TWI636078B - Biomass thermoplastic polyurethane - Google Patents
Biomass thermoplastic polyurethane Download PDFInfo
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- TWI636078B TWI636078B TW106146226A TW106146226A TWI636078B TW I636078 B TWI636078 B TW I636078B TW 106146226 A TW106146226 A TW 106146226A TW 106146226 A TW106146226 A TW 106146226A TW I636078 B TWI636078 B TW I636078B
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- polyol
- biothermoplastic
- weight
- lignin
- diisocyanate
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- 239000004433 Thermoplastic polyurethane Substances 0.000 title claims abstract description 19
- 229920002803 thermoplastic polyurethane Polymers 0.000 title claims abstract description 19
- 239000002028 Biomass Substances 0.000 title abstract description 13
- 229920005862 polyol Polymers 0.000 claims abstract description 68
- 150000003077 polyols Chemical class 0.000 claims abstract description 68
- 229920005610 lignin Polymers 0.000 claims abstract description 64
- 239000004814 polyurethane Substances 0.000 claims abstract description 32
- 229920002635 polyurethane Polymers 0.000 claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 20
- 125000005442 diisocyanate group Chemical group 0.000 claims abstract description 11
- 239000000203 mixture Substances 0.000 claims abstract description 11
- -1 methylene diphenyl Chemical group 0.000 claims description 17
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 13
- 229920000570 polyether Polymers 0.000 claims description 13
- 229920005906 polyester polyol Polymers 0.000 claims description 12
- 125000000524 functional group Chemical group 0.000 claims description 10
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- 125000004178 (C1-C4) alkyl group Chemical group 0.000 claims description 5
- ALQLPWJFHRMHIU-UHFFFAOYSA-N 1,4-diisocyanatobenzene Chemical compound O=C=NC1=CC=C(N=C=O)C=C1 ALQLPWJFHRMHIU-UHFFFAOYSA-N 0.000 claims description 4
- 239000005057 Hexamethylene diisocyanate Substances 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 4
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical group O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 claims description 4
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 claims description 4
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 4
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 claims description 4
- SBJCUZQNHOLYMD-UHFFFAOYSA-N 1,5-Naphthalene diisocyanate Chemical compound C1=CC=C2C(N=C=O)=CC=CC2=C1N=C=O SBJCUZQNHOLYMD-UHFFFAOYSA-N 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 2
- XTDOJEFMYWVGBA-UHFFFAOYSA-N C=C.C=C.C1(=CC=CC=C1)CC1=CC=CC=C1 Chemical compound C=C.C=C.C1(=CC=CC=C1)CC1=CC=CC=C1 XTDOJEFMYWVGBA-UHFFFAOYSA-N 0.000 claims 1
- 238000006356 dehydrogenation reaction Methods 0.000 claims 1
- 150000002009 diols Chemical class 0.000 description 11
- 238000002360 preparation method Methods 0.000 description 9
- 229920000909 polytetrahydrofuran Polymers 0.000 description 8
- 238000003756 stirring Methods 0.000 description 8
- 239000003054 catalyst Substances 0.000 description 6
- 239000002981 blocking agent Substances 0.000 description 5
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000002202 Polyethylene glycol Substances 0.000 description 4
- 238000005299 abrasion Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 229920001223 polyethylene glycol Polymers 0.000 description 4
- 229920001451 polypropylene glycol Polymers 0.000 description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 229940113088 dimethylacetamide Drugs 0.000 description 3
- 229920001169 thermoplastic Polymers 0.000 description 3
- 239000004416 thermosoftening plastic Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 239000005058 Isophorone diisocyanate Substances 0.000 description 2
- KLDXJTOLSGUMSJ-JGWLITMVSA-N Isosorbide Chemical compound O[C@@H]1CO[C@@H]2[C@@H](O)CO[C@@H]21 KLDXJTOLSGUMSJ-JGWLITMVSA-N 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- ALQSHHUCVQOPAS-UHFFFAOYSA-N Pentane-1,5-diol Chemical compound OCCCCCO ALQSHHUCVQOPAS-UHFFFAOYSA-N 0.000 description 2
- 229920000616 Poly(1,4-butylene adipate) Polymers 0.000 description 2
- 229920000562 Poly(ethylene adipate) Polymers 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 229960002479 isosorbide Drugs 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003209 petroleum derivative Substances 0.000 description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 230000005070 ripening Effects 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- YSRSBDQINUMTIF-SNVBAGLBSA-N (2r)-decane-1,2-diol Chemical compound CCCCCCCC[C@@H](O)CO YSRSBDQINUMTIF-SNVBAGLBSA-N 0.000 description 1
- DWANEFRJKWXRSG-UHFFFAOYSA-N 1,2-tetradecanediol Chemical compound CCCCCCCCCCCCC(O)CO DWANEFRJKWXRSG-UHFFFAOYSA-N 0.000 description 1
- 229940043375 1,5-pentanediol Drugs 0.000 description 1
- ALVZNPYWJMLXKV-UHFFFAOYSA-N 1,9-Nonanediol Chemical compound OCCCCCCCCCO ALVZNPYWJMLXKV-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- FJDQFPXHSGXQBY-UHFFFAOYSA-L caesium carbonate Chemical compound [Cs+].[Cs+].[O-]C([O-])=O FJDQFPXHSGXQBY-UHFFFAOYSA-L 0.000 description 1
- 229910000024 caesium carbonate Inorganic materials 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229940097037 decylene glycol Drugs 0.000 description 1
- GHLKSLMMWAKNBM-UHFFFAOYSA-N dodecane-1,12-diol Chemical compound OCCCCCCCCCCCCO GHLKSLMMWAKNBM-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- GKEMUBZAKCZMKO-UHFFFAOYSA-N ethane-1,2-diol;ethene Chemical compound C=C.OCCO GKEMUBZAKCZMKO-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- FNKQFBWKNIGIOS-UHFFFAOYSA-N furan-2,5-diol Chemical compound OC1=CC=C(O)O1 FNKQFBWKNIGIOS-UHFFFAOYSA-N 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- SXCBDZAEHILGLM-UHFFFAOYSA-N heptane-1,7-diol Chemical compound OCCCCCCCO SXCBDZAEHILGLM-UHFFFAOYSA-N 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- OEIJHBUUFURJLI-UHFFFAOYSA-N octane-1,8-diol Chemical compound OCCCCCCCCO OEIJHBUUFURJLI-UHFFFAOYSA-N 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000004382 potting Methods 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 125000002914 sec-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007655 standard test method Methods 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 239000012974 tin catalyst Substances 0.000 description 1
- XSMIOONHPKRREI-UHFFFAOYSA-N undecane-1,11-diol Chemical compound OCCCCCCCCCCCO XSMIOONHPKRREI-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Polyurethanes Or Polyureas (AREA)
Abstract
本揭露提供一種生質熱可塑性聚氨酯。該生質熱可塑性聚氨酯係由一組合物反應所形成,該組合物包含:1-50重量份的改質木質素,其中該改質木質素的羥基值(OH value)係小於3mmol/g;50-99重量份的第一多元醇,其中該改質木質素與該第一多元醇的總重為100重量份;以及,40-60重量份二異氰酸酯。 The present disclosure provides a biomass thermoplastic polyurethane. The biothermoplastic polyurethane is formed by a reaction of a composition comprising: 1-50 parts by weight of modified lignin, wherein the modified lignin has a hydroxyl value (OH value) of less than 3 mmol/g; 50 to 99 parts by weight of the first polyol, wherein the total weight of the modified lignin and the first polyol is 100 parts by weight; and, 40 to 60 parts by weight of the diisocyanate.
Description
本揭露關於一種生質熱可塑性聚氨酯。 The present disclosure relates to a biomass thermoplastic polyurethane.
熱塑性聚氨酯(thermoplastic polyurethane,TPU)由於其柔韌且高彈性,已廣泛應用於泡沫坐墊、保溫板、電子灌封膠、高性能粘合劑、表面塗層、包裝、表面密封劑以及合成纖維。 Thermoplastic polyurethane (TPU) has been widely used in foam cushions, insulation boards, electronic potting compounds, high performance adhesives, surface coatings, packaging, surface sealants and synthetic fibers due to its flexibility and high elasticity.
用於熱塑性聚氨酯生產的多元醇通常來自於石油產物。然而,由於環境問題,如今越來越多的工業製造方法正試圖用生物質產物來替代石油產物。其中,木質素作為一種多元醇生物質,可以很容易的從食品級和非食品級的生物質中提取得到,例如農業廢棄物或森林中的生物質。然而,直接將木質素與異氰酸酯反應合成熱塑性聚氨酯則會因為過度交聯而導致產物失去熱可塑性。 Polyols used in the production of thermoplastic polyurethanes are typically derived from petroleum products. However, due to environmental concerns, more and more industrial manufacturing methods are now attempting to replace petroleum products with biomass products. Among them, lignin, as a polyol biomass, can be easily extracted from food-grade and non-food-grade biomass, such as agricultural waste or biomass in forests. However, direct reaction of lignin with isocyanate to form a thermoplastic polyurethane results in loss of thermoplasticity due to excessive crosslinking.
因此,業界需要一種新穎的熱塑性聚氨酯,以解決習知技術所遭遇到的問題。 Therefore, the industry needs a novel thermoplastic polyurethane to solve the problems encountered in the prior art.
根據本揭露實施例,本揭露提供一種生質熱可塑性聚氨酯。該生質熱可塑性聚氨酯可由一組合物反應所形成,該組 合物包含:1-50重量份的改質木質素;50-99重量份的第一多元醇;以及,40-60重量份二異氰酸酯。其中,該改質木質素的羥基值(OH value)係小於3mmol/g,且該改質木質素與該第一多元醇的總重為100重量份。 According to an embodiment of the present disclosure, the present disclosure provides a biomass thermoplastic polyurethane. The biothermoplastic polyurethane can be formed by a reaction of a group of components, the group The composition comprises: 1 to 50 parts by weight of modified lignin; 50 to 99 parts by weight of the first polyol; and, 40 to 60 parts by weight of diisocyanate. Wherein, the modified lignin has a hydroxyl value (OH value) of less than 3 mmol/g, and the total weight of the modified lignin and the first polyol is 100 parts by weight.
本揭露實施例提供一種生質熱可塑性聚氨酯。本揭露利用特定比例的改質木質素(羥基值(OH value)小於3mmol/g)、多元醇、以及二異氰酸酯來製備生質熱可塑性聚氨酯,可使所得之生質熱可塑性聚氨酯具有較高的機械強度及耐磨耗性。此外,當添加未改質的木質素與多元醇及二異氰酸酯反應時,若木質素添加量過多,易導致木質素聚集使得所得產物機械強度下降。若木質素添加量不夠,則無法明顯改善所得產物的機械強度及耐磨性。由於本揭露使用羥基值(OH value)小於3mmol/g的改質木質素與多元醇及二異氰酸酯反應,當提昇木質素添加量時不會導致過度交聯,因此所得生質聚氨酯在具有明顯提昇的機械強度、及耐磨耗性的同時,還保有熱可塑性。 The disclosed embodiments provide a biomass thermoplastic polyurethane. The present disclosure utilizes a specific proportion of modified lignin (hydroxy value (OH value) less than 3 mmol / g), polyol, and diisocyanate to prepare a biothermoplastic polyurethane, which can make the obtained biothermoplastic polyurethane have higher Mechanical strength and wear resistance. Further, when unmodified lignin is added to react with a polyol and a diisocyanate, if the amount of lignin added is too large, lignin aggregation is liable to cause a decrease in mechanical strength of the obtained product. If the amount of lignin added is insufficient, the mechanical strength and wear resistance of the obtained product cannot be remarkably improved. Since the present invention uses a modified lignin having a hydroxyl value (OH value) of less than 3 mmol/g to react with a polyhydric alcohol and a diisocyanate, when the amount of lignin is increased, no excessive crosslinking is caused, and thus the resulting bio-based polyurethane has a significant improvement. At the same time of mechanical strength and wear resistance, it also retains thermoplasticity.
根據本揭露實施例,本揭露提供一種生質熱可塑性聚氨酯。該生質熱可塑性聚氨酯可由一組合物反應所形成,該組合物包含:1-50重量份(例如2-25重量份、10-30重量份、或10-20重量份)的改質木質素;50-99重量份(例如75-98重量份、70-90 重量份、或80-90重量份)的第一多元醇;以及,40-60重量份(例如45-55重量份)二異氰酸酯。其中,該改質木質素的羥基值(OH value)係小於約3mmol/g,且該改質木質素與該第一多元醇的總重可為100重量份。 According to an embodiment of the present disclosure, the present disclosure provides a biomass thermoplastic polyurethane. The biothermoplastic polyurethane may be formed by a reaction of a composition comprising: 1 to 50 parts by weight (for example, 2 to 25 parts by weight, 10 to 30 parts by weight, or 10 to 20 parts by weight) of modified lignin. 50-99 parts by weight (for example, 75-98 parts by weight, 70-90 Parts by weight, or 80 to 90 parts by weight, of the first polyol; and, 40 to 60 parts by weight (for example, 45 to 55 parts by weight) of the diisocyanate. Wherein, the modified lignin has a hydroxyl value (OH value) of less than about 3 mmol/g, and the total weight of the modified lignin and the first polyol may be 100 parts by weight.
根據本揭露實施例,該改質木質素可具有至少一封端官能基的木質素,且該封端官能基係與該木質素上羥基去氫所得之殘基鍵結。其中,該封端官能基(R1)係C1-4烷基、苯基、 、或,其中R2及R3係各自獨立為C1-4烷基; 以及,n係1、2、3或4。 According to an embodiment of the present disclosure, the modified lignin may have at least one terminal functional group of lignin, and the capping functional group is bonded to a residue obtained by dehydrogenating a hydroxyl group on the lignin. Wherein the capping functional group (R 1 ) is a C 1-4 alkyl group, a phenyl group, ,or Wherein R 2 and R 3 are each independently C 1-4 alkyl; and n is 1, 2, 3 or 4.
根據本揭露實施例,該C1-4烷基可為直鏈或分支(linear or branched)鏈的烷基。舉例來說,C1-4烷基可為甲基(methyl)、乙基(ethyl)、丙基(propyl)、異丙基(isopropyl)、正丁基(n-butyl)、叔丁基(t-butyl)、仲丁基(sec-butyl)、或異丁基(isobutyl)。 According to an embodiment of the present disclosure, the C 1-4 alkyl group may be a linear or branched chain alkyl group. For example, a C 1-4 alkyl group can be methyl, ethyl, propyl, isopropyl, n-butyl, t-butyl ( T-butyl), sec-butyl, or isobutyl.
根據本揭露實施例,本揭露所述該改質木質素可具有式(I)所述結構
其中,L係為去除i個羥基所留下之木質素殘基;R1 係C1-4烷基、苯基、、或,其中R2及R2係 各自獨立為C1-4烷基;以及,n係1、2、3或4:以及,3<i≦10(例如:3<i≦9、3<i≦7、3<i≦6、3<i≦5、3<i≦4.8、3<i≦4.6、3<i ≦4.4、3<i≦4.2、或3<i≦4.0)。 Wherein, L is a lignin residue left by removing i hydroxyl groups; R 1 is a C 1-4 alkyl group, a phenyl group, ,or Wherein R 2 and R 2 are each independently C 1-4 alkyl; and, n is 1, 2, 3 or 4: and 3 < i ≦ 10 (for example: 3 < i ≦ 9, 3 < i ≦ 7, 3 < i ≦ 6, 3 < i ≦ 5, 3 < i ≦ 4.8, 3 < i ≦ 4.6, 3 < i ≦ 4.4, 3 < i ≦ 4.2, or 3 < i ≦ 4.0).
根據本揭露實施例,用來形成改質木質素的木質素可為磺酸鹽木質素、鹼木質素、或上述之組合。根據本揭露實施例,該改質木質素的羥基值(OH value)可為約2mmol/g至2.9mmol/g,例如:2.1mmol/g至2.8mmol/g、2.2mmol/g至2.7mmol/g、或2.3mmol/g至2.6mmol/g。若改質木質素的羥基值(OH value)過高時,易導致PU交聯失去熱可塑特性;若改質木質素的羥基值(OH value)過低時,易導致分子量低物性差。 According to embodiments of the present disclosure, the lignin used to form the modified lignin may be a sulfonate lignin, an alkali lignin, or a combination thereof. According to an embodiment of the present disclosure, the modified lignin may have a hydroxyl value (OH value) of from about 2 mmol/g to 2.9 mmol/g, for example, from 2.1 mmol/g to 2.8 mmol/g, from 2.2 mmol/g to 2.7 mmol/ g, or 2.3 mmol/g to 2.6 mmol/g. If the hydroxyl value (OH value) of the modified lignin is too high, the PU cross-linking tends to lose the thermoplastic property; if the hydroxyl value (OH value) of the modified lignin is too low, the molecular weight is low and the physical properties are poor.
根據本揭露實施例,該第一多元醇係為聚合物多元醇。根據本揭露實施例,其中該第一多元醇之數目平均分子量可為500至100000,例如500至80000、1000至60000、2000至50000、或5000至40000。 According to an embodiment of the present disclosure, the first polyol is a polymer polyol. According to an embodiment of the present disclosure, the number average molecular weight of the first polyol may be from 500 to 100,000, such as from 500 to 80,000, from 1,000 to 60,000, from 2,000 to 50,000, or from 5,000 to 40,000.
根據本揭露實施例,該第一多元醇可為聚酯多元醇(polyester polyol)、或聚醚多元醇(polyether polyol)。根據本揭露實施例,該聚酯多元醇可為聚(乙二醇己二酸酯)二醇(poly(ethylene adipate)diol)、聚(1,4-丁二醇己二酸酯)二醇(poly(1,4-butylene adipate)diol)、聚(乙二醇十二酸酯)二醇(poly(ethylene dodecanoate)diol)、或聚(1,6-己二醇己二酸酯)二醇(poly(1,6-hexathylene adipate)diol)。 According to an embodiment of the present disclosure, the first polyol may be a polyester polyol, or a polyether polyol. According to an embodiment of the present disclosure, the polyester polyol may be poly(ethylene adipate) diol or poly(1,4-butanediol adipate) diol. (poly(1,4-butylene adipate) diol), poly(ethylene dodecanoate) diol, or poly(1,6-hexanediol adipate) Poly(1,6-hexathylene adipate) diol.
此外,根據本揭露實施例,該聚醚多元醇可為聚乙二醇(polyethylene glycol,PEG)、聚丙二醇(polypropylene glycol,PPG)、或聚四亞甲基醚二醇(polytetramethylene ether glycol,PTMEG)。 In addition, according to the embodiments of the present disclosure, the polyether polyol may be polyethylene glycol (PEG), polypropylene glycol (PPG), or polytetramethylene ether (polytetramethylene ether). Glycol, PTMEG).
根據本揭露實施例,本揭露所述組合物更包含一第二多元醇。其中,該第二多元醇與該第一多元醇不同。 According to an embodiment of the present disclosure, the composition of the present disclosure further comprises a second polyol. Wherein the second polyol is different from the first polyol.
根據本揭露實施例,該第二多元醇可為聚酯多元醇、聚醚多元醇、或C2-14之多元醇(polyol)。舉例來說,該第二多元醇可為聚(乙二醇己二酸酯)二醇(poly(ethylene adipate)diol)、聚(1,4-丁二醇己二酸酯)二醇(poly(1,4-butylene adipate)diol)、聚(乙二醇十二酸酯)二醇(poly(ethylene dodecanoate)diol)、聚(1,6-己二醇己二酸酯)二醇(poly(1,6-hexathylene adipate)diol)、聚乙二醇(polyethylene glycol,PEG)、聚丙二醇(polypropylene glycol,PPG)、聚四亞甲基醚二醇(polytetramethylene ether glycol,PTMEG)、乙二醇(ethylene glycol)、1,3-丙二醇(1,3-propylene glycol)、丙三醇(glycerol)、1,4-丁二醇(1,4-butylene glycol)、1,5-戊二醇(1,5-pentylene glycol)、新戊二醇(neo-pentylene glycol)、1,6-己二醇(1,6-hexylene glycol)、1,7-庚二醇(1,7-heptylene glycol)、1,8-辛二醇(1,8-octylene glycol)、1,9-壬二醇(1,9-nonylene glycol)、癸二醇(decylene glycol)、十一烷二醇(undecylene glycol)、十二烷二醇(dodecylene glycol)、十四烷二醇(tetradecylene glycol)、松香二醇(rosin-diol)、異山梨醇(isosorbide)、或2,5-呋喃二醇(2,5-furandiol)。根據本揭露實施例,該第二多元醇為聚酯多元醇或聚醚多元醇,且第二多元醇之數目平均分子量可為500至 100000,例如500至80000、1000至60000、2000至50000、或5000至40000。 According to an embodiment of the present disclosure, the second polyol may be a polyester polyol, a polyether polyol, or a C 2-14 polyol. For example, the second polyol may be poly(ethylene adipate) diol or poly(1,4-butanediol adipate) diol ( Poly(1,4-butylene adipate) diol, poly(ethylene dodecanoate) diol, poly(1,6-hexanediol adipate) diol ( Poly(1,6-hexathylene adipate) diol), polyethylene glycol (PEG), polypropylene glycol (PPG), polytetramethylene ether glycol (PTMEG), ethylene Ethylene glycol, 1,3-propylene glycol, glycerol, 1,4-butylene glycol, 1,5-pentanediol (1,5-pentylene glycol), neopentylene glycol, 1,6-hexylene glycol, 1,7-heptylene glycol , 1,8-octylene glycol, 1,9-nonylene glycol, decylene glycol, undecylene glycol ), dodecylene glycol, tetradecylene glycol, rosin-diol, isosorbide Isosorbide), or 2,5-furandiol. According to an embodiment of the present disclosure, the second polyol is a polyester polyol or a polyether polyol, and the number average molecular weight of the second polyol may be 500 to 100000, for example, 500 to 80,000, 1000 to 60,000, 2000 to 50000, or 5000 to 40,000.
根據本揭露實施例,該第二多元醇與該第一多元醇的重量比可為0.1至0.5(例如:0.11、0.13、0.15、0.2、0.22、0.25、0.27、或0.29),以同時提昇本揭露所述生質熱可塑性聚氨酯的機械強度、耐磨耗性、及耐水解性。 According to an embodiment of the present disclosure, the weight ratio of the second polyol to the first polyol may be 0.1 to 0.5 (for example, 0.11, 0.13, 0.15, 0.2, 0.22, 0.25, 0.27, or 0.29) to simultaneously The mechanical strength, the abrasion resistance, and the hydrolysis resistance of the biothermoplastic polyurethane of the present disclosure are improved.
根據本揭露實施例,該第一多元醇可為聚酯多元醇,以及該第二多元醇可為C2-14之多元醇(polyol);該第一多元醇可為聚酯多元醇,以及該第二多元醇可為聚醚多元醇;該第一多元醇可為聚醚多元醇,以及該第二多元醇可為C2-14之多元醇(polyol);或者,該第一多元醇可為聚醚多元醇,以及該第二多元醇可為聚酯多元醇。 According to an embodiment of the present disclosure, the first polyol may be a polyester polyol, and the second polyol may be a C 2-14 polyol; the first polyol may be a polyester polyol The alcohol, and the second polyol may be a polyether polyol; the first polyol may be a polyether polyol, and the second polyol may be a C 2-14 polyol; The first polyol may be a polyether polyol, and the second polyol may be a polyester polyol.
根據本揭露實施例,該二異氰酸酯可為二異氰酸六亞甲基酯(Hexamethylene Diisocyanate,HDI)、二異氰酸二苯甲烷(methylene diphenyl diisocyanate,MDI)、二異氰酸甲苯(toluene diisocyanate,TDI)、二異氰酸異佛爾酮(isophorone diisocyanate,IPDI)、1,5-萘基二異氰酸酯(1,5-naphthalene diisocyanate,NDI)、對-伸苯基二異氰酸酯(p-phenylene diisocyanate,PPDI)、或上述之組合。 According to an embodiment of the present disclosure, the diisocyanate may be Hexamethylene Diisocyanate (HDI), methylene diphenyl diisocyanate (MDI), toluene diisocyanate (toluene diisocyanate). , TDI), isophorone diisocyanate (IPDI), 1,5-naphthalene diisocyanate (NDI), p-phenylene diisocyanate , PPDI), or a combination of the above.
根據本揭露實施例,該組合物可包含二種或二種以上的二異氰酸酯。 According to embodiments of the present disclosure, the composition may comprise two or more diisocyanates.
根據本揭露實施例,本揭露所述改質木質素可以下 述步驟製備。首先,將木質素對鹼劑(alkali agent)反應,得到一混合物。接著,將封端劑(capping agent)加入該混合物中,反應後得到該改質木質素。 According to the disclosed embodiment, the modified lignin can be Prepare the steps. First, lignin is reacted with an alkali agent to obtain a mixture. Next, a capping agent is added to the mixture, and the modified lignin is obtained after the reaction.
值得注意的是,本揭露使用特定鹼劑,可選擇性拔除芳香羥基上的氫並保留脂族羥基(aliphatic hydroxyl)上OH的氫。因此,本揭露所述改質木質素其芳香封端劑官能基(封端劑官能基取代芳香羥基上的氫)的數量大於脂族封端劑官能基(封端劑官能基取代脂族羥基上的氫)的數量。 It is noted that the present disclosure uses a particular base agent to selectively extract hydrogen from the aromatic hydroxyl group and retain the hydrogen of the OH on the aliphatic hydroxyl. Therefore, the modified lignin has an aromatic terminal blocking agent functional group (the hydrogen of the terminal blocking agent functional group substituted for the aromatic hydroxyl group) is larger than the aliphatic terminal blocking agent functional group (the terminal blocking agent functional group replaces the aliphatic hydroxyl group) The number of hydrogen on the).
根據本揭露實施例,該鹼劑(alkali agent)可為氫氧化鈉、氫氧化鉀、碳酸銫、碳酸鉀、或上述之組合。根據本揭露實施例,該封端劑可為X-R1,其中X係為鹵素,而R1可為C1-4 烷基、苯基、、或,其中R2及R3係各自獨 立為C1-4烷基;以及,n係1、2、3或4。 According to an embodiment of the present disclosure, the alkali agent may be sodium hydroxide, potassium hydroxide, cesium carbonate, potassium carbonate, or a combination thereof. According to an embodiment of the present disclosure, the blocking agent may be XR 1 , wherein X is halogen, and R 1 may be C 1-4 alkyl, phenyl, ,or Wherein R 2 and R 3 are each independently C 1-4 alkyl; and n is 1, 2, 3 or 4.
根據本揭露實施例,本揭露所述生質熱可塑性聚氨酯的製備方式包含將上述組合物加熱反應,並進行熟成。根據本揭露實施例,本揭露所述組合物可更包含一0.01至5重量份的觸媒,該觸媒可為有機鉍觸媒、有機錫觸媒、或四級銨觸媒,其中該改質木質素與該第一多元醇的總重為100重量份。 According to an embodiment of the present disclosure, the preparation method of the biothermoplastic polyurethane of the present disclosure comprises heating the reaction of the above composition and performing aging. According to an embodiment of the present disclosure, the composition may further comprise 0.01 to 5 parts by weight of a catalyst, and the catalyst may be an organic tantalum catalyst, an organic tin catalyst, or a quaternary ammonium catalyst, wherein the modification The total weight of the lignin and the first polyol is 100 parts by weight.
為了讓本揭露之上述和其他目的、特徵、和優點能更明顯易懂,下文特舉數實施例,作詳細說明如下: The above and other objects, features, and advantages of the present invention will become more apparent and understood.
改質木質素的製備 Preparation of modified lignin
製備例1: Preparation Example 1:
將100重量份木質素(lignin,Mw:1000-1500,由稻殼萃取)加入一反應瓶中,並以丙酮溶解。充份攪拌後,將120重量份碳酸鉀(potassium carbonate)於室溫下加入該反應瓶中。接著,攪拌30分鐘後,在室溫下加入140重量份的碘甲烷(methyl iodide)於該反應瓶中,使得木質素中部份羥基轉換成甲氧基。在反應72小時後,加入大量水於該反應瓶中使得固體析出。過濾及乾燥後,得到改質木質素(1)。以核磁共振光譜計算出改質木質素(1)所殘留的羥基,結果如表1所示。 100 parts by weight of lignin (lignin, Mw: 1000-1500, extracted from rice hulls) was added to a reaction flask and dissolved in acetone. After thorough stirring, 120 parts by weight of potassium carbonate was added to the reaction flask at room temperature. Next, after stirring for 30 minutes, 140 parts by weight of methyl iodide was added to the reaction flask at room temperature to convert a part of the hydroxyl groups in the lignin to a methoxy group. After 72 hours of the reaction, a large amount of water was added to the reaction flask to precipitate a solid. After filtration and drying, modified lignin (1) is obtained. The hydroxyl groups remaining in the modified lignin (1) were calculated by nuclear magnetic resonance spectroscopy, and the results are shown in Table 1.
製備例2: Preparation Example 2:
依據製備例1所述改質木質素(1)的製備方法,除了將反應時間從72小時縮短至24小時,得到改質木質素(2)。以核磁共振光譜計算出改質木質素(2)所殘留的羥基,結果如表1所示。 According to the preparation method of the modified lignin (1) described in Preparation Example 1, except that the reaction time was shortened from 72 hours to 24 hours, modified lignin (2) was obtained. The hydroxyl groups remaining in the modified lignin (2) were calculated by nuclear magnetic resonance spectroscopy, and the results are shown in Table 1.
生質熱可塑性聚氨酯 Biomass thermoplastic polyurethane
實施例1 Example 1
將10重量份改質木質素(1)、及90重量份聚四亞甲基醚二醇(polytetramethylene ether glycol,PTMEG)(由Aldrich製造販售、數目平均分子量為1000-2000)置入一反應瓶中。在昇溫 至80℃後,真空除水一小時。在將反應瓶通入氬氣後,將13.5重量份1,4-丁二醇(1,4-butanediol)及1重量份有機鉍催化劑(由King Industries,Inc.製造及販售、商品編號為K348)加入至反應瓶。充份攪拌後,將46.68重量份二異氰酸異佛爾酮(isophorone diisocyanate、由Bayer製造及販售)加入至反應瓶,並持續攪拌。當反應瓶溫度上昇至90℃-100℃時,停止攪拌,並迅速將所得物倒入模具中,並將模具置於80℃烘箱內。烘烤16小時後,得到生質熱可塑性聚氨酯(1)。 10 parts by weight of modified lignin (1), and 90 parts by weight of polytetramethylene ether glycol (PTMEG) (sold by Aldrich, number average molecular weight 1000-2000) were placed in a reaction In the bottle. Warming up After 80 ° C, the water was removed by vacuum for one hour. After the reaction flask was purged with argon, 13.5 parts by weight of 1,4-butanediol and 1 part by weight of an organic ruthenium catalyst (manufactured and sold by King Industries, Inc., article numbered as K348) was added to the reaction flask. After thorough stirring, 46.68 parts by weight of isophorone diisocyanate (manufactured and sold by Bayer) was added to the reaction flask and stirring was continued. When the temperature of the reaction flask was raised to 90 ° C - 100 ° C, the stirring was stopped, and the resultant was quickly poured into a mold, and the mold was placed in an oven at 80 ° C. After baking for 16 hours, a biothermoplastic polyurethane (1) was obtained.
接著,將生質熱可塑性聚氨酯(1)溶於二甲基乙醯胺(dimethyl acetamide),並利用低溫烘箱烘烤成膜(烘烤溫度為60-80℃)。裁切成試片後,以萬能拉力機根據ASTM D412進行100%模數(100%modulus)、拉伸強度(tensile strength)、及拉伸伸長率(tensile elongation)的量測,結果如表2所示。 Next, the bio-thermoplastic polyurethane (1) was dissolved in dimethyl acetamide and baked into a film by a low-temperature oven (baking temperature: 60-80 ° C). After cutting into test pieces, the 100% modulus (tensile modulus), tensile strength, and tensile elongation were measured by a universal tensile machine according to ASTM D412. The results are shown in Table 2. Shown.
實施例2 Example 2
依實施例1所述生質熱可塑性聚氨酯(1)的製備方式進行,除了將改質木質素(1)由10重量份增加至20重量份、並將聚四亞甲基醚二醇由90重量份降低至80重量份,得到生質熱可塑性聚氨酯(2)。接著,將生質熱可塑性聚氨酯(2)溶於二甲基乙醯胺(dimethyl acetamide),並利用低溫烘箱烘烤成膜(烘烤溫度為60-80℃)。裁切成試片後,以萬能拉力機根據ASTM D412進行100%模數(100%modulus)、拉伸強度(tensile strength)、及拉伸伸長率(tensile elongation)的量測,結果如表2所示。 The preparation of the biothermoplastic polyurethane (1) according to Example 1 was carried out except that the modified lignin (1) was increased from 10 parts by weight to 20 parts by weight, and the polytetramethylene ether glycol was 90. The weight fraction was reduced to 80 parts by weight to obtain a biomass thermoplastic polyurethane (2). Next, the bio-thermoplastic polyurethane (2) was dissolved in dimethyl acetamide and baked into a film using a low-temperature oven (baking temperature: 60-80 ° C). After cutting into test pieces, the 100% modulus (tensile modulus), tensile strength, and tensile elongation were measured by a universal tensile machine according to ASTM D412. The results are shown in Table 2. Shown.
比較例1 Comparative example 1
將100重量份聚四亞甲基醚二醇(PTMEG)(由Aldrich製造販售、數目平均分子量為1000-2000)置入一反應瓶中。在昇溫至80℃後,真空除水一小時。在將反應瓶通入氬氣後,將13.5重量份1,4-丁二醇(1,4-butanediol)及1重量份有機鉍催化劑(由King Industries,Inc.製造及販售、商品編號為K348)加入至反應瓶。充份攪拌後,將46.68重量份二異氰酸異佛爾酮(isophorone diisocyanate、由Bayer製造及販售)加入至反應瓶,並持續攪拌。當反應瓶溫度上昇至90℃-100℃時,停止攪拌,並迅速將所得物倒入模具中,並將模具置於80℃烘箱內。烘烤16小時後,得到聚氨酯(1)。接著,將聚氨酯(1)溶於二甲基乙醯胺(dimethyl acetamide),並利用低溫烘箱烘烤成膜(烘烤溫度為60-80℃)。裁切成試片後,以萬能拉力機根據ASTM D412進行100%模數(100%modulus)、拉伸強度(tensile strength)、及拉伸伸長率(tensile elongation)的量測,結果如表2所示。 100 parts by weight of polytetramethylene ether glycol (PTMEG) (sold by Aldrich, number average molecular weight 1000-2000) was placed in a reaction flask. After warming to 80 ° C, water was removed by vacuum for one hour. After the reaction flask was purged with argon, 13.5 parts by weight of 1,4-butanediol and 1 part by weight of an organic ruthenium catalyst (manufactured and sold by King Industries, Inc., article numbered as K348) was added to the reaction flask. After thorough stirring, 46.68 parts by weight of isophorone diisocyanate (manufactured and sold by Bayer) was added to the reaction flask and stirring was continued. When the temperature of the reaction flask was raised to 90 ° C - 100 ° C, the stirring was stopped, and the resultant was quickly poured into a mold, and the mold was placed in an oven at 80 ° C. After baking for 16 hours, a polyurethane (1) was obtained. Next, the polyurethane (1) was dissolved in dimethyl acetamide, and baked into a film using a low-temperature oven (baking temperature: 60-80 ° C). After cutting into test pieces, the 100% modulus (tensile modulus), tensile strength, and tensile elongation were measured by a universal tensile machine according to ASTM D412. The results are shown in Table 2. Shown.
比較例2 Comparative example 2
依實施例2所述生質熱可塑性聚氨酯(2)的製備方式進行,除了將改質木質素(1)以改質木質素(2)取代。由於所得產物在熟成過程(90℃-100℃)即產生交聯硬化,不具熱可塑性,無法成膜。 The preparation of the biothermoplastic polyurethane (2) according to Example 2 was carried out except that the modified lignin (1) was substituted with the modified lignin (2). Since the obtained product is crosslinked and hardened during the ripening process (90 ° C - 100 ° C), it is not thermoplastic and cannot be formed into a film.
比較例3: Comparative Example 3:
依實施例2所述生質熱可塑性聚氨酯(2)的製備方式進行,除了將改質木質素(1)以未改質木質素(lignin,Mw:1000-1500,由稻殼萃取)(殘留之羥基值為6.0mmol/g)取 代。由於所得產物在熟成過程(90℃-100℃)即產生交聯硬化,不具熱可塑性,無法成膜。 The preparation method of the biothermoplastic polyurethane (2) according to Example 2 is carried out except that the modified lignin (1) is extracted from unmodified lignin (lignin, Mw: 1000-1500, from rice husk) (residue The hydroxyl value is 6.0 mmol/g) generation. Since the obtained product is crosslinked and hardened during the ripening process (90 ° C - 100 ° C), it is not thermoplastic and cannot be formed into a film.
由表2可知,與比較例1相比,添加改質木質素(1)(殘留之羥基值為2.5mmol/g)可大幅提昇所得生質熱可塑性聚氨酯的100%模數及抗拉強度。雖然,添加改質木質素(1)導致所得生質熱可塑性聚氨酯的拉伸伸長率下降,但仍維持在700%以上。 As is clear from Table 2, the addition of the modified lignin (1) (residual hydroxyl value of 2.5 mmol/g) compared with Comparative Example 1 greatly improved the 100% modulus and tensile strength of the obtained biothermoplastic polyurethane. Although the addition of the modified lignin (1) resulted in a decrease in the tensile elongation of the obtained biothermoplastic polyurethane, it was maintained at 700% or more.
抗磨耗測試 Abrasion resistance test
將比較例1所得之聚氨酯(1)及本揭露實施例2所得之生質熱可塑性聚氨酯(2)依據DIN 53516量測磨耗量(abrasion loss),結果如表3所示。 The polyurethane (1) obtained in Comparative Example 1 and the bio-thermoplastic polyurethane (2) obtained in Inventive Example 2 were measured for abrasion loss according to DIN 53516, and the results are shown in Table 3.
由表3可得知,藉由添加本揭露所述改質木質素,確實可提昇所得之生質熱可塑性聚氨酯的耐磨耗性。 As can be seen from Table 3, by adding the modified lignin of the present disclosure, the abrasion resistance of the resulting biothermoplastic polyurethane can be improved.
耐水解測試 Hydrolysis resistance test
將本揭露實施例2所得之生質熱可塑性聚氨酯(2)在80℃及95% RH進行35天耐水解測試(依據ASTM D882標準測試法),並量測生質熱可塑性聚氨酯(2)在進行耐水解測試前及後的100%模數變化率,結果如表4所示。100%模數變化率的計算方式如下:
由表4可得知,藉由添加本揭露所述改質木質素,本揭露所述之生質熱可塑性聚氨酯其具有良好的耐候性,即使在高溫高濕環境下其機械性質仍不會劣化。 It can be seen from Table 4 that by adding the modified lignin of the present disclosure, the biothermoplastic polyurethane of the present disclosure has good weather resistance, and its mechanical properties are not deteriorated even under high temperature and high humidity environment. .
雖然本揭露已以數個實施例揭露如上,然其並非用以限定本揭露,任何本技術領域中具有通常知識者,在不脫離本揭露之精神和範圍內,當可作任意之更動與潤飾,因此本揭露之保護範圍當視後附之申請專利範圍所界定者為準。 The present disclosure has been disclosed in the above several embodiments, but it is not intended to limit the disclosure, and any one skilled in the art can make any changes and refinements without departing from the spirit and scope of the disclosure. Therefore, the scope of protection of this disclosure is subject to the definition of the scope of the patent application.
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