed and pulverized in an agate mortar. The obtained mixed powder is put into a platinum crucible and heated at a rate of 10 ° C./min from 30 ° C. to 950 ° C. in air at a temperature of 20 ° C. and a relative humidity of 50% (water vapor pressure of about 1.2 kPa) using a muffle furnace. The potassium dititanate was synthesized by maintaining at 950 ° C. for 48 hours.
In order to perform a process of repeating hydration and dehydration, the potassium dititanate synthesized as described above was transferred to a thermo-hygrostat, and the water vapor pressure was controlled to 1.2 kPa at 30 ° C. for 24 hours. After leaving it to stand, the temperature-and-humidity chamber was heated and left at 300 ° C. for 0.5 hour to lower the temperature. The treatment according to this temperature program was performed once, and this treatment was repeated three times to obtain potassium dititanate hydrate as a heat storage material.
(結果)
上記のようにして得られた二チタン酸カリウム塩水和物の蓄熱量は次のようにして測定した。
二チタン酸カリウム塩水和物を気温20℃、相対湿度50%の空気中に72時間放置することで水和した後、示差熱分析装置を用い気温20℃、相対湿度50%の空気中で30℃から300℃まで1℃/分で昇温した。この昇温による脱水和に伴う吸熱量(J/g)を測定し、これを蓄熱量(J/g)とした。
二チタン酸カリウム塩水和物の水和は、気温20℃、相対湿度50%の空気中に72時間放置することで行った。このとき水和量nの値は最大値となる。二チタン酸カリウム塩水和物の脱水和は、上記水和の後、示差熱分析装置を用い気温20℃、相対湿度50%の空気中で30℃から300℃まで1℃/分で昇温して行った。このとき水和量nの値は最小値となる。
水和させたときと脱水和させたときでの二チタン酸カリウム塩水和物の重量をそれぞれ測定し、それらの重量差から水和量の変化Δnを求めた。また水和させたときの重量からnの最大値と、脱水和させたときの重量からnの最小値をそれぞれ算出した。
これらの結果を以下の表1に示す。
(result)
The heat storage amount of the potassium dititanate hydrate obtained as described above was measured as follows.
Hydration by allowing potassium dititanate hydrate to stand in air at a temperature of 20 ° C. and a relative humidity of 50% for 72 hours, followed by using a differential thermal analyzer in air at a temperature of 20 ° C. and a relative humidity of 50%. The temperature was raised from 1 ° C. to 300 ° C. at 1 ° C./min. The endothermic amount (J / g) associated with dehydration due to this temperature rise was measured, and this was defined as the heat storage amount (J / g).
Hydration of potassium dititanate hydrate was performed by leaving it in air at a temperature of 20 ° C. and a relative humidity of 50% for 72 hours. At this time, the value of the hydration amount n is the maximum value. The dehydration of potassium dititanate hydrate is carried out at a rate of 1 ° C./min from 30 ° C. to 300 ° C. in air at a temperature of 20 ° C. and a relative humidity of 50% using a differential thermal analyzer after the above hydration. I went. At this time, the value of the hydration amount n becomes the minimum value.
The weight of the potassium dititanate hydrate when hydrated and dehydrated was measured, and the change Δn in the amount of hydration was determined from the weight difference. Further, the maximum value of n was calculated from the weight when hydrated, and the minimum value of n was calculated from the weight when dehydrated.
These results are shown in Table 1 below.
実施例1はy=0.1、実施例2はy=0.2、実施例3はy=0.4、比較例1はy=0、比較例2はy=0.5、比較例3はy=1.0である。
蓄熱量は、0<y<0.5で比較例1を上回り、y=0.2で最大値408J/gであった。また、水和量の変化Δnは、0≦y≦0.4で2.7〜2.8であった。
Example 1 is y = 0.1, Example 2 is y = 0.2, Example 3 is y = 0.4, Comparative Example 1 is y = 0, Comparative Example 2 is y = 0.5, Comparative Example 3 is y = 1.0.
The amount of stored heat was 0 <y <0.5, which exceeded that of Comparative Example 1, and the maximum value was 408 J / g when y = 0.2. Moreover, the change Δn in the amount of hydration was 2.7 to 2.8 when 0 ≦ y ≦ 0.4.
図1は、比較例1と実施例2についての加熱温度と水和量nの関係を示している。
比較例1と実施例2はいずれも水和量nの最大値は4.1であり、最小値は、1.4であった。
FIG. 1 shows the relationship between the heating temperature and the hydration amount n for Comparative Example 1 and Example 2.
In both Comparative Example 1 and Example 2, the maximum value of hydration amount n was 4.1, and the minimum value was 1.4.
Claims (4)
前記二チタン酸カリウム塩水和物を水和させたときの前記nの最大値が2.7を超える値であることを特徴とする蓄熱材料。 Formula K 2-y Mg (y / 2) Ti 2 O 5-x · nH 2 O (0 ≦ x ≦ 1,0 <y <0.5) the main two potassium titanate hydrate, denoted by A heat storage material characterized by being an ingredient,
The heat storage material, wherein the maximum value of n when the potassium dititanate hydrate is hydrated exceeds 2.7.
蓄熱量が360J/g以上であることを特徴とする蓄熱材料。 The heat storage material according to any one of claims 1 to 3,
A heat storage material having a heat storage amount of 360 J / g or more.
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