JP6967943B2 - Heat storage material composition - Google Patents
Heat storage material composition Download PDFInfo
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- JP6967943B2 JP6967943B2 JP2017220392A JP2017220392A JP6967943B2 JP 6967943 B2 JP6967943 B2 JP 6967943B2 JP 2017220392 A JP2017220392 A JP 2017220392A JP 2017220392 A JP2017220392 A JP 2017220392A JP 6967943 B2 JP6967943 B2 JP 6967943B2
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- JP
- Japan
- Prior art keywords
- heat storage
- storage material
- material composition
- latent heat
- acid
- Prior art date
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- 238000005338 heat storage Methods 0.000 title claims description 167
- 239000011232 storage material Substances 0.000 title claims description 154
- 239000000203 mixture Substances 0.000 title claims description 101
- ULQISTXYYBZJSJ-UHFFFAOYSA-N 12-hydroxyoctadecanoic acid Chemical class CCCCCCC(O)CCCCCCCCCCC(O)=O ULQISTXYYBZJSJ-UHFFFAOYSA-N 0.000 claims description 58
- 239000000758 substrate Substances 0.000 claims description 56
- 239000000155 melt Substances 0.000 claims description 36
- 229920002725 thermoplastic elastomer Polymers 0.000 claims description 35
- 239000003349 gelling agent Substances 0.000 claims description 34
- 125000004432 carbon atom Chemical group C* 0.000 claims description 31
- 239000012188 paraffin wax Substances 0.000 claims description 31
- 229940114072 12-hydroxystearic acid Drugs 0.000 claims description 29
- 150000003440 styrenes Chemical class 0.000 claims description 27
- 229920006395 saturated elastomer Polymers 0.000 claims description 20
- 229920001400 block copolymer Polymers 0.000 claims description 18
- 150000003839 salts Chemical class 0.000 claims description 16
- 229920001971 elastomer Polymers 0.000 claims description 15
- 239000000806 elastomer Substances 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 12
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 10
- 238000004898 kneading Methods 0.000 claims description 9
- 150000001413 amino acids Chemical class 0.000 claims description 5
- 229920005996 polystyrene-poly(ethylene-butylene)-polystyrene Polymers 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- FMZUHGYZWYNSOA-VVBFYGJXSA-N (1r)-1-[(4r,4ar,8as)-2,6-diphenyl-4,4a,8,8a-tetrahydro-[1,3]dioxino[5,4-d][1,3]dioxin-4-yl]ethane-1,2-diol Chemical compound C([C@@H]1OC(O[C@@H]([C@@H]1O1)[C@H](O)CO)C=2C=CC=CC=2)OC1C1=CC=CC=C1 FMZUHGYZWYNSOA-VVBFYGJXSA-N 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 229940087101 dibenzylidene sorbitol Drugs 0.000 claims description 3
- 150000001735 carboxylic acids Chemical class 0.000 claims 2
- 238000005470 impregnation Methods 0.000 description 29
- 239000003921 oil Substances 0.000 description 29
- 238000002844 melting Methods 0.000 description 24
- 230000008018 melting Effects 0.000 description 24
- 238000002474 experimental method Methods 0.000 description 17
- 238000010438 heat treatment Methods 0.000 description 17
- 239000000463 material Substances 0.000 description 17
- 239000012071 phase Substances 0.000 description 16
- 238000012360 testing method Methods 0.000 description 16
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 14
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 9
- 238000000926 separation method Methods 0.000 description 9
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 8
- BXOUVIIITJXIKB-UHFFFAOYSA-N ethene;styrene Chemical group C=C.C=CC1=CC=CC=C1 BXOUVIIITJXIKB-UHFFFAOYSA-N 0.000 description 7
- 238000005227 gel permeation chromatography Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 7
- 239000004793 Polystyrene Substances 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- 229920002223 polystyrene Polymers 0.000 description 5
- 239000004711 α-olefin Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- RZJRJXONCZWCBN-UHFFFAOYSA-N alpha-octadecene Natural products CCCCCCCCCCCCCCCCCC RZJRJXONCZWCBN-UHFFFAOYSA-N 0.000 description 4
- 235000001014 amino acid Nutrition 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 description 4
- DCAYPVUWAIABOU-UHFFFAOYSA-N hexadecane Chemical compound CCCCCCCCCCCCCCCC DCAYPVUWAIABOU-UHFFFAOYSA-N 0.000 description 4
- VKOBVWXKNCXXDE-UHFFFAOYSA-N icosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCC(O)=O VKOBVWXKNCXXDE-UHFFFAOYSA-N 0.000 description 4
- 238000009413 insulation Methods 0.000 description 4
- 238000010998 test method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 150000002148 esters Chemical class 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- WQEPLUUGTLDZJY-UHFFFAOYSA-N pentadecanoic acid Chemical compound CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 3
- 229920002743 polystyrene-poly(ethylene-ethylene/propylene) block-polystyrene Polymers 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- ADOBXTDBFNCOBN-UHFFFAOYSA-N 1-heptadecene Chemical compound CCCCCCCCCCCCCCCC=C ADOBXTDBFNCOBN-UHFFFAOYSA-N 0.000 description 2
- GQEZCXVZFLOKMC-UHFFFAOYSA-N 1-hexadecene Chemical compound CCCCCCCCCCCCCCC=C GQEZCXVZFLOKMC-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 2
- 239000005639 Lauric acid Substances 0.000 description 2
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 239000004721 Polyphenylene oxide Chemical class 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 2
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- GHVNFZFCNZKVNT-UHFFFAOYSA-N decanoic acid Chemical compound CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 2
- 239000003480 eluent Substances 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- NDJKXXJCMXVBJW-UHFFFAOYSA-N heptadecane Chemical compound CCCCCCCCCCCCCCCCC NDJKXXJCMXVBJW-UHFFFAOYSA-N 0.000 description 2
- KEMQGTRYUADPNZ-UHFFFAOYSA-N heptadecanoic acid Chemical compound CCCCCCCCCCCCCCCCC(O)=O KEMQGTRYUADPNZ-UHFFFAOYSA-N 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 150000004668 long chain fatty acids Chemical class 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- VAMFXQBUQXONLZ-UHFFFAOYSA-N n-alpha-eicosene Natural products CCCCCCCCCCCCCCCCCCC=C VAMFXQBUQXONLZ-UHFFFAOYSA-N 0.000 description 2
- LQERIDTXQFOHKA-UHFFFAOYSA-N n-nonadecane Natural products CCCCCCCCCCCCCCCCCCC LQERIDTXQFOHKA-UHFFFAOYSA-N 0.000 description 2
- NHLUYCJZUXOUBX-UHFFFAOYSA-N nonadec-1-ene Chemical compound CCCCCCCCCCCCCCCCCC=C NHLUYCJZUXOUBX-UHFFFAOYSA-N 0.000 description 2
- CCCMONHAUSKTEQ-UHFFFAOYSA-N octadec-1-ene Chemical compound CCCCCCCCCCCCCCCCC=C CCCMONHAUSKTEQ-UHFFFAOYSA-N 0.000 description 2
- WWZKQHOCKIZLMA-UHFFFAOYSA-N octanoic acid Chemical compound CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 description 2
- SECPZKHBENQXJG-FPLPWBNLSA-N palmitoleic acid Chemical compound CCCCCC\C=C/CCCCCCCC(O)=O SECPZKHBENQXJG-FPLPWBNLSA-N 0.000 description 2
- 229920000570 polyether Chemical class 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 229960002920 sorbitol Drugs 0.000 description 2
- 229920006132 styrene block copolymer Polymers 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- 239000002025 wood fiber Substances 0.000 description 2
- WMFHUUKYIUOHRA-UHFFFAOYSA-N (3-phenoxyphenyl)methanamine;hydrochloride Chemical compound Cl.NCC1=CC=CC(OC=2C=CC=CC=2)=C1 WMFHUUKYIUOHRA-UHFFFAOYSA-N 0.000 description 1
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- 229940106006 1-eicosene Drugs 0.000 description 1
- FIKTURVKRGQNQD-UHFFFAOYSA-N 1-eicosene Natural products CCCCCCCCCCCCCCCCCC=CC(O)=O FIKTURVKRGQNQD-UHFFFAOYSA-N 0.000 description 1
- TWJNQYPJQDRXPH-UHFFFAOYSA-N 2-cyanobenzohydrazide Chemical compound NNC(=O)C1=CC=CC=C1C#N TWJNQYPJQDRXPH-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- 235000021357 Behenic acid Nutrition 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical class [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000005632 Capric acid (CAS 334-48-5) Substances 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical class C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000021353 Lignoceric acid Nutrition 0.000 description 1
- CQXMAMUUWHYSIY-UHFFFAOYSA-N Lignoceric acid Natural products CCCCCCCCCCCCCCCCCCCCCCCC(=O)OCCC1=CC=C(O)C=C1 CQXMAMUUWHYSIY-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical class [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical class [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 235000021360 Myristic acid Nutrition 0.000 description 1
- TUNFSRHWOTWDNC-UHFFFAOYSA-N Myristic acid Natural products CCCCCCCCCCCCCC(O)=O TUNFSRHWOTWDNC-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 235000021319 Palmitoleic acid Nutrition 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical class [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 235000021322 Vaccenic acid Nutrition 0.000 description 1
- UWHZIFQPPBDJPM-FPLPWBNLSA-M Vaccenic acid Natural products CCCCCC\C=C/CCCCCCCCCC([O-])=O UWHZIFQPPBDJPM-FPLPWBNLSA-M 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- OBETXYAYXDNJHR-UHFFFAOYSA-N alpha-ethylcaproic acid Natural products CCCCC(CC)C(O)=O OBETXYAYXDNJHR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical class [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- -1 amine salts Chemical class 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical class [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 229940116226 behenic acid Drugs 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- OOVILSPCZKYHEM-UTLKBRERSA-N butanamide (2S)-2-(dodecanoylamino)pentanedioic acid Chemical compound CCCC(N)=O.CCCC(N)=O.CCCCCCCCCCCC(=O)N[C@@H](CCC(O)=O)C(O)=O OOVILSPCZKYHEM-UTLKBRERSA-N 0.000 description 1
- 239000011575 calcium Chemical class 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- SECPZKHBENQXJG-UHFFFAOYSA-N cis-palmitoleic acid Natural products CCCCCCC=CCCCCCCCC(O)=O SECPZKHBENQXJG-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000008162 cooking oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- WMKGGPCROCCUDY-PHEQNACWSA-N dibenzylideneacetone Chemical compound C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1 WMKGGPCROCCUDY-PHEQNACWSA-N 0.000 description 1
- HFCSXCKLARAMIQ-UHFFFAOYSA-L disodium;sulfate;hydrate Chemical compound O.[Na+].[Na+].[O-]S([O-])(=O)=O HFCSXCKLARAMIQ-UHFFFAOYSA-L 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 1
- FARYTWBWLZAXNK-WAYWQWQTSA-N ethyl (z)-3-(methylamino)but-2-enoate Chemical compound CCOC(=O)\C=C(\C)NC FARYTWBWLZAXNK-WAYWQWQTSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000011777 magnesium Chemical class 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 150000004667 medium chain fatty acids Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 235000021313 oleic acid Nutrition 0.000 description 1
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000011591 potassium Chemical class 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- WBHHMMIMDMUBKC-XLNAKTSKSA-N ricinelaidic acid Chemical compound CCCCCC[C@@H](O)C\C=C\CCCCCCCC(O)=O WBHHMMIMDMUBKC-XLNAKTSKSA-N 0.000 description 1
- 229960003656 ricinoleic acid Drugs 0.000 description 1
- FEUQNCSVHBHROZ-UHFFFAOYSA-N ricinoleic acid Natural products CCCCCCC(O[Si](C)(C)C)CC=CCCCCCCCC(=O)OC FEUQNCSVHBHROZ-UHFFFAOYSA-N 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000011734 sodium Chemical class 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- RSIJVJUOQBWMIM-UHFFFAOYSA-L sodium sulfate decahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.[Na+].[Na+].[O-]S([O-])(=O)=O RSIJVJUOQBWMIM-UHFFFAOYSA-L 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- TUNFSRHWOTWDNC-HKGQFRNVSA-N tetradecanoic acid Chemical compound CCCCCCCCCCCCC[14C](O)=O TUNFSRHWOTWDNC-HKGQFRNVSA-N 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- UWHZIFQPPBDJPM-BQYQJAHWSA-N trans-vaccenic acid Chemical compound CCCCCC\C=C\CCCCCCCCCC(O)=O UWHZIFQPPBDJPM-BQYQJAHWSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は、潜熱蓄熱材を含む蓄熱材組成物、その製造方法、及び、多孔質基材と前記蓄熱材組成物とを備える蓄熱体に関する。 The present invention relates to a heat storage material composition containing a latent heat storage material, a method for producing the same, and a heat storage body including a porous substrate and the heat storage material composition.
最近の住宅では、スマートハウスに代表されるように、「省エネ」、「創エネ」、「蓄エネ」をキーワードとして、快適で二酸化炭素を排出させない住宅造りを目指している。一方で、パッシブハウスという考え方があり、高性能な断熱性能を備えることで、高い省エネルギー性と快適性を実現した住宅造りが注目されている。いずれの住宅においても、住宅の断熱性能と熱環境に対する性能の向上が必要不可欠とされている。そういった背景から、住宅の床、壁で蓄熱し、省エネで快適な住空間を提供できる蓄熱性を有した建材の研究・開発が盛んとなってきている。 In recent homes, as represented by smart houses, we are aiming to build comfortable homes that do not emit carbon dioxide, with the keywords "energy saving," "energy creation," and "energy storage." On the other hand, there is an idea of a passive house, and attention is being paid to housing construction that realizes high energy saving and comfort by providing high-performance heat insulation performance. In any house, it is indispensable to improve the heat insulation performance of the house and the performance against the thermal environment. Against this background, research and development of building materials with heat storage that can store heat on the floors and walls of houses and provide energy-saving and comfortable living spaces are becoming active.
たとえば、太陽光等の自然エネルギー、冷暖房装置等により発生する熱エネルギー、または、生活において発生する熱エネルギー等を、ノルマルパラフィン等の潜熱蓄熱材に蓄熱し、外気温の変動に対して吸熱・放熱を行うことで室内の温度変化を極力少なくしようという提案や試みがなされてきた。 For example, natural energy such as sunlight, heat energy generated by heating and cooling equipment, or heat energy generated in daily life is stored in a latent heat storage material such as normal paraffin, and heat is absorbed and dissipated in response to fluctuations in the outside temperature. Proposals and attempts have been made to minimize the temperature change in the room by doing this.
本出願人は、特許文献1において、潜熱蓄熱材を含む蓄熱材組成物を、多孔質基材に含浸した蓄熱体を開示している。潜熱蓄熱材は固相−液相間の相転移に要する潜熱を利用するため、液化した潜熱蓄熱材の流出が課題となるが、特許文献1ではこの課題を解決するために、潜熱蓄熱材に水素添加スチレン系熱可塑性エラストマーを所定量配合した蓄熱材組成物を、多孔質基材に含浸することを開示している。 The present applicant discloses in Patent Document 1 a heat storage body in which a porous substrate is impregnated with a heat storage material composition containing a latent heat storage material. Since the latent heat storage material utilizes the latent heat required for the phase transition between the solid phase and the liquid phase, the outflow of the liquefied latent heat storage material becomes a problem. It is disclosed that a porous substrate is impregnated with a heat storage material composition containing a predetermined amount of a hydrogenated styrene-based thermoplastic elastomer.
一方特許文献2は、凝固と融解の相転移を繰り返すヒートサイクル下においても、潜熱蓄熱材であるn−パラフィンの担持材料からの滲み出しや相分離がなく、潜熱蓄熱材料を高濃度で担持材料に混合しても安定なゲル状体を維持できる潜熱蓄熱材組成物として、潜熱により蓄熱可能な炭素数12以上50以下のn−パラフィンからなる潜熱蓄熱材料(A)を30質量%以上93.5質量%以下、前記潜熱蓄熱材料(A)を担持する担持材料(B)であるスチレン−エチレン/プロピレンブロック共重合体を6質量%以上70質量%以下、炭素数が12以上24以下の飽和もしくは不飽和カルボン酸、ヒドロキシカルボン酸、またはこれらの金属塩から選択される少なくとも1種のゲル化剤(C)を0.5質量%以上5質量%以下の割合で含んでなることを特徴とする潜熱蓄熱材組成物を開示している。 On the other hand, Patent Document 2 states that even under a heat cycle in which solidification and melting phase transitions are repeated, there is no exudation or phase separation from the material supporting the latent heat storage material n-paraffin, and the material supporting the latent heat storage material at a high concentration. As a latent heat storage material composition capable of maintaining a stable gel-like body even when mixed with, a latent heat storage material (A) made of n-paraffin having 12 or more and 50 or less carbon atoms that can store heat by latent heat is 30% by mass or more 93. Saturation of the styrene-ethylene / propylene block copolymer, which is 5% by mass or less and is the supporting material (B) that supports the latent heat storage material (A), is 6% by mass or more and 70% by mass or less, and has 12 or more and 24 or less carbon atoms. Alternatively, it is characterized by containing at least one gelling agent (C) selected from unsaturated carboxylic acid, hydroxycarboxylic acid, or a metal salt thereof in a proportion of 0.5% by mass or more and 5% by mass or less. The latent heat storage material composition is disclosed.
特許文献1に記載の、潜熱蓄熱材に水素添加スチレン系熱可塑性エラストマーを所定量配合した蓄熱材組成物の多孔質基材への含浸は、蓄熱材組成物をおおよそ80℃〜100℃の温度にて溶融し、多孔質基材を溶融物に浸漬することにより行う。本発明者らは、特許文献1に記載の潜熱蓄熱材は、80℃〜100℃の温度範囲において、溶融物の粘度の温度依存性が大きいため、溶融物の多孔質基材への含浸量を安定させることが難しいという新たな課題を見出した。 The impregnation of the heat storage material composition, which is described in Patent Document 1 in which a predetermined amount of a hydrogenated styrene-based thermoplastic elastomer is blended with the latent heat storage material, impregnates the porous substrate with the heat storage material composition at a temperature of about 80 ° C to 100 ° C. This is done by immersing the porous substrate in the melt. Since the latent heat storage material described in Patent Document 1 has a large temperature dependence of the viscosity of the melt in the temperature range of 80 ° C to 100 ° C, the present inventors have impregnated the porous substrate with the melt. I found a new problem that it is difficult to stabilize.
本発明者らはまた、特許文献2に記載されているスチレン−エチレン/プロピレンブロック共重合体を潜熱蓄熱材と組み合わせた蓄熱材組成物は、加熱溶融時のパネル基材への含浸性を確保するために潜熱蓄熱材とエラストマーの混合物の粘度調整を行った場合、5〜60℃の範囲での加温と冷却のヒートサイクル(寒熱処理)下において、潜熱蓄熱材が分離し易いとう新たな課題を見出した。 The present inventors also ensure that the heat storage material composition in which the styrene-ethylene / propylene block copolymer described in Patent Document 2 is combined with the latent heat storage material ensures the impregnation property into the panel substrate during heat melting. When the viscosity of the mixture of latent heat storage material and elastomer is adjusted, the latent heat storage material can be easily separated under the heat cycle (cold heat treatment) of heating and cooling in the range of 5 to 60 ° C. I found a problem.
本発明者らは、80℃以上の温度域における溶融粘度が十分に小さく、溶融粘度の温度依存性も小さく、且つ、60℃以下の温度域での寒熱処理に対して安定性が高い蓄熱材組成物を提供することを目的として鋭意検討した結果、以下の発明を完成するに至った。 The present inventors have a heat storage material having a sufficiently small melt viscosity in a temperature range of 80 ° C. or higher, a small temperature dependence of the melt viscosity, and high stability against cold heat treatment in a temperature range of 60 ° C. or lower. As a result of diligent studies for the purpose of providing the composition, the following inventions have been completed.
本発明は第一に、
潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを含み、
前記エラストマーが、ソフトセグメントと、前記ソフトセグメントの両端に結合したハードセグメントとを少なくとも含む、トリブロック以上のブロック共重合体を含み、
前記油ゲル化剤が、炭素数が12以上24以下の飽和又は不飽和カルボン酸、炭素数が12以上24以下の飽和又は不飽和カルボン酸の金属塩、炭素数が12以上24以下のヒドロキシカルボン酸、炭素数が12以上24以下のヒドロキシカルボン酸の金属塩、ジベンジリデンソルビトール、及び、アミノ酸系油ゲル化剤からなる群から選択される1種以上を含み、
80℃での溶融粘度が200mPa・s以下であり、
前記潜熱蓄熱材100質量部に対しX質量部の前記エラストマーを含み、ここでX質量部とは、100質量部の前記潜熱蓄熱材とX質量部の前記エラストマーとからなる混合物の60℃での溶融粘度が3500mPa・s以上となる量である、
ことを特徴とする蓄熱材組成物に関する。
First of all, the present invention
It contains a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent.
The elastomer comprises a block copolymer of triblock or higher, comprising at least a soft segment and hard segments bonded to both ends of the soft segment.
The oil gelling agent is a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, a metal salt of a saturated or unsaturated carboxylic acid having 12 or more and 24 carbon atoms or less, and a hydroxycarboxylic acid having 12 or more and 24 carbon atoms or less. It contains one or more selected from the group consisting of an acid, a metal salt of a hydroxycarboxylic acid having 12 or more and 24 or less carbon atoms, dibenzylidene sorbitol, and an amino acid-based oil gelling agent.
The melt viscosity at 80 ° C. is 200 mPa · s or less,
An X mass portion of the elastomer is contained with respect to 100 parts by mass of the latent heat storage material, and the X mass portion is the mixture of 100 parts by mass of the latent heat storage material and the X mass portion of the elastomer at 60 ° C. The amount is such that the melt viscosity is 3500 mPa · s or more.
The present invention relates to a heat storage material composition.
本発明の蓄熱材組成物は、80℃以上で加温した際の溶融粘度が十分小さく、また、その温度依存性が小さいため、蓄熱材組成物の溶融物を多孔質基材に含浸する際の含浸量が安定し、ばらつきが少ない。また、本発明の蓄熱材組成物は、60℃での溶融粘度が3500mPa・s以上と高く、且つ、トリブロック以上の熱可塑性エラストマーを含むことにより、60℃以下の温度域での寒熱処理に対する安定性が高い。 The heat storage material composition of the present invention has a sufficiently small melt viscosity when heated at 80 ° C. or higher, and its temperature dependence is small. Therefore, when the melt of the heat storage material composition is impregnated into the porous substrate. The impregnation amount is stable and there is little variation. Further, the heat storage material composition of the present invention has a high melt viscosity at 60 ° C. of 3500 mPa · s or more and contains a thermoplastic elastomer of triblock or more, so that it can be used for cold heat treatment in a temperature range of 60 ° C. or lower. High stability.
本発明の蓄熱材組成物は、好ましい態様において、100℃での溶融粘度が150mPa・s以下である。 In a preferred embodiment, the heat storage material composition of the present invention has a melt viscosity at 100 ° C. of 150 mPa · s or less.
この態様の本発明の蓄熱材組成物は、多孔質基材に飽和状態まで含浸することが容易であるため好ましい。 The heat storage material composition of the present invention of this aspect is preferable because it is easy to impregnate the porous substrate to a saturated state.
本発明の蓄熱材組成物の他の好ましい態様では、前記潜熱蓄熱材が、相変化温度が15℃以上35℃以下の範囲のパラフィンである。 In another preferred embodiment of the heat storage material composition of the present invention, the latent heat storage material is paraffin having a phase change temperature in the range of 15 ° C. or higher and 35 ° C. or lower.
この態様の本発明の蓄熱材組成物は、相変化温度が住環境の温度に対応するため、住宅用途に好適である。 The heat storage material composition of the present invention in this aspect is suitable for residential use because the phase change temperature corresponds to the temperature of the living environment.
本発明の蓄熱材組成物の他の好ましい態様では、前記エラストマーが、スチレン−エチレン/ブチレン−スチレンブロック共重合体(SEBS)を含む。 In another preferred embodiment of the heat storage composition of the present invention, the elastomer comprises a styrene-ethylene / butylene-styrene block copolymer (SEBS).
この態様の本発明の蓄熱材組成物は、60℃以下の温度域での寒熱処理に対する耐性が特に高いため好ましい。 The heat storage material composition of the present invention of this aspect is preferable because it has particularly high resistance to cold heat treatment in a temperature range of 60 ° C. or lower.
本発明の蓄熱材組成物の他の好ましい態様では、前記油ゲル化剤が、12−ヒドロキシステアリン酸又はその金属塩を含む。 In another preferred embodiment of the heat storage composition of the present invention, the oil gelling agent comprises 12-hydroxystearic acid or a metal salt thereof.
12−ヒドロキシステアリン酸又はその金属塩は、融点が75℃である。このため、この態様の本発明の蓄熱材組成物は、60℃において固化物となり易く、多孔質基材に安定に保持され得る。 12-Hydroxystearic acid or a metal salt thereof has a melting point of 75 ° C. Therefore, the heat storage material composition of the present invention of this aspect tends to be solidified at 60 ° C. and can be stably held on the porous substrate.
本発明は第二に、
上記の本発明の蓄熱材組成物の製造方法であって、
潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを、溶融混練する溶融混練工程と、
溶融混練工程において生成した混合物を冷却する冷却工程と
を含む方法に関する。
本発明の方法により、上記の有利な特性を有する蓄熱材組成物を製造することができる。
Secondly, the present invention
The above-mentioned method for producing a heat storage material composition of the present invention.
A melt-kneading step in which a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent are melt-kneaded.
The present invention relates to a method including a cooling step of cooling the mixture produced in the melt-kneading step.
According to the method of the present invention, a heat storage material composition having the above-mentioned advantageous properties can be produced.
本発明は第三に、
多孔質基材と、
前記多孔質基材に含浸された、前記蓄熱材組成物と
を少なくとも備える蓄熱体に関する。
本発明の蓄熱体は、60℃以下の温度域での蓄熱材組成物の多孔質基材からの染み出しが少ない。
The present invention is third,
Porous substrate and
The present invention relates to a heat storage body including at least the heat storage material composition impregnated in the porous substrate.
The heat storage body of the present invention has little exudation from the porous substrate of the heat storage material composition in the temperature range of 60 ° C. or lower.
本発明の蓄熱材組成物は、80℃以上で加温した際の溶融粘度が十分小さく、また、その温度依存性が小さいため、蓄熱材組成物の溶融物を多孔質基材に含浸する際の含浸量が安定し、ばらつきが少ない。また、本発明の蓄熱材組成物を構成する潜熱蓄熱材とエラストマーの混合物は、60℃での溶融粘度が3500mPa・s以上と高く、且つ、トリブロック以上の熱可塑性エラストマーを含むことにより、60℃以下の温度域での寒熱処理に対する安定性が高い。 The heat storage material composition of the present invention has a sufficiently small melt viscosity when heated at 80 ° C. or higher, and its temperature dependence is small. Therefore, when the melt of the heat storage material composition is impregnated into the porous substrate. The impregnation amount is stable and there is little variation. Further, the mixture of the latent heat storage material and the elastomer constituting the heat storage material composition of the present invention has a high melt viscosity at 60 ° C. of 3500 mPa · s or more and contains a thermoplastic elastomer of triblock or more. High stability against cold heat treatment in the temperature range below ° C.
本発明の蓄熱材組成物が多孔質基材に含浸された蓄熱体は、60℃以下の温度域での蓄熱材組成物の多孔質基材からの染み出しが少ないため好ましい。 The heat storage material in which the heat storage material composition of the present invention is impregnated in the porous base material is preferable because the heat storage material composition does not exude from the porous base material in a temperature range of 60 ° C. or lower.
<1.材料>
1.1.潜熱蓄熱材
本発明に用いることができる潜熱蓄熱材は、例えば、室内の暖房、日光による熱などで固相から液相に相変化する潜熱蓄熱材であり、相変化温度(融点)は、好ましくは5℃〜60℃の範囲にあり、より好ましくは15℃以上であり、より好ましくは18℃以上であり、より好ましくは35℃以下であり、より好ましくは28℃以下であり、より好ましくは15℃〜35℃の範囲にあり、より好ましくは18℃〜28℃の範囲にある。本明細書において相変化温度及び融点は1atmでの値を指す。相変化温度は相転移温度ともいう。
<1. Material>
1.1. Latent heat storage material The latent heat storage material that can be used in the present invention is, for example, a latent heat storage material that undergoes a phase change from a solid phase to a liquid phase due to indoor heating, heat from sunlight, etc., and the phase change temperature (melting point) is preferable. Is in the range of 5 ° C to 60 ° C, more preferably 15 ° C or higher, more preferably 18 ° C or higher, more preferably 35 ° C or lower, more preferably 28 ° C or lower, and even more preferably. It is in the range of 15 ° C to 35 ° C, more preferably in the range of 18 ° C to 28 ° C. In the present specification, the phase change temperature and the melting point refer to the values at 1 atm. The phase change temperature is also called the phase transition temperature.
例えば、夏季において、冷房により冷やされた空気、日陰の空気又は夜間の空気の冷温を貯蔵し、室温が高いときにその熱を吸収する目的では、前記冷温よりも高く、低下させるべき高い室温よりも低い相変化温度の潜熱蓄熱材を用いることが好ましい。このような相変化温度としては、22〜28℃が例示できる。また、冬季において、暖房により温められた空気、日向の空気又は昼間の空気の暖温を貯蔵し、温度が下がった時に放熱する目的では、前記暖温よりも低く、上昇させるべき低い室温よりも高い相変化温度の潜熱蓄熱材を用いることが好ましい。このような相変化温度としては、18〜26℃が例示できる。 For example, in the summer, for the purpose of storing the cold temperature of air cooled by air conditioning, shaded air, or nighttime air and absorbing the heat when the room temperature is high, it is higher than the cold temperature and higher than the high room temperature to be lowered. It is preferable to use a latent heat storage material having a low phase change temperature. Examples of such a phase change temperature include 22 to 28 ° C. Also, in winter, for the purpose of storing the warm temperature of the air warmed by heating, the sun's air, or the daytime air and dissipating it when the temperature drops, it is lower than the warm temperature and lower than the low room temperature that should be raised. It is preferable to use a latent heat storage material having a high phase change temperature. Examples of such a phase change temperature include 18 to 26 ° C.
潜熱蓄熱材としては、n−ヘキサデカン、n−ヘプタデカン、n−オクタデカン、及びn−ノナデカンからなる群から選択される少なくとも1種(2種以上の混合物であってもよい)等で構成される又は前記少なくとも1種を含む、典型的には炭素数16〜24の範囲内の炭素数を有する、n−パラフィンやパラフィンワックス等の飽和脂肪族炭化水素(好ましくは直鎖飽和脂肪族炭化水素);1−ヘキサデセン、1−ヘプタデセン、1−オクタデセン、1−ノナデセン、及び1−エイコセン等からなる群から選択される少なくとも1種(2種以上の混合物であってもよい)等で構成される又は前記少なくとも1種を含む、典型的には炭素数16〜26の範囲内(好ましくは24以下)の炭素数を有する、α−オレフィン(好ましくは直鎖α−オレフィン)等の一価又は多価不飽和脂肪族炭化水素(好ましくは直鎖状の一価又は多価不飽和脂肪族炭化水素);オクタン酸、カプリン酸、ラウリン酸、及びミリスチン酸からなる群から選択される少なくとも1種(2種以上の混合物であってもよい)等で構成される又は前記少なくとも1種を含む、典型的には炭素数6〜24、好ましくは炭素数8〜14の範囲内の炭素数を有する、中鎖又は長鎖脂肪酸;上記脂肪酸のエステル;ポリエチレングリコール(例えば分子量500〜1000)等のポリエーテル化合物;硫酸ナトリウム水和物、塩化カルシウム水和物、硫酸ナトリウム10水和物等の無機塩等を挙げることができる。好ましくは、潜熱蓄熱材は、前記飽和脂肪族炭化水素、前記一価又は多価不飽和脂肪族炭化水素、前記中鎖又は長鎖脂肪酸、前記脂肪酸のエステル及び前記ポリエーテル化合物からなる群から選択される1種又は2種以上の混合物であり、より好ましくは前記飽和脂肪族炭化水素及び前記一価又は多価不飽和脂肪族炭化水素からなる群から選択される1種又は2種以上の混合物であり、より好ましくは前記飽和脂肪族炭化水素及び前記α−オレフィンからなる群から選択される1種又は2種以上の混合物である。例えば、28℃で融解するものであれば、n−オクタデカンを選択し、18℃で融解するものであれば、n−ヘキサデカンを選択することができる。さらに、上述した相変化温度の異なる複数の潜熱蓄熱材を混合して用いてもよい。また、潜熱蓄熱材として前記α−オレフィンを用いる場合、炭素数の異なる複数の前記α−オレフィンの混合物を用いることができる。 The latent heat storage material is composed of at least one selected from the group consisting of n-hexadecane, n-heptadecane, n-octadecan, and n-nonadecan (may be a mixture of two or more) or the like. Saturated aliphatic hydrocarbons such as n-paraffin and paraffin wax (preferably linear saturated aliphatic hydrocarbons) containing at least one of the above and typically having carbon atoms in the range of 16 to 24 carbon atoms; It is composed of at least one selected from the group consisting of 1-hexadecene, 1-heptadecene, 1-octadecene, 1-nonadecene, 1-eicosene and the like (may be a mixture of two or more) or the above. Monovalent or polyvalent non-valent, such as α-olefins (preferably linear α-olefins), including at least one, typically having a carbon number in the range of 16 to 26 (preferably 24 or less). Saturated aliphatic hydrocarbons (preferably linear monovalent or polyunsaturated aliphatic hydrocarbons); at least one selected from the group consisting of octanoic acid, capric acid, lauric acid, and myristic acid (two). A medium chain composed of (may be a mixture of the above) or the like, or containing at least one of the above, typically having a carbon number in the range of 6 to 24 carbon atoms, preferably 8 to 14 carbon atoms. Or long-chain fatty acids; esters of the above fatty acids; polyether compounds such as polyethylene glycol (for example, molecular weight 500 to 1000); inorganic salts such as sodium sulfate hydrate, calcium chloride hydrate, sodium sulfate decahydrate and the like. be able to. Preferably, the latent heat storage material is selected from the group consisting of the saturated aliphatic hydrocarbon, the monovalent or polyunsaturated aliphatic hydrocarbon, the medium-chain or long-chain fatty acid, the ester of the fatty acid, and the polyether compound. One or more mixtures, more preferably one or more mixtures selected from the group consisting of the saturated aliphatic hydrocarbons and the monovalent or polyunsaturated aliphatic hydrocarbons. It is more preferably one or a mixture of two or more selected from the group consisting of the saturated aliphatic hydrocarbon and the α-olefin. For example, n-octadecane can be selected if it melts at 28 ° C., and n-hexadecane can be selected if it melts at 18 ° C. Further, a plurality of latent heat storage materials having different phase change temperatures may be mixed and used. When the α-olefin is used as the latent heat storage material, a mixture of a plurality of the α-olefins having different carbon atoms can be used.
1.2.水素添加スチレン系熱可塑性エラストマー
本発明で用いる水素添加スチレン系熱可塑性エラストマーは、ソフトセグメントと、前記ソフトセグメントの両端に結合したハードセグメントとを少なくとも含む、トリブロック以上のブロック共重合体を含むことを特徴とする。ソフトセグメントは潜熱蓄熱材と親和性が高いため、上記構造の水素添加スチレン系熱可塑性エラストマーと潜熱蓄熱材とを含む蓄熱材組成物では、前記エラストマーのソフトセグメントが潜熱蓄熱材と親和性により一体化する。一方、ソフトセグメントの両端のハードセグメントは、それぞれ、温度低下時に他の分子のハードセグメントと疑似架橋を形成して、3次元網目構造を形成する。このため、スチレン−エチレン/プロピレンブロック共重合体(SEP)等のジブロック構造の水素添加スチレン系熱可塑性エラストマーを用いる場合とは異なり、上記のトリブロック構造の水素添加スチレン系熱可塑性エラストマーと潜熱蓄熱材とを含む蓄熱材組成物は温度低下に伴い溶融物の粘度が顕著に増加する。このため本発明の蓄熱材組成物では、5〜60℃の範囲で加温と冷却を繰り返す寒熱処理に対して潜熱蓄熱材の分離が抑えられる特徴を有する。特許文献2に記載されている、スチレン−エチレン/プロピレンブロック共重合体は、1つのハードセグメントと1つのソフトセグメントとが隣接したジブロック構造の共重合体であるため、トリブロック以上のブロック共重合体による上記の効果を有していないことが実験3において確認されている。
1.2. Hydrogenated Styrene-based Thermoplastic Elastomer The hydrogenated styrene-based thermoplastic elastomer used in the present invention includes a block copolymer of triblock or higher containing at least a soft segment and a hard segment bonded to both ends of the soft segment. It is characterized by. Since the soft segment has a high affinity with the latent heat storage material, in the heat storage material composition containing the hydrogenated styrene-based thermoplastic elastomer having the above structure and the latent heat storage material, the soft segment of the elastomer is integrated with the latent heat storage material due to its affinity. To become. On the other hand, the hard segments at both ends of the soft segment form pseudo-crosslinks with the hard segments of other molecules when the temperature drops, forming a three-dimensional network structure. Therefore, unlike the case of using a diblock-structured hydrogenated styrene-based thermoplastic elastomer such as styrene-ethylene / propylene block copolymer (SEP), the above-mentioned triblock-structured hydrogenated styrene-based thermoplastic elastomer and latent heat are used. In the heat storage material composition containing the heat storage material, the viscosity of the melt increases remarkably as the temperature decreases. Therefore, the heat storage material composition of the present invention has a feature that the separation of the latent heat storage material is suppressed in the cold heat treatment in which heating and cooling are repeated in the range of 5 to 60 ° C. The styrene-ethylene / propylene block copolymer described in Patent Document 2 is a copolymer having a diblock structure in which one hard segment and one soft segment are adjacent to each other. It has been confirmed in Experiment 3 that the polymer does not have the above-mentioned effect.
上記の水素添加スチレン系熱可塑性エラストマーとしては、スチレン−エチレン/ブチレン−スチレンブロック共重合体(SEBS)、スチレン−エチレン/プロピレン−スチレンブロック共重合体(SEPS)、及びスチレン−エチレン−エチレン/プロピレン−スチレンブロック共重合体(SEEPS)からなる群から選択される少なくとも1種(2種以上の混合物であってもよい)の共重合体を含むものが例示できる。前記共重合体としては、SEBS及びSEEPSからなる群から選択される少なくとも1種が好ましい。SEBSはポリスチレン−ポリ(エチレン/ブチレン)−ポリスチレンブロック共重合体と、SEPSはポリスチレン−ポリ(エチレン/プロピレン)−ポリスチレンブロック共重合体と、SEEPSはポリスチレン−ポリ(エチレン−エチレン/プロピレン)−ポリスチレンブロック共重合体と、それぞれ表記することもできる。水素添加スチレン系熱可塑性エラストマーにおけるスチレン含量の範囲は特に限定されないが分子全体に対してスチレン含量が25〜35質量%の範囲であることが好ましい。 Examples of the hydrogenated styrene-based thermoplastic elastomer include styrene-ethylene / butylene-styrene block copolymer (SEBS), styrene-ethylene / propylene-styrene block copolymer (SEPS), and styrene-ethylene-ethylene / propylene. Examples thereof include those containing at least one polymer (which may be a mixture of two or more) selected from the group consisting of -styrene block copolymers (SEEPS). As the copolymer, at least one selected from the group consisting of SEBS and SEEPS is preferable. SEBS is a polystyrene-poly (ethylene / butylene) -polystyrene block copolymer, SEPS is a polystyrene-poly (ethylene / propylene) -polystyrene block copolymer, and SEEPS is a polystyrene-poly (ethylene-ethylene / propylene) -polystyrene. It can also be referred to as a block copolymer. The range of the styrene content in the hydrogenated styrene-based thermoplastic elastomer is not particularly limited, but the styrene content is preferably in the range of 25 to 35% by mass with respect to the entire molecule.
水素添加スチレン系熱可塑性エラストマーを構成する前記共重合体の重量平均分子量は好ましくは6万以上、より好ましくは7.5万以上、更に好ましくは8.5万以上、最も好ましくは9万以上である。また水素添加スチレン系熱可塑性エラストマーの重量平均分子量は好ましくは25万以下、より好ましくは20万以下、最も好ましくは15万以下である。前記共重合体の重量平均分子量がこの範囲のとき、蓄熱材組成物の多孔質基材からの流出が抑制できるとともに蓄熱材組成物の溶融時の粘度が十分に低く多孔質基材への含浸が容易となる効果が特に高い。 The weight average molecular weight of the copolymer constituting the hydrogenated styrene-based thermoplastic elastomer is preferably 60,000 or more, more preferably 75,000 or more, still more preferably 85,000 or more, and most preferably 90,000 or more. be. The weight average molecular weight of the hydrogenated styrene-based thermoplastic elastomer is preferably 250,000 or less, more preferably 200,000 or less, and most preferably 150,000 or less. When the weight average molecular weight of the copolymer is in this range, the outflow of the heat storage material composition from the porous substrate can be suppressed, and the viscosity of the heat storage material composition at the time of melting is sufficiently low to impregnate the porous substrate. The effect of facilitating is particularly high.
本発明において重量平均分子量は、ゲル・パーミエーション・クロマトグラフィー(GPC)による測定に基づき、標準ポリスチレン換算値として求められたものである。GPC測定時の溶離液はテトラヒドロフランを用いることができる。GPCのためのカラムとしては、東ソー株式会社製TSKgel GMHXL、TSKgel G4000HXL、及びTSKgel G5000HXLを直列に連結したカラムを用いることができる。GPC測定機器としては、東ソー株式会社製ゲルパーミエーションクロマトグラフ(HLC−8020)を用いることができる。 In the present invention, the weight average molecular weight is determined as a standard polystyrene equivalent value based on the measurement by gel permeation chromatography (GPC). Tetrahydrofuran can be used as the eluent for GPC measurement. As the column for GPC, a column in which TSKgel GMHXL, TSKgel G4000HXL, and TSKgel G5000HXL manufactured by Tosoh Corporation are connected in series can be used. As the GPC measuring device, a gel permeation chromatograph (HLC-8020) manufactured by Tosoh Corporation can be used.
1.3.油ゲル化剤
本発明で用いる油ゲル化剤は、炭素数が12以上24以下の飽和又は不飽和カルボン酸、炭素数が12以上24以下の飽和又は不飽和カルボン酸の金属塩、炭素数が12以上24以下のヒドロキシカルボン酸、炭素数が12以上24以下のヒドロキシカルボン酸の金属塩、ジベンジリデンソルビトール、及び、アミノ酸系油ゲル化剤からなる群から選択される1種以上を含み、好ましくは、炭素数が12以上24以下の飽和又は不飽和カルボン酸、炭素数が12以上24以下の飽和又は不飽和カルボン酸の金属塩、炭素数が12以上24以下のヒドロキシカルボン酸、及び、炭素数が12以上24以下のヒドロキシカルボン酸の金属塩からなる群から選択される1種以上を含む。
1.3. Oil Gelling Agent The oil gelling agent used in the present invention is a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, a metal salt of a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, and a carbon number of carbon atoms. It contains one or more selected from the group consisting of a hydroxycarboxylic acid of 12 or more and 24 or less, a metal salt of a hydroxycarboxylic acid having 12 or more and 24 or less carbon atoms, dibenzylidene sorbitol, and an amino acid-based oil gelling agent, preferably one or more. Is a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, a metal salt of a saturated or unsaturated carboxylic acid having 12 or more and 24 carbon atoms or less, a hydroxycarboxylic acid having 12 or more and 24 carbon atoms or less, and carbon. Includes one or more selected from the group consisting of metal salts of hydroxycarboxylic acids having a number of 12 or more and 24 or less.
前記エラストマー及び潜熱蓄熱材のみを含む蓄熱材組成物は、80℃で加温した際の溶融粘度が高く、且つ、80℃以上の温度域での溶融粘度の温度依存性が大きいという課題があった。本発明者らは、前記油ゲル化剤を更に配合した蓄熱材組成物は、80℃以上の温度域において溶融粘度が十分に低く、且つ、溶融粘度の温度依存性が小さいという予想外の現象を見出し、本発明を完成するに至った。
油ゲル化剤は、加温した調理用油に添加し冷却したときにゲル状に固化する性質を有する。
The heat storage material composition containing only the elastomer and the latent heat storage material has a problem that the melt viscosity when heated at 80 ° C. is high and the temperature dependence of the melt viscosity in the temperature range of 80 ° C. or higher is large. rice field. The present inventors have an unexpected phenomenon that the heat storage material composition further blended with the oil gelling agent has a sufficiently low melt viscosity in a temperature range of 80 ° C. or higher and a small temperature dependence of the melt viscosity. The present invention was completed.
The oil gelling agent has the property of solidifying into a gel when added to warm cooking oil and cooled.
炭素数が12以上24以下の飽和又は不飽和カルボン酸、或いは、炭素数が12以上24以下のヒドロキシカルボン酸としては、炭素数が12以上24以下であれば、飽和、不飽和、直鎖状、分岐状のいずれであってもよい。たとえば、ラウリン酸、ミリスチン酸、ペンタデシル酸、パルミチン酸、パルミトレイン酸、マルガリン酸、ステアリン酸、オレイン酸、バクセン酸、リノール酸、アラキジン酸、アラキドン酸、ベヘン酸、リグノセリン酸、12−ヒドロキシステアリン酸、リシノール酸等が例示される。また、これらの金属塩としては、リチウム、カリウム、ナトリウム、マグネシウム、カルシウム、バリウム、アルミニウム等の塩が例示される。 As a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, or a hydroxycarboxylic acid having 12 or more and 24 or less carbon atoms, if the number of carbon atoms is 12 or more and 24 or less, it is saturated, unsaturated or linear. , It may be branched. For example, lauric acid, myristic acid, pentadecylic acid, palmitic acid, palmitoleic acid, margaric acid, stearic acid, oleic acid, vaccenic acid, rinoleic acid, arachidic acid, arachidic acid, behenic acid, lignoceric acid, 12-hydroxystearic acid, Examples thereof include ricinoleic acid. Examples of these metal salts include salts of lithium, potassium, sodium, magnesium, calcium, barium, aluminum and the like.
ジベンジリデンソルビトールとしては、D−ソルビトールとベンズアルデヒドとの1:2脱水縮合物が好ましい。 The dibenzylideneacetone sorbitol is preferably a 1: 2 dehydration condensate of D-sorbitol and benzaldehyde.
アミノ酸系油ゲル化剤としては、N−アシルアミノ酸のアミド、エステル、アミン塩等の誘導体が好ましい。アミノ酸系油ゲル化剤の具体例としては、N−ラウロイルグルタミン酸ジ−n−ブチルアミドが例示できる。 As the amino acid-based oil gelling agent, derivatives such as amides, esters, and amine salts of N-acylamino acids are preferable. Specific examples of the amino acid-based oil gelling agent include N-lauroyl glutamic acid di-n-butyramide.
油ゲル化剤の融点は、潜熱蓄熱材料の相変化温度以上の温度、好ましくは、潜熱蓄熱材料の相変化温度より10℃以上高い温度、より好ましくは20℃以上高い温度であることが好ましい。
油ゲル化剤としては特に、12−ヒドロキシステアリン酸又はその金属塩が好ましい。
The melting point of the oil gelling agent is preferably a temperature equal to or higher than the phase change temperature of the latent heat storage material, preferably a temperature 10 ° C. or higher, more preferably 20 ° C. or higher higher than the phase change temperature of the latent heat storage material.
As the oil gelling agent, 12-hydroxystearic acid or a metal salt thereof is particularly preferable.
1.4.多孔質基材
本発明に使用できる多孔質基材は、蓄熱材組成物を含浸し保持することができる微細な空隙を有する基材である。具体的には、潜熱蓄熱材を含浸し保持することができる微細な空隙を有する材料を含む多孔質基材であればよく、その材料は限定されない。
1.4. Porous base material The porous base material that can be used in the present invention is a base material having fine voids that can be impregnated and held with the heat storage material composition. Specifically, it may be a porous base material containing a material having fine voids capable of impregnating and holding a latent heat storage material, and the material is not limited.
多孔質基材の具体的な材料としては、例えば、パーティクルボード、木質繊維板(MDF、インシュレーションボード、ハードボード等)等の木質系ボードを挙げることができる。この他にも、石膏ボード、ケイ酸カルシウム板等の無機質ボード;鉱物質がボード状に成形された鉱物質ボード;グラスウール、カーボンファイバー、金属繊維などの無機繊維を集積したボードなどを挙げることができる。 Specific examples of the material of the porous base material include wood-based boards such as particle boards and wood fiber boards (MDF, insulation boards, hard boards, etc.). In addition to this, inorganic boards such as gypsum boards and calcium silicate boards; mineral boards in which mineral substances are molded into a board shape; boards in which inorganic fibers such as glass wool, carbon fiber, and metal fibers are integrated can be mentioned. can.
多孔質基材の全体の形状は特に限定されず、板状、柱状、ブロック状等の各種形状であってよい。また各種形状の多孔質基材は、曲げ加工が施されたものであってもよい。ここで曲げ加工は蓄熱材組成物を含浸する工程の前に行われてもよいし、該工程の後に行われてもよい。多孔質基材が板状である場合、その厚さは特に限定されないが、通常は3〜30mmであり、好ましくは5〜20mmである。多孔質基材の全体に蓄熱材組成物が含浸されることが好ましいが、これには限定されず、多孔質基材のうち表層部分の一部のみに蓄熱材組成物が含浸されてもよい。 The overall shape of the porous substrate is not particularly limited, and may be various shapes such as a plate shape, a columnar shape, and a block shape. Further, the porous substrate having various shapes may be bent. Here, the bending process may be performed before the step of impregnating the heat storage material composition, or may be performed after the step. When the porous substrate is plate-shaped, its thickness is not particularly limited, but is usually 3 to 30 mm, preferably 5 to 20 mm. It is preferable that the entire porous substrate is impregnated with the heat storage material composition, but the present invention is not limited to this, and only a part of the surface layer portion of the porous substrate may be impregnated with the heat storage material composition. ..
多孔質基材の密度が小さい値であるほど、前記多孔質基材に蓄熱材組成物が含浸され易い。多孔質基材としては、少なくとも蓄熱材組成物が含浸される部分の密度(含浸処理前の密度)が好ましくは0.1g/cm3以上、より好ましくは0.2g/cm3以上であり、好ましくは0.9g/cm3未満である。多孔質基材の密度は、一般的に含浸率を高めるためには低密度であることが好ましく、例えば、0.8g/cm3未満、0.7g/cm3以下、0.6g/cm3以下、又は0.5g/cm3以下の密度であることが好ましい。 The smaller the density of the porous substrate, the easier it is for the porous substrate to be impregnated with the heat storage material composition. As the porous substrate, the density of the portion impregnated with the heat storage material composition (density before impregnation treatment) is preferably 0.1 g / cm 3 or more, more preferably 0.2 g / cm 3 or more. It is preferably less than 0.9 g / cm 3. The density of the porous substrate is generally preferably low in order to increase the impregnation rate, for example, less than 0.8 g / cm 3 , 0.7 g / cm 3 or less, 0.6 g / cm 3. The density is preferably 0.5 g / cm 3 or less.
<2.蓄熱材組成物>
2.1.溶融粘度
本発明の蓄熱材組成物は、80℃での溶融粘度が200mPa・s以下であることを第一の特徴とする。
<2. Heat storage material composition>
2.1. Melt Viscosity The heat storage material composition of the present invention is characterized by having a melt viscosity at 80 ° C. of 200 mPa · s or less.
蓄熱材組成物を多孔質基材に含浸するとき、80℃以上の温度域で溶融し、溶融液に多孔質基材を浸漬することにより行うことが通常である。蓄熱材組成物の溶融粘度がこの範囲であるとき、多孔質基材へと含浸され易いため好ましい。また、潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを含み、且つ、80℃での溶融粘度が200mPa・s以下である蓄熱材組成物は、80℃以上の温度域で粘度の温度依存性が小さいため、多孔質基材の浸漬時の温度が多少変動しても、多孔質基材への含浸量のばらつきが少ないため好ましい。 When the porous base material is impregnated with the heat storage material composition, it is usually melted in a temperature range of 80 ° C. or higher and the porous base material is immersed in the molten liquid. When the melt viscosity of the heat storage material composition is in this range, it is preferable because it is easily impregnated into the porous substrate. Further, the heat storage material composition containing a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent and having a melt viscosity at 80 ° C. of 200 mPa · s or less has a temperature of 80 ° C. or higher. Since the temperature dependence of the viscosity is small in the region, even if the temperature at the time of immersion of the porous substrate fluctuates slightly, the amount of impregnation into the porous substrate does not vary, which is preferable.
本発明の蓄熱材組成物の80℃での溶融粘度は、より好ましくは、170mPa・s以下である。 The melt viscosity of the heat storage material composition of the present invention at 80 ° C. is more preferably 170 mPa · s or less.
本発明の蓄熱材組成物は、更に、100℃での溶融粘度が150mPa・s以下であることが好ましく、30mPa・s以下であることが特に好ましい。このような蓄熱材組成物は、100℃前後で溶融した時に、多孔質基材に速やかに含浸され得る。 Further, the heat storage material composition of the present invention preferably has a melt viscosity at 100 ° C. of 150 mPa · s or less, and particularly preferably 30 mPa · s or less. Such a heat storage material composition can be rapidly impregnated into the porous substrate when melted at around 100 ° C.
粘度の測定はJIS Z8803−2011及びJIS K7117−1に規定されている、ブルックフィールド型回転粘度計(B型粘度計)を用いた方法により行うことができる。B型粘度計としては東機産業製ABS−100を用い、ローターサイズ:No.1、No.2、回転速度:6〜60rpmの条件で測定を行うことができる。 The viscosity can be measured by a method using a Brookfield type rotational viscometer (B type viscometer) specified in JIS Z8803-2011 and JIS K7117-1. As the B-type viscometer, ABS-100 manufactured by Toki Sangyo is used, and measurement can be performed under the conditions of rotor size: No. 1, No. 2, and rotation speed: 6 to 60 rpm.
2.2.熱可塑性エラストマーの量
本発明の蓄熱材組成物は、潜熱蓄熱材100質量部に対しX質量部の前記エラストマーを含み、ここでX質量部とは、100質量部の前記潜熱蓄熱材とX質量部の前記エラストマーとからなる混合物の60℃での溶融粘度が3500mPa・s以上となる量であることを更なる特徴とする。潜熱蓄熱材100質量部に対しX質量部の前記エラストマーを含み、且つ、更に油ゲル化剤を含む本発明の蓄熱材組成物は、60℃以下の温度域での寒熱処理に対する安定性が高いため好ましい。
2.2. Amount of Thermoplastic Elastomer The heat storage material composition of the present invention contains X mass parts of the elastomer with respect to 100 parts by mass of the latent heat storage material, where X mass parts means 100 parts by mass of the latent heat storage material and X mass. A further feature is that the melt viscosity of the mixture composed of the above-mentioned elastomer in the portion at 60 ° C. is 3500 mPa · s or more. The heat storage material composition of the present invention containing X parts by mass of the elastomer with respect to 100 parts by mass of the latent heat storage material and further containing an oil gelling agent has high stability against cold heat treatment in a temperature range of 60 ° C. or lower. Therefore, it is preferable.
X質量部の具体例としては、特に限定されないが、典型的には25質量部以下、更に好ましくは20質量部以下、更に好ましくは17.5質量部以下であり、更に好ましくは12.5質量部以下であり、典型的には6質量部以上、より好ましくは7.5質量部以上である。水素添加スチレン系熱可塑性エラストマーの添加量が上記範囲のとき、蓄熱材組成物の多孔質基材からの流出が抑制できるとともに蓄熱材組成物の溶融時の粘度が十分に低く多孔質基材への含浸が容易となる効果が特に高い。 The specific example of the X part by mass is not particularly limited, but is typically 25 parts by mass or less, more preferably 20 parts by mass or less, still more preferably 17.5 parts by mass or less, still more preferably 12.5 parts by mass. It is 5 parts or less, typically 6 parts by mass or more, and more preferably 7.5 parts by mass or more. When the amount of the hydrogenated styrene-based thermoplastic elastomer added is within the above range, the outflow of the heat storage material composition from the porous substrate can be suppressed, and the viscosity of the heat storage material composition at the time of melting is sufficiently low to the porous substrate. The effect of facilitating impregnation is particularly high.
<3.蓄熱材組成物の製造方法>
本発明の蓄熱材組成物は、
潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを、溶融混練する溶融混練工程と、
溶融混練工程において生成した混合物を冷却する冷却工程と
を含む方法により製造することができる。
<3. Method for manufacturing heat storage material composition>
The heat storage material composition of the present invention is
A melt-kneading step in which a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent are melt-kneaded.
It can be produced by a method including a cooling step of cooling the mixture produced in the melt-kneading step.
溶融混練工程では、潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを、例えば80℃〜140℃、好ましくは100℃〜120℃の範囲で溶融混練することを含む。 The melt-kneading step includes melt-kneading the latent heat storage material, the hydrogenated styrene-based thermoplastic elastomer, and the oil gelling agent in the range of, for example, 80 ° C. to 140 ° C., preferably 100 ° C. to 120 ° C.
冷却工程では、溶融混練工程において生成した混合物を例えば60℃〜0℃、好ましくは40℃〜10℃の範囲で冷却することを含む。 The cooling step includes cooling the mixture produced in the melt-kneading step in the range of, for example, 60 ° C to 0 ° C, preferably 40 ° C to 10 ° C.
<4.蓄熱体>
本発明の蓄熱体は、
多孔質基材と、
前記多孔質基材に含浸された、前記蓄熱材組成物と
を少なくとも備える。
<4. Heat storage body>
The heat storage body of the present invention is
Porous substrate and
It includes at least the heat storage material composition impregnated in the porous substrate.
多孔質基材への前記蓄熱材組成物の含浸方法としては、前記蓄熱材組成物を、80℃以上の温度域、好ましくは80〜110℃の温度域に加温して溶融し、溶融液に、多孔質基材を、適当な時間、例えば1〜10分間浸漬する方法が例示できる。 As a method of impregnating the porous substrate with the heat storage material composition, the heat storage material composition is heated and melted in a temperature range of 80 ° C. or higher, preferably 80 to 110 ° C., and melted. Further, a method of immersing the porous substrate for an appropriate time, for example, 1 to 10 minutes can be exemplified.
多孔質基材への蓄熱材組成物の含浸率としては、好ましくは180%以上、より好ましくは200%以上、より好ましくは210%以上が挙げられる。含浸率の上限は特に限定されないが通常は250%以下である。 The impregnation rate of the heat storage material composition in the porous substrate is preferably 180% or more, more preferably 200% or more, and more preferably 210% or more. The upper limit of the impregnation rate is not particularly limited, but is usually 250% or less.
含浸率(%)は次式により表すことができる。
含浸率=(含浸後の蓄熱体重量−含浸前の多孔質基材重量)/(含浸前の多孔質基材重量)x100(%)
すなわち含浸率は、多孔質基材に含浸された蓄熱材組成物の重量(=含浸後の蓄熱体重量−含浸前の多孔質基材重量)の、含浸前の多孔質基材の重量に対する割合を、後者を100%として表したものである。
The impregnation rate (%) can be expressed by the following equation.
Impregnation rate = (Weight of heat storage body after impregnation-Weight of porous substrate before impregnation) / (Weight of porous substrate before impregnation) x 100 (%)
That is, the impregnation rate is the ratio of the weight of the heat storage material composition impregnated in the porous substrate (= weight of the heat storage body after impregnation-weight of the porous substrate before impregnation) to the weight of the porous substrate before impregnation. Is expressed with the latter as 100%.
以下の試験において「部」は「質量部」を意味する。
以下の試験において、粘度の測定はJIS Z8803−2011及びJIS K7117−1に規定されている、ブルックフィールド型回転粘度計(B型粘度計)を用いた方法により行った。B型粘度計としては東機産業製ABS−100を用い、ローターサイズ:NO1、回転速度:6〜60rpmの条件で測定を行った。
In the following tests, "parts" means "parts by mass".
In the following tests, the viscosity was measured by the method using a Brookfield type rotational viscometer (B type viscometer) specified in JIS Z8803-2011 and JIS K7117-1. As the B-type viscometer, ABS-100 manufactured by Toki Sangyo was used, and the measurement was performed under the conditions of rotor size: NO1 and rotation speed: 6 to 60 rpm.
以下の試験において、熱可塑性エラストマーの重量平均分子量は、以下の条件でのゲル・パーミエーション・クロマトグラフィー(GPC)による測定に基づき、標準ポリスチレン換算値として求められたものである。 In the following tests, the weight average molecular weight of the thermoplastic elastomer was determined as a standard polystyrene equivalent value based on the measurement by gel permeation chromatography (GPC) under the following conditions.
測定機器:東ソー株式会社製ゲルパーミエーションクロマトグラフ(HLC−8020)
カラム:東ソー株式会社製TSKgel GMHXL、TSKgel G4000HXL、及びTSKgel G5000HXLを直列に連結したカラム
溶離液:テトラヒドロフラン
Measuring equipment: Gel Permeation Chromatograph manufactured by Tosoh Corporation (HLC-8020)
Column: Column in which TSKgel GMHXL, TSKgel G4000HXL, and TSKgel G5000HXL manufactured by Tosoh Corporation are connected in series Eluent: Tetrahydrofuran
<1.実験1>
本実験では、潜熱蓄熱材(ノルマルパラフィン)に、スチレン系熱可塑性エラストマー(SEBS)及び油ゲル化剤(12−ヒドロキシステアリン酸)の1種以上を添加した組成物の、70〜100℃での加熱溶融粘度、60℃での物性、寒熱試験(5℃/60℃)での潜熱蓄熱材の分離の有無を調べた。
<1. Experiment 1>
In this experiment, a composition obtained by adding one or more of a styrene-based thermoplastic elastomer (SEBS) and an oil gelling agent (12-hydroxystearic acid) to a latent heat storage material (normal paraffin) at 70 to 100 ° C. The heat melt viscosity, the physical properties at 60 ° C., and the presence or absence of separation of the latent heat storage material in the cold heat test (5 ° C./60 ° C.) were investigated.
1.1.試料
潜熱蓄熱材として融点18℃のノルマルパラフィン(炭素数16)を用いた。
トリブロック構造の水素添加スチレン系熱可塑性エラストマーとして、重量平均分子量が11万のスチレンーエチレン/ブチレンースチレンブロック共重合体(「SEBS(1)」とする)、又は、重量平均分子量が8万のスチレンーエチレン/ブチレンースチレンブロック共重合体(「SEBS(2)」とする)を用いた。
油ゲル化剤として12−ヒドロキシステアリン酸を用いた。
1.1. Sample A normal paraffin (16 carbon atoms) having a melting point of 18 ° C. was used as the latent heat storage material.
A styrene-ethylene / butylene-styrene block copolymer (referred to as "SEBS (1)") having a weight average molecular weight of 110,000 or a weight average molecular weight of 80,000 as a hydrogenated styrene-based thermoplastic elastomer having a triblock structure. Styrene-ethylene / butylene-styrene block copolymer (referred to as "SEBS (2)") was used.
12-Hydroxystearic acid was used as the oil gelling agent.
1.2.試験方法
融点18℃のノルマルパラフィン100部に対して、SEBS(1)、SEBS(2)及び12−ヒドロキシステアリン酸のうち1つ以上を、表1に示す質量部となるように添加し、100〜130℃で加熱して溶融混合して、試料1〜7の組成物を調製した。
1.2. Test method To 100 parts of normal paraffin having a melting point of 18 ° C., one or more of SEBS (1), SEBS (2) and 12-hydroxystearic acid was added so as to have a mass portion shown in Table 1 and 100 parts were added. The compositions of Samples 1 to 7 were prepared by heating at ~ 130 ° C. and melting and mixing.
調製した各試料を、100℃、90℃、80℃又は70℃で溶融させた状態で、上記の粘度計を用いて粘度を測定した。 Each of the prepared samples was melted at 100 ° C., 90 ° C., 80 ° C. or 70 ° C., and the viscosity was measured using the above viscometer.
200mLの容器に組成物を100g入れ、60℃で24時間加温し、組成物が流動性を有するか、固化しているかを観察した。 100 g of the composition was placed in a 200 mL container and heated at 60 ° C. for 24 hours, and it was observed whether the composition had fluidity or solidified.
更に、寒熱試験を次の手順で行った。上記と同様に容器に蓄熱材組成物を100g入れて常温で固化させた後、容器を横転した状態で5℃24時間の冷却と60℃24時間の加熱を5回繰り返し行った。そして、試料から潜熱蓄熱材の分離があるか否かを評価した。 Furthermore, the cold test was carried out by the following procedure. In the same manner as above, 100 g of the heat storage material composition was placed in a container and solidified at room temperature, and then cooling at 5 ° C. for 24 hours and heating at 60 ° C. for 24 hours were repeated 5 times with the container rolled over. Then, it was evaluated whether or not the latent heat storage material was separated from the sample.
1.3.結果
結果を表1に示す。
100部の潜熱蓄熱材中に15部のSEBS(1)を含むが油ゲル化剤を含まない試料1は、70℃以上での加熱溶融粘度が高く、粘度の温度依存性が高いものであった。また、60℃においてゲル化状態(固化状態)の維持が困難であった。
1.3. Results The results are shown in Table 1.
Sample 1, which contains 15 parts of SEBS (1) in 100 parts of the latent heat storage material but does not contain the oil gelling agent, has a high heat-melt viscosity at 70 ° C. or higher, and has a high temperature dependence of viscosity. rice field. In addition, it was difficult to maintain the gelled state (solidified state) at 60 ° C.
100部の潜熱蓄熱材中に表1に示す量のSEBS(1)及び/又はSEBS(2)と12−ヒドロキシステアリン酸を含む試料2〜6は、70℃以上での加熱溶融粘度が低く、粘度の温度依存性は低く、60℃においてゲル化状態(固化状態)が維持されるものであった。しかしながら寒熱試験で潜熱蓄熱材の分離(染み出し)が認められた。 Samples 2 to 6 containing SEBS (1) and / or SEBS (2) and 12-hydroxystearic acid in the amounts shown in Table 1 in 100 parts of the latent heat storage material have a low heat-melt viscosity at 70 ° C. or higher. The temperature dependence of the viscosity was low, and the gelled state (solidified state) was maintained at 60 ° C. However, separation (exudation) of the latent heat storage material was observed in the cold heat test.
これに対して、100部の潜熱蓄熱材中に10部のSEBS(1)及び5部の12−ヒドロキシステアリン酸を含む試料7(実施例)は、70℃以上での加熱溶融粘度が低く、粘度の温度依存性は低く、60℃においてゲル化状態(固化状態)が維持されるものであり、且つ、寒熱試験で潜熱蓄熱材の分離(染み出し)が認められなかった。 On the other hand, Sample 7 (Example) containing 10 parts of SEBS (1) and 5 parts of 12-hydroxystearic acid in 100 parts of the latent heat storage material has a low heat-melt viscosity at 70 ° C. or higher. The temperature dependence of the viscosity was low, the gelled state (solidified state) was maintained at 60 ° C., and the latent heat storage material was not separated (exuded) in the thermal test.
<2.実験2>
本実験では、潜熱蓄熱材(ノルマルパラフィン)にスチレン系熱可塑性エラストマー(SEBS)の1種以上を添加した試料A−1、B−1、C−1、D−1、E−1、F−1の60〜100℃での加熱溶融粘度を調べた。本実験ではまた、前記試料に、油ゲル化剤(12−ヒドロキシステアリン酸)を更に添加した試料A−2、B−2、C−2、D−2、E−2、F−2の70〜100℃での加熱溶融粘度と、寒熱試験(5℃/60℃)での潜熱蓄熱材の分離の有無を調べた。
<2. Experiment 2>
In this experiment, samples A-1, B-1, C-1, D-1, E-1, F- in which one or more styrene-based thermoplastic elastomers (SEBS) were added to a latent heat storage material (normal paraffin). The heat melt viscosity of No. 1 at 60 to 100 ° C. was examined. In this experiment, 70 of Samples A-2, B-2, C-2, D-2, E-2, and F-2 in which an oil gelling agent (12-hydroxystearic acid) was further added to the sample. The hot melt viscosity at ~ 100 ° C. and the presence / absence of separation of the latent heat storage material in the cold test (5 ° C./60 ° C.) were examined.
2.1.試料
潜熱蓄熱材として融点18℃のノルマルパラフィン(炭素数16)、又は、融点28℃のノルマルパラフィン(炭素数18)を用いた。
トリブロック構造の水素添加スチレン系熱可塑性エラストマーとして、実験1と同様に、SEBS(1)又はSEBS(2)を用いた。
油ゲル化剤として12−ヒドロキシステアリン酸を用いた。
2.1. Sample A normal paraffin having a melting point of 18 ° C. (16 carbon atoms) or a normal paraffin having a melting point of 28 ° C. (18 carbon atoms) was used as the latent heat storage material.
SEBS (1) or SEBS (2) was used as the hydrogenated styrene-based thermoplastic elastomer having a triblock structure, as in Experiment 1.
12-Hydroxystearic acid was used as the oil gelling agent.
2.2.試験方法
融点18℃のノルマルパラフィン100部又は融点28℃のノルマルパラフィン100部に対して、SEBS(1)、SEBS(2)及び12−ヒドロキシステアリン酸のうち1つ以上を、表2に示す質量部となるように添加し、100〜130℃で加熱して溶融混合して、試料A−1、B−1、C−1、D−1、E−1、F−1、A−2、B−2、C−2、D−2、E−2、F−2の組成物を調製した。試料A−2、B−2、C−2、D−2、E−2、F−2は、それぞれ、試料A−1、B−1、C−1、D−1、E−1、F−1に、5部の12−ヒドロキシステアリン酸を更に配合したものである。
2.2. Test method The mass of one or more of SEBS (1), SEBS (2) and 12-hydroxystearic acid with respect to 100 parts of normal paraffin having a melting point of 18 ° C. or 100 parts of normal paraffin having a melting point of 28 ° C. is shown in Table 2. Samples A-1, B-1, C-1, D-1, E-1, F-1, A-2, The compositions of B-2, C-2, D-2, E-2 and F-2 were prepared. Samples A-2, B-2, C-2, D-2, E-2, and F-2 are samples A-1, B-1, C-1, D-1, E-1, F, respectively. -1 is further blended with 5 parts of 12-hydroxystearic acid.
調製した各試料を、100℃、90℃、80℃、70℃又は60℃で溶融させた状態で上記の粘度計を用いて粘度を測定した。ただし、試料A−2、B−2、C−2、D−2、E−2、F−2については、60℃での溶融粘度は測定していない。 The viscosity of each of the prepared samples was measured using the above viscometer in a state of being melted at 100 ° C., 90 ° C., 80 ° C., 70 ° C. or 60 ° C. However, for the samples A-2, B-2, C-2, D-2, E-2, and F-2, the melt viscosity at 60 ° C. was not measured.
また、試料A−2、B−2、C−2、D−2、E−2、F−2については、実験1と同様の手順で寒熱試験を行い、潜熱蓄熱材の分離があるか否かを評価した。 For samples A-2, B-2, C-2, D-2, E-2, and F-2, a thermal test was performed in the same procedure as in Experiment 1, and whether or not the latent heat storage material was separated. Was evaluated.
2.3.結果
結果を表2に示す。
潜熱蓄熱材(ノルマルパラフィン)にSEBS(1)及び/又はSEBS(2)と12−ヒドロキシステアリン酸とを配合した試料A−2、B−2、C−2、D−2、E−2、F−2は、70℃以上での加熱溶融粘度が低く(例えば80℃での溶融粘度が200mPa・s以下)、且つ、粘度の温度依存性は低いことが認められた。これらの試料は多孔質基材への含浸が容易であることがわかる。
2.3. Results The results are shown in Table 2.
Samples A-2, B-2, C-2, D-2, E-2, in which SEBS (1) and / or SEBS (2) and 12-hydroxystearic acid are mixed with a latent heat storage material (normal paraffin). It was found that F-2 had a low heat melt viscosity at 70 ° C. or higher (for example, a melt viscosity at 80 ° C. was 200 mPa · s or less), and the temperature dependence of the viscosity was low. It can be seen that these samples are easily impregnated into the porous substrate.
更に、試料C−2、E−2、F−2は、寒熱試験で潜熱蓄熱材の分離が認められなかった。一方で、試料A−2、B−2、D−2は、寒熱試験で潜熱蓄熱材の分離が認められた。 Furthermore, in the samples C-2, E-2, and F-2, separation of the latent heat storage material was not observed in the cold heat test. On the other hand, in the samples A-2, B-2 and D-2, the separation of the latent heat storage material was confirmed in the cold heat test.
試料C−2、E−2、F−2は、それぞれ、試料C−1、E−1、F−1に12−ヒドロキシステアリン酸を5部配合したものであり、試料A−2、B−2、D−2は、それぞれ、試料A−1、B−1、D−1に12−ヒドロキシステアリン酸を5部配合したものである。試料C−1、E−1、F−1の60℃での溶融粘度が3500mPa・s以上であるのに対し、試料A−1、B−1、D−1の60℃での溶融粘度が3500mPa・s未満であった。 Samples C-2, E-2, and F-2 are prepared by blending 5 parts of 12-hydroxystearic acid with Samples C-1, E-1, and F-1, respectively, and Samples A-2 and B- 2 and D-2 are samples A-1, B-1, and D-1 mixed with 5 parts of 12-hydroxystearic acid, respectively. The melt viscosities of the samples C-1, E-1, and F-1 at 60 ° C. are 3500 mPa · s or more, whereas the melt viscosities of the samples A-1, B-1, and D-1 at 60 ° C. are high. It was less than 3500 mPa · s.
このことから、水素添加スチレン系熱可塑性エラストマー(SEBS)のみを添加した潜熱蓄熱材(ノルマルパラフィン)の60℃での溶融粘度が3500mPa・s以上となるようにSEBSの種類と配合量を調節し、更に油ゲル化剤(12−ヒドロキシステアリン酸)を配合することで、潜熱蓄熱材の分離の無い組成物が得られることが支持される。 Therefore, the type and blending amount of SEBS were adjusted so that the melt viscosity of the latent heat storage material (normal paraffin) to which only the hydrogenated styrene-based thermoplastic elastomer (SEBS) was added at 60 ° C. was 3500 mPa · s or more. Further, by blending an oil gelling agent (12-hydroxystearic acid), it is supported that a composition without separation of the latent heat storage material can be obtained.
<3.実験3>
本実験では、潜熱蓄熱材(ノルマルパラフィン)に水素添加スチレン系熱可塑性エラストマーとしてスチレン−エチレン/プロピレンブロック共重合体(SEP)を添加した組成物(試料G−1、H−1、I−1)の60〜100℃での加熱溶融粘度を調べた。本実験ではまた、前記試料に、油ゲル化剤(12−ヒドロキシステアリン酸)を更に添加した試料G−2、H−2、I−2の70〜100℃での加熱溶融粘度と、寒熱試験(5℃/60℃)での潜熱蓄熱材の分離の有無を調べた。
<3. Experiment 3>
In this experiment, a composition (Samples G-1, H-1, I-1) in which a styrene-ethylene / propylene block copolymer (SEP) was added as a hydrogenated styrene-based thermoplastic elastomer to a latent heat storage material (normal paraffin). ) Was examined by heating and melting at 60 to 100 ° C. In this experiment, the heat melt viscosity of the samples G-2, H-2, and I-2 to which the oil gelling agent (12-hydroxystearic acid) was further added to the sample at 70 to 100 ° C. and the thermal test The presence or absence of separation of the latent heat storage material at (5 ° C / 60 ° C) was investigated.
3.1.試料
潜熱蓄熱材として融点18℃のノルマルパラフィン(炭素数16)を用いた。
ジブロック構造の水素添加スチレン系熱可塑性エラストマーとして、重量平均分子量が22万のスチレン−エチレン/プロピレンブロック共重合体(「SEP(1)」とする)、又は、重量平均分子量が30万のスチレン−エチレン/プロピレンブロック共重合体(「SEP(2)」とする)を用いた。
油ゲル化剤として12−ヒドロキシステアリン酸を用いた。
3.1. Sample A normal paraffin (16 carbon atoms) having a melting point of 18 ° C. was used as the latent heat storage material.
As a diblock-structured hydrogenated styrene-based thermoplastic elastomer, a styrene-ethylene / propylene block copolymer having a weight average molecular weight of 220,000 (referred to as "SEP (1)") or styrene having a weight average molecular weight of 300,000. -An ethylene / propylene block copolymer (referred to as "SEP (2)") was used.
12-Hydroxystearic acid was used as the oil gelling agent.
3.2.試験方法
融点18℃のノルマルパラフィン100部に対して、SEP(1)、SEP(2)及び12−ヒドロキシステアリン酸のうち1つ以上を、表3に示す質量部となるように添加し、100〜130℃で加熱して溶融混合して、試料G−1、H−1、I−1、G−2、H−2、I−2の組成物を調製した。試料G−2、H−2、I−2は、それぞれ、試料G−1、H−1、I−1に、5部の12−ヒドロキシステアリン酸を更に配合したものである。
3.2. Test method To 100 parts of normal paraffin having a melting point of 18 ° C., one or more of SEP (1), SEP (2) and 12-hydroxystearic acid was added so as to have a mass portion shown in Table 3 and 100 parts were added. The compositions of Samples G-1, H-1, I-1, G-2, H-2, and I-2 were prepared by heating at ~ 130 ° C. and melting and mixing. Samples G-2, H-2, and I-2 are prepared by further blending 5 parts of 12-hydroxystearic acid with Samples G-1, H-1, and I-1, respectively.
調製した各試料を、100℃、90℃、80℃、70℃又は60℃で溶融させた状態で上記の粘度計を用いて粘度を測定した。ただし、試料G−2、H−2、I−2については、60℃での溶融粘度は測定していない。 The viscosity of each of the prepared samples was measured using the above viscometer in a state of being melted at 100 ° C., 90 ° C., 80 ° C., 70 ° C. or 60 ° C. However, for the samples G-2, H-2, and I-2, the melt viscosity at 60 ° C. was not measured.
また、試料G−2、H−2、I−2については、実験1と同様の手順で寒熱試験を行い、潜熱蓄熱材の分離があるか否かを評価した。 Further, the samples G-2, H-2, and I-2 were subjected to a cold heat test in the same procedure as in Experiment 1 to evaluate whether or not the latent heat storage material was separated.
3.3.結果
結果を表3に示す。
潜熱蓄熱材(ノルマルパラフィン)にSEP(1)又はSEP(2)を配合した試料G−1、H−1、I−1は、70〜100℃の温度域での溶融粘度の温度依存性が低いことが認められた。また、試料G−1、H−1に更に12−ヒドロキシステアリン酸を配合した試料G−2、H−2は、寒熱試験で潜熱蓄熱材の分離が認められた。すなわち、潜熱蓄熱材(ノルマルパラフィン)にSEP(1)又はSEP(2)を配合した試料に更に12−ヒドロキシステアリン酸を配合したとしても、多孔質基材への含浸時の低粘度化と、潜熱蓄熱材の安定保持(寒熱試験耐性)を両立することが困難であることが確認された。
3.3. Results The results are shown in Table 3.
Samples G-1, H-1, and I-1 in which SEP (1) or SEP (2) is mixed with a latent heat storage material (normal paraffin) have a temperature dependence of the melt viscosity in the temperature range of 70 to 100 ° C. It was found to be low. Further, in the samples G-2 and H-2 in which 12-hydroxystearic acid was further added to the samples G-1 and H-1, separation of the latent heat storage material was observed in the cold heat test. That is, even if 12-hydroxystearic acid is further added to the sample in which SEP (1) or SEP (2) is added to the latent heat storage material (normal paraffin), the viscosity at the time of impregnation into the porous substrate is reduced. It was confirmed that it is difficult to achieve both stable retention of the latent heat storage material (resistant to the cold test).
以上の結果から、ジブロック構造の水素添加スチレン系熱可塑性エラストマーを潜熱蓄熱材の固化に用いた場合には、油ゲル化剤を更に配合したとしても、多孔質基材への含浸時の低粘度化と、潜熱蓄熱材の安定保持(寒熱試験耐性)を両立することが困難であることが分かる。 From the above results, when a hydrogenated styrene-based thermoplastic elastomer having a diblock structure is used for solidifying the latent heat storage material, even if an oil gelling agent is further added, the amount is low when impregnated into the porous substrate. It can be seen that it is difficult to achieve both viscosity increase and stable retention of the latent heat storage material (cold heat test resistance).
<4.実験4>
本実験では、潜熱蓄熱材(ノルマルパラフィン)にスチレン系熱可塑性エラストマー(SEBS)を配合した試料10、並びに、潜熱蓄熱材(ノルマルパラフィン)にスチレン系熱可塑性エラストマー(SEBS又はSEP)と油ゲル化剤(12−ヒドロキシステアリン酸)とを配合した試料8、9、11の100℃又は80℃での加熱溶融粘度を調べた。本実験ではまた、100℃に溶融した試料8〜11に多孔質基材を1〜10分間浸漬したときの、試料8〜11の多孔質基材への含浸率を測定した。
<4. Experiment 4>
In this experiment, sample 10 in which a styrene-based thermoplastic elastomer (SEBS) was mixed with a latent heat storage material (normal paraffin), and a styrene-based thermoplastic elastomer (SEBS or SEP) and oil gelled in a latent heat storage material (normal paraffin). The heat melt viscosity of Samples 8, 9 and 11 containing the agent (12-hydroxystearic acid) at 100 ° C. or 80 ° C. was examined. In this experiment, the impregnation rate of the porous substrate into the porous substrate was measured when the porous substrate was immersed in the samples 8 to 11 melted at 100 ° C. for 1 to 10 minutes.
4.1.試料
潜熱蓄熱材として融点18℃のノルマルパラフィン(炭素数16)、又は、融点28℃のノルマルパラフィン(炭素数18)を用いた。
トリブロック構造の水素添加スチレン系熱可塑性エラストマーとして、実験1で記載のSEBS(1)を用いた。ジブロック構造の水素添加スチレン系熱可塑性エラストマーとして、実験3で記載のSEP(2)を用いた。
油ゲル化剤として12−ヒドロキシステアリン酸を用いた。
多孔質基材として木質繊維板(インシュレーションボード、寸法:200×200×厚さ5mm)を用いた。
4.1. Sample A normal paraffin having a melting point of 18 ° C. (16 carbon atoms) or a normal paraffin having a melting point of 28 ° C. (18 carbon atoms) was used as the latent heat storage material.
SEBS (1) described in Experiment 1 was used as a hydrogenated styrene-based thermoplastic elastomer having a triblock structure. The SEP (2) described in Experiment 3 was used as the hydrogenated styrene-based thermoplastic elastomer having a diblock structure.
12-Hydroxystearic acid was used as the oil gelling agent.
A wood fiber board (insulation board, dimensions: 200 × 200 × thickness 5 mm) was used as the porous base material.
4.2.試験方法
融点18℃のノルマルパラフィン100部又は融点28℃のノルマルパラフィン100部に対して、SEBS(1)、SEP(2)及び12−ヒドロキシステアリン酸のうち1つ以上を、表4に示す質量部となるように添加し、100〜130℃で加熱して溶融混合して、試料8〜11の組成物を調製した。
4.2. Test method For 100 parts of normal paraffin with a melting point of 18 ° C or 100 parts of normal paraffin with a melting point of 28 ° C, one or more of SEBS (1), SEP (2) and 12-hydroxystearic acid is added to the mass shown in Table 4. The composition was prepared as a sample 8 to 11 by adding the mixture in portions, heating at 100 to 130 ° C. and melting and mixing.
調製した各試料を、100℃又は80℃で溶融させた状態で上記の粘度計を用いて粘度を測定した。 The viscosity of each of the prepared samples was measured using the above-mentioned viscometer in a state of being melted at 100 ° C. or 80 ° C.
100℃で加熱溶融した状態の各試料に、多孔質基材を、1分間、3分間、5分間又は10分間浸漬し、引き揚げた。多孔質基材の重量を含浸の前後で求め、次式により含浸率を算出した。
含浸率=(含浸後の蓄熱体重量−含浸前の多孔質基材重量)/(含浸前の多孔質基材重量)x100(%)
The porous substrate was immersed in each sample heated and melted at 100 ° C. for 1 minute, 3 minutes, 5 minutes or 10 minutes, and then withdrawn. The weight of the porous substrate was determined before and after impregnation, and the impregnation rate was calculated by the following formula.
Impregnation rate = (Weight of heat storage body after impregnation-Weight of porous substrate before impregnation) / (Weight of porous substrate before impregnation) x 100 (%)
4.3.結果
結果を表4に示す。
100部の潜熱蓄熱材(ノルマルパラフィン)に10部のSEBS(1)と5部の12−ヒドロキシステアリン酸とを配合した、80℃での溶融粘度が200mPa・s以下、100℃での溶融粘度が30mPa・s以下である、試料8、9の100℃での溶融液に多孔質基材を浸漬したとき、3分間の浸漬で含浸率は飽和状態(約220%)に到達した。1分間の浸漬でも含浸率は十分に高かった。
4.3. Results The results are shown in Table 4.
A blend of 10 parts of SEBS (1) and 5 parts of 12-hydroxystearic acid in 100 parts of latent heat storage material (normal paraffin), the melt viscosity at 80 ° C is 200 mPa · s or less, and the melt viscosity at 100 ° C. When the porous substrate was immersed in the melt of Samples 8 and 9 at 100 ° C., which had a viscosity of 30 mPa · s or less, the impregnation rate reached a saturated state (about 220%) after immersion for 3 minutes. The impregnation rate was sufficiently high even after soaking for 1 minute.
一方、100部の潜熱蓄熱材(ノルマルパラフィン)に15部のSEBS(1)のみを配合した試料10の100℃での溶融液に多孔質基材を浸漬したとき、5分間以上の浸漬で含浸率は飽和状態(約220%)に到達するが、含浸時間が短い場合は含浸率が大きく低下した。 On the other hand, when the porous substrate is immersed in a melt of sample 10 containing only 15 parts of SEBS (1) in 100 parts of latent heat storage material (normal paraffin) at 100 ° C., it is impregnated by immersion for 5 minutes or more. The rate reached a saturated state (about 220%), but when the impregnation time was short, the impregnation rate was greatly reduced.
100部の潜熱蓄熱材(ノルマルパラフィン)に5部のSEP(2)と5部の12−ヒドロキシステアリン酸とを配合した試料11の100℃での溶融液に多孔質基材を浸漬したとき、10分間浸漬した場合でも含浸率は飽和状態(約220%)に到達しなかった。 When the porous substrate is immersed in the melt of sample 11 at 100 ° C., which is a mixture of 100 parts of latent heat storage material (normal paraffin), 5 parts of SEP (2) and 5 parts of 12-hydroxystearic acid. The impregnation rate did not reach the saturated state (about 220%) even when immersed for 10 minutes.
Claims (7)
前記エラストマーが、ソフトセグメントと、前記ソフトセグメントの両端に結合したハードセグメントとを少なくとも含む、トリブロック以上のブロック共重合体を含み、
前記油ゲル化剤が、炭素数が12以上24以下の飽和又は不飽和カルボン酸、炭素数が12以上24以下の飽和又は不飽和カルボン酸の金属塩、炭素数が12以上24以下のヒドロキシカルボン酸、炭素数が12以上24以下のヒドロキシカルボン酸の金属塩、ジベンジリデンソルビトール、及び、アミノ酸系油ゲル化剤からなる群から選択される1種以上を含み、
80℃での溶融粘度が200mPa・s以下であり、
前記潜熱蓄熱材100質量部に対しX質量部の前記エラストマーを含み、ここでX質量部とは、100質量部の前記潜熱蓄熱材とX質量部の前記エラストマーとからなる混合物の60℃での溶融粘度が3500mPa・s以上となる量である、
ことを特徴とする蓄熱材組成物。 It contains a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent.
The elastomer comprises a block copolymer of triblock or higher, comprising at least a soft segment and hard segments bonded to both ends of the soft segment.
The oil gelling agent is a saturated or unsaturated carboxylic acid having 12 or more and 24 or less carbon atoms, a metal salt of a saturated or unsaturated carboxylic acid having 12 or more and 24 carbon atoms or less, and a hydroxycarboxylic acid having 12 or more and 24 carbon atoms or less. It contains one or more selected from the group consisting of an acid, a metal salt of a hydroxycarboxylic acid having 12 or more and 24 or less carbon atoms, dibenzylidene sorbitol, and an amino acid-based oil gelling agent.
The melt viscosity at 80 ° C. is 200 mPa · s or less,
An X mass portion of the elastomer is contained with respect to 100 parts by mass of the latent heat storage material, and the X mass portion is the mixture of 100 parts by mass of the latent heat storage material and the X mass portion of the elastomer at 60 ° C. The amount is such that the melt viscosity is 3500 mPa · s or more.
A heat storage material composition characterized by this.
潜熱蓄熱材と、水素添加スチレン系熱可塑性エラストマーと、油ゲル化剤とを、溶融混練する溶融混練工程と、
溶融混練工程において生成した混合物を冷却する冷却工程と
を含む方法。 The method for producing a heat storage material composition according to any one of claims 1 to 5.
A melt-kneading step in which a latent heat storage material, a hydrogenated styrene-based thermoplastic elastomer, and an oil gelling agent are melt-kneaded.
A method comprising a cooling step of cooling the mixture produced in the melt-kneading step.
前記多孔質基材に含浸された、請求項1〜5のいずれか1項に記載の蓄熱材組成物と
を少なくとも備える蓄熱体。 Porous substrate and
A heat storage body comprising at least the heat storage material composition according to any one of claims 1 to 5, which is impregnated with the porous substrate.
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