CN101544813A - Rapid crystallization polylactic acid composite material and preparation method thereof - Google Patents
Rapid crystallization polylactic acid composite material and preparation method thereof Download PDFInfo
- Publication number
- CN101544813A CN101544813A CN200910050364A CN200910050364A CN101544813A CN 101544813 A CN101544813 A CN 101544813A CN 200910050364 A CN200910050364 A CN 200910050364A CN 200910050364 A CN200910050364 A CN 200910050364A CN 101544813 A CN101544813 A CN 101544813A
- Authority
- CN
- China
- Prior art keywords
- polylactic acid
- composite material
- parts
- rapid crystallization
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229920000747 poly(lactic acid) Polymers 0.000 title claims abstract description 64
- 239000004626 polylactic acid Substances 0.000 title claims abstract description 62
- 238000002425 crystallisation Methods 0.000 title claims abstract description 55
- 230000008025 crystallization Effects 0.000 title claims abstract description 54
- 239000002131 composite material Substances 0.000 title claims abstract description 43
- 238000002360 preparation method Methods 0.000 title abstract description 21
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 29
- 239000011707 mineral Substances 0.000 claims abstract description 25
- 229920001432 poly(L-lactide) Polymers 0.000 claims abstract description 16
- 239000000314 lubricant Substances 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 12
- 239000011159 matrix material Substances 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 4
- -1 poly(lactic acid) Polymers 0.000 claims description 22
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 claims description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 11
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 10
- 150000002148 esters Chemical class 0.000 claims description 8
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical group O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- CEGOLXSVJUTHNZ-UHFFFAOYSA-K aluminium tristearate Chemical group [Al+3].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CEGOLXSVJUTHNZ-UHFFFAOYSA-K 0.000 claims description 7
- 229940063655 aluminum stearate Drugs 0.000 claims description 7
- 239000013078 crystal Substances 0.000 claims description 7
- 239000008367 deionised water Substances 0.000 claims description 7
- 229910021641 deionized water Inorganic materials 0.000 claims description 7
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 claims description 4
- KMZHZAAOEWVPSE-UHFFFAOYSA-N 2,3-dihydroxypropyl acetate Chemical compound CC(=O)OCC(O)CO KMZHZAAOEWVPSE-UHFFFAOYSA-N 0.000 claims description 3
- 239000005995 Aluminium silicate Substances 0.000 claims description 3
- 235000012211 aluminium silicate Nutrition 0.000 claims description 3
- 239000010428 baryte Substances 0.000 claims description 3
- 229910052601 baryte Inorganic materials 0.000 claims description 3
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 3
- 239000008116 calcium stearate Substances 0.000 claims description 3
- 235000013539 calcium stearate Nutrition 0.000 claims description 3
- 230000004048 modification Effects 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 235000012424 soybean oil Nutrition 0.000 claims description 3
- 239000003549 soybean oil Substances 0.000 claims description 3
- SJECZPVISLOESU-UHFFFAOYSA-N 3-trimethoxysilylpropan-1-amine Chemical compound CO[Si](OC)(OC)CCCN SJECZPVISLOESU-UHFFFAOYSA-N 0.000 claims description 2
- FKIOYBLZUCCLTL-UHFFFAOYSA-N 4-butyl-2-tert-butyl-5-methylphenol Chemical compound CCCCC1=CC(C(C)(C)C)=C(O)C=C1C FKIOYBLZUCCLTL-UHFFFAOYSA-N 0.000 claims description 2
- 229910021532 Calcite Inorganic materials 0.000 claims description 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 claims description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-M Lactate Chemical compound CC(O)C([O-])=O JVTAAEKCZFNVCJ-UHFFFAOYSA-M 0.000 claims description 2
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims description 2
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 claims description 2
- NKSJNEHGWDZZQF-UHFFFAOYSA-N ethenyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C=C NKSJNEHGWDZZQF-UHFFFAOYSA-N 0.000 claims description 2
- 235000011187 glycerol Nutrition 0.000 claims description 2
- JJTUDXZGHPGLLC-UHFFFAOYSA-N lactide Chemical compound CC1OC(=O)C(C)OC1=O JJTUDXZGHPGLLC-UHFFFAOYSA-N 0.000 claims description 2
- 239000010445 mica Substances 0.000 claims description 2
- 229910052618 mica group Inorganic materials 0.000 claims description 2
- 239000002480 mineral oil Substances 0.000 claims description 2
- 235000010446 mineral oil Nutrition 0.000 claims description 2
- MQWFLKHKWJMCEN-UHFFFAOYSA-N n'-[3-[dimethoxy(methyl)silyl]propyl]ethane-1,2-diamine Chemical compound CO[Si](C)(OC)CCCNCCN MQWFLKHKWJMCEN-UHFFFAOYSA-N 0.000 claims description 2
- 238000010992 reflux Methods 0.000 claims description 2
- 238000000967 suction filtration Methods 0.000 claims description 2
- DQZNLOXENNXVAD-UHFFFAOYSA-N trimethoxy-[2-(7-oxabicyclo[4.1.0]heptan-4-yl)ethyl]silane Chemical compound C1C(CC[Si](OC)(OC)OC)CCC2OC21 DQZNLOXENNXVAD-UHFFFAOYSA-N 0.000 claims description 2
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 claims description 2
- 239000010455 vermiculite Substances 0.000 claims description 2
- 229910052902 vermiculite Inorganic materials 0.000 claims description 2
- 235000019354 vermiculite Nutrition 0.000 claims description 2
- 239000010456 wollastonite Substances 0.000 claims description 2
- 229910052882 wollastonite Inorganic materials 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims 3
- 239000003112 inhibitor Substances 0.000 claims 3
- 230000003647 oxidation Effects 0.000 claims 3
- 238000007254 oxidation reaction Methods 0.000 claims 3
- 239000003381 stabilizer Substances 0.000 claims 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims 2
- 239000004593 Epoxy Substances 0.000 claims 1
- UYXTWWCETRIEDR-UHFFFAOYSA-N Tributyrin Chemical compound CCCC(=O)OCC(OC(=O)CCC)COC(=O)CCC UYXTWWCETRIEDR-UHFFFAOYSA-N 0.000 claims 1
- 150000001412 amines Chemical class 0.000 claims 1
- 150000002632 lipids Chemical class 0.000 claims 1
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 claims 1
- GLDOVTGHNKAZLK-UHFFFAOYSA-N n-octadecyl alcohol Natural products CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 claims 1
- 238000005453 pelletization Methods 0.000 claims 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical group OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 claims 1
- 229960003742 phenol Drugs 0.000 claims 1
- 235000019260 propionic acid Nutrition 0.000 claims 1
- 229910000077 silane Inorganic materials 0.000 claims 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims 1
- 229920002554 vinyl polymer Polymers 0.000 claims 1
- 239000002667 nucleating agent Substances 0.000 abstract description 9
- 239000012760 heat stabilizer Substances 0.000 abstract description 8
- 239000008187 granular material Substances 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 230000002195 synergetic effect Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract description 2
- 239000000945 filler Substances 0.000 abstract 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 12
- 239000003963 antioxidant agent Substances 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 6
- HQYALQRYBUJWDH-UHFFFAOYSA-N trimethoxy(propyl)silane Chemical compound CCC[Si](OC)(OC)OC HQYALQRYBUJWDH-UHFFFAOYSA-N 0.000 description 6
- 230000003078 antioxidant effect Effects 0.000 description 5
- 239000007822 coupling agent Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- UAUDZVJPLUQNMU-UHFFFAOYSA-N Erucasaeureamid Natural products CCCCCCCCC=CCCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-UHFFFAOYSA-N 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- QZCLKYGREBVARF-UHFFFAOYSA-N Acetyl tributyl citrate Chemical compound CCCCOC(=O)CC(C(=O)OCCCC)(OC(C)=O)CC(=O)OCCCC QZCLKYGREBVARF-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical compound C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 238000002715 modification method Methods 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical group CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- 239000003017 thermal stabilizer Substances 0.000 description 2
- OXDXXMDEEFOVHR-CLFAGFIQSA-N (z)-n-[2-[[(z)-octadec-9-enoyl]amino]ethyl]octadec-9-enamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)NCCNC(=O)CCCCCCC\C=C/CCCCCCCC OXDXXMDEEFOVHR-CLFAGFIQSA-N 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229920002988 biodegradable polymer Polymers 0.000 description 1
- 239000004621 biodegradable polymer Substances 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 238000004177 carbon cycle Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 229920006238 degradable plastic Polymers 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- WOXXJEVNDJOOLV-UHFFFAOYSA-N ethenyl-tris(2-methoxyethoxy)silane Chemical compound COCCO[Si](OCCOC)(OCCOC)C=C WOXXJEVNDJOOLV-UHFFFAOYSA-N 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- RIEABXYBQSLTFR-UHFFFAOYSA-N monobutyrin Chemical compound CCCC(=O)OCC(O)CO RIEABXYBQSLTFR-UHFFFAOYSA-N 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- YTXCAJNHPVBVDJ-UHFFFAOYSA-N octadecyl propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CC YTXCAJNHPVBVDJ-UHFFFAOYSA-N 0.000 description 1
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 description 1
- FATBGEAMYMYZAF-UHFFFAOYSA-N oleicacidamide-heptaglycolether Natural products CCCCCCCCC=CCCCCCCCC(N)=O FATBGEAMYMYZAF-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical group 0.000 description 1
- 230000029553 photosynthesis Effects 0.000 description 1
- 238000010672 photosynthesis Methods 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 235000012222 talc Nutrition 0.000 description 1
- 229910052623 talc Inorganic materials 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
- 238000002834 transmittance Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
本发明涉及一种快速结晶聚乳酸复合材料及其制备技术。该复合材料的组成以重量份计为:半结晶型聚L-乳酸59~98份,有机改性天然矿物1~40份,有机结晶促进剂1~20份,热稳定剂0.1~1.0份,润滑剂0.05~1.0份,以上各组分的质量百分比之和为100%。该材料的制备方法:首先制备改性天然矿物,然后按复合材料的组成进行配料,高搅机搅拌混合均匀,将共混物放入双螺杆挤出机中挤出造粒。本发明通过有机化的矿物与结晶促进剂的协同作用提高了聚乳酸基体的结晶速率。在加快聚乳酸结晶速率的同时,由于有机结晶促进剂的加入还可以对聚乳酸复合材料的力学性能有所增强,避免了单一无机矿物成核剂的加入导致聚乳酸基复合材料力学性能大幅度下降的缺陷。本发明采用的填料价格低、整个制备方法工艺流程简单、工艺流程耗时少,可实现大规模工业化生产。The invention relates to a rapid crystallization polylactic acid composite material and its preparation technology. The composition of the composite material is calculated in parts by weight: 59-98 parts of semi-crystalline poly-L-lactic acid, 1-40 parts of organically modified natural minerals, 1-20 parts of organic crystallization accelerator, 0.1-1.0 parts of heat stabilizer, 0.05-1.0 parts of lubricant, the sum of the mass percentages of the above components is 100%. The preparation method of the material: firstly prepare the modified natural mineral, then carry out batching according to the composition of the composite material, stir and mix evenly with a high mixer, put the blend into a twin-screw extruder to extrude and granulate. The invention improves the crystallization rate of the polylactic acid matrix through the synergistic effect of the organic mineral and the crystallization accelerator. While accelerating the crystallization rate of polylactic acid, the addition of organic crystallization accelerators can also enhance the mechanical properties of polylactic acid composites, avoiding the significant increase in the mechanical properties of polylactic acid-based composites due to the addition of a single inorganic mineral nucleating agent. Falling flaws. The filler used in the invention has low price, simple process flow of the whole preparation method, less time-consuming process flow, and large-scale industrial production can be realized.
Description
技术领域 technical field
本发明涉及一种改性聚乳酸复合材料及其制备方法,特别是一种快速结晶聚乳酸复合材料及其制备方法。The invention relates to a modified polylactic acid composite material and a preparation method thereof, in particular to a rapidly crystallizing polylactic acid composite material and a preparation method thereof.
背景技术 Background technique
随着全球经济不断发展,工农业对石油资源消耗不断增加。同时,各种依赖石油的不可降解塑料用量却在不断增加,造成严重的白色污染,给社会可持续发展带来巨大挑战。在我国,难以回收的一次性塑料制品占我国塑料总量的20%,产生的塑料垃圾每年达400万吨。这些塑料垃圾对环境造成严重破坏,致使粮食减产,海洋生物死亡,水力发电受到破坏,温室效应加剧等。解决白色污染是当前世界各国面临的重大科学与技术问题、环境和经济问题,甚至是政治问题。With the continuous development of the global economy, the consumption of petroleum resources by industry and agriculture continues to increase. At the same time, the amount of non-degradable plastics that rely on petroleum is increasing, causing serious white pollution and posing a huge challenge to the sustainable development of society. In my country, disposable plastic products that are difficult to recycle account for 20% of the total plastic in my country, and the plastic waste generated reaches 4 million tons every year. These plastic wastes have caused serious damage to the environment, resulting in reduced food production, the death of marine life, damage to hydroelectric power generation, and increased greenhouse effect. Solving white pollution is a major scientific and technological issue, environmental and economic issue, and even political issue facing countries all over the world.
聚乳酸是一种以可再生植物资源为原料经过化学合成制备的生物降解高分子材料,其原料乳酸是从玉米等可再生天然物质中发酵制取,摆脱了对石油资源的依赖,其生产过程造成的环境污染小,且具有良好的生物降解性,降解产生的二氧化碳和水可以返回自然界,重新参加植物的光合作用,从而维持自然界的碳循环平衡,满足可持续发展的要求,另外,聚乳酸的力学强度,加工性,防渗透性,光泽度和透光度与聚丙稀和聚苯乙烯相似,目前已经研发出注塑级、薄膜级、片材级、纤维级、医用级等不同工业用途的聚乳酸,其市场需求量巨大。Polylactic acid is a biodegradable polymer material prepared by chemical synthesis using renewable plant resources as raw materials. The raw material lactic acid is fermented from renewable natural materials such as corn. It causes little environmental pollution and has good biodegradability. The carbon dioxide and water produced by degradation can return to nature and re-participate in the photosynthesis of plants, thereby maintaining the carbon cycle balance in nature and meeting the requirements of sustainable development. In addition, polylactic acid The mechanical strength, processability, impermeability, gloss and light transmittance are similar to polypropylene and polystyrene. At present, injection molding grade, film grade, sheet grade, fiber grade, medical grade and other industrial grades have been developed. Polylactic acid has a huge market demand.
当前制约聚乳酸实际应用的主要瓶颈是成型加工周期长。由于聚乳酸结晶速率慢使其成型时间过长,导致工艺条件复杂,能耗增加,最终使生产成本提高,提高聚乳酸的结晶速率是缩短成型周期的有效办法。因此,提高聚乳酸结晶速率对于解决聚乳酸的应用问题具有重要的应用价值。The main bottleneck restricting the practical application of polylactic acid at present is the long molding cycle. Due to the slow crystallization rate of polylactic acid, the molding time is too long, resulting in complex process conditions, increased energy consumption, and ultimately increased production costs. Improving the crystallization rate of polylactic acid is an effective way to shorten the molding cycle. Therefore, improving the crystallization rate of polylactic acid has important application value for solving the application problems of polylactic acid.
目前,提高聚乳酸结晶速率的有效办法是加入结晶成核剂,成核剂能降低成核的表面自由能垒,因而加快树脂基体的结晶速率。专利JP1999-106628使用蜡作为聚乳酸结晶成核剂,然而,该结晶成核剂与聚乳酸相容性不好,容易析出,导致实际添加量减少,晶核形成不充分。专利US6417294通过添加脂肪族羧酸胺、脂肪族羧酸盐、脂肪醇及脂肪族羧酸脂等复合成核剂到聚乳酸基体中,获得具有透明性及结晶性的聚乳酸产品。但是由于成核剂为小分子量的有机化合物,与聚乳酸制成母料或产品后容易逸出。滑石粉是一种广泛使用的成核剂,专利JP1997-25345A添加质量分数为15%MWHS-T滑石粉作为结晶成核剂(平均粒径2.75μm),再添加质量分数为1%的芥酰胺,其熔融热焓与结晶热焓绝对值之差达到了25Jg-1以上,用XRD测定制品结晶度大于35%,130℃以下的半结晶时间低于20min。At present, an effective way to increase the crystallization rate of polylactic acid is to add a crystallization nucleating agent, which can reduce the surface free energy barrier for nucleation, thereby accelerating the crystallization rate of the resin matrix. Patent JP1999-106628 uses wax as polylactic acid crystallization nucleating agent. However, the crystallization nucleating agent has poor compatibility with polylactic acid and is easy to precipitate, resulting in a decrease in actual addition amount and insufficient crystal nucleus formation. Patent US6417294 obtains polylactic acid products with transparency and crystallinity by adding complex nucleating agents such as aliphatic carboxylic acid amines, aliphatic carboxylate salts, fatty alcohols and aliphatic carboxylic acid esters to the polylactic acid matrix. However, since the nucleating agent is an organic compound with a small molecular weight, it is easy to escape after being made into a masterbatch or product with polylactic acid. Talc powder is a widely used nucleating agent. Patent JP1997-25345A adds 15% MWHS-T talcum powder as a crystallization nucleating agent (average particle size 2.75 μm), and then adds erucamide with a mass fraction of 1%. , the difference between the absolute value of the melting enthalpy and the crystallization enthalpy is above 25Jg -1 , the crystallinity of the product measured by XRD is greater than 35%, and the half-crystallization time below 130°C is less than 20min.
发明内容 Contents of the invention
本发明的目的之一在于克服现有技术中聚乳酸结晶速率慢的缺陷,通过有机改性的天然矿物与结晶促进剂的协同作用改善聚乳酸基体的结晶速率,从而获得一种快速结晶聚乳酸复合材料。One of the purposes of the present invention is to overcome the defects of slow crystallization rate of polylactic acid in the prior art, and improve the crystallization rate of the polylactic acid matrix through the synergistic effect of organically modified natural minerals and crystallization accelerators, thereby obtaining a fast crystallization polylactic acid composite material.
本发明的目的之二在于提供该复合材料的制备方法。The second object of the present invention is to provide a preparation method of the composite material.
为实现上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种快速结晶聚乳酸复合材料,其特征在于该复合材料的组成和质量百分比含量为:A kind of rapid crystallization polylactic acid composite material is characterized in that the composition and mass percentage content of this composite material are:
半结晶型聚L-乳酸 59~98%Semi-crystalline poly-L-lactic acid 59~98%
有机改性天然矿物 1~40%Organic modified natural minerals 1~40%
有机结晶促进剂 0.5~20%Organic crystallization accelerator 0.5~20%
热稳定剂 0.1~1.0%Heat stabilizer 0.1~1.0%
润滑剂 0.05~1.0%Lubricant 0.05~1.0%
抗氧剂 0.2~1.5%Antioxidant 0.2~1.5%
以上各组分的质量百分比之和为100%;其中所述的半结晶型聚L-乳酸为左旋聚乳酸,其中内消旋聚L-乳酸的含量低于5wt%,聚乳酸的粘均分子量为10~30万。The sum of the mass percentages of the above components is 100%; wherein the semi-crystalline poly-L-lactic acid is L-polylactic acid, wherein the content of mesogenic poly-L-lactic acid is lower than 5wt%, and the viscosity-average molecular weight of polylactic acid is 100,000 to 300,000.
上述的天然矿物为:重晶石、硅灰石、云母、滑石粉、蛭石、蒙脱土、高岭土、方解石或蛇纹石。The aforementioned natural minerals are: barite, wollastonite, mica, talc, vermiculite, montmorillonite, kaolin, calcite or serpentine.
上述有机改性天然矿物的具体改性方法为:按重量份计,将天然矿物5~20份,80%~95%乙醇水溶液75~94份,硅烷偶联剂1~5份,0.1mol/L浓盐酸0.01~0.05份进行配料,在70~90℃下进行搅拌混合,再回流3~5小时;经抽滤,去离子水洗涤后,在100~105℃下烘干,即得到改性天然矿物。The specific modification method of the above-mentioned organically modified natural minerals is as follows: in parts by weight, 5 to 20 parts of natural minerals, 75 to 94 parts of 80% to 95% ethanol aqueous solution, 1 to 5 parts of silane coupling agent, 0.1mol/ 0.01-0.05 part of L concentrated hydrochloric acid is mixed, stirred and mixed at 70-90°C, and then refluxed for 3-5 hours; after suction filtration, deionized water washing, drying at 100-105°C, the modified natural minerals.
上述的硅烷偶联剂是3-(2-氨乙基)-氨丙基甲基二甲氧基硅烷、γ-缩水甘油醚丙基三甲氧基硅烷、γ-氨基丙基三乙基硅氧烷、乙烯基三甲氧基硅烷、乙烯基三(β-甲氧乙氧基)硅烷、乙烯基三乙氧基硅烷、β-(3、4-环氧环己基)乙基三甲氧基硅烷中的至少一种。The above-mentioned silane coupling agents are 3-(2-aminoethyl)-aminopropylmethyldimethoxysilane, γ-glycidyl ether propyltrimethoxysilane, γ-aminopropyltriethylsiloxane alkane, vinyltrimethoxysilane, vinyltris(β-methoxyethoxy)silane, vinyltriethoxysilane, β-(3,4-epoxycyclohexyl)ethyltrimethoxysilane at least one of .
上述的有机改性天然矿物的具体改性方法为:将粒径小于150目的天然矿物95~99份,改性剂1~5份在高速碰撞机中进行混合,混合温度在80℃以上,混合30~90分钟,得到干法改性天然矿物;所述的改性剂为硬酯酸、氨丙基三甲氧基硅烷或单烷氧基脂肪酸钛酸酯;高速碰撞机为高速混合机、粉碎机或球磨机。The specific modification method of the above-mentioned organically modified natural minerals is as follows: mix 95-99 parts of natural minerals with a particle size of less than 150 mesh, and 1-5 parts of modifiers in a high-speed collision machine, and the mixing temperature is above 80°C. 30 to 90 minutes to obtain dry modified natural minerals; the modifier is stearic acid, aminopropyltrimethoxysilane or monoalkoxy fatty acid titanate; the high-speed collision machine is a high-speed mixer, pulverizer machine or ball mill.
上述有机结晶促进剂为:乙撑双硬酸酯酰胺、芥酸酰胺、油酸酰胺、乙撑双油酸酰胺、邻苯二甲酸酯、柠檬酸酯、乳酸酯、丙交酯、矿物油、磷酸三苯酯、甘油、乙酸甘油酯或丁酸甘油酯。The above organic crystallization accelerators are: ethylene bisstearamide, erucamide, oleamide, ethylene bisoleamide, phthalate, citrate, lactate, lactide, mineral Oil, Triphenyl Phosphate, Glycerin, Glyceryl Acetate, or Glyceryl Butyrate.
上述的抗氧剂为四季戊四醇酯、丙酸十八醇酯或1,1,3三(2-甲基-4-羟基-5叔丁基苯基)丁烷;热稳定剂是顺丁烯二酸酐或环氧大豆油;润滑剂为硬脂酸铝或硬酯酸钙。The above-mentioned antioxidant is tetraerythritol ester, stearyl propionate or 1,1,3 three (2-methyl-4-hydroxyl-5 tert-butylphenyl) butane; heat stabilizer is butene dianhydride or epoxidized soybean oil; lubricants are aluminum stearate or calcium stearate.
一种制备上述的快速结晶聚乳酸复合材料的方法,其特征在于该方法的具体步骤如下:按上述配比将半结晶型聚L-乳酸、有机改性天然矿物、有机结晶促进剂、热稳定剂、润滑剂和抗氧剂进行混合,混合后搅拌均匀;再进行挤出造粒,即得到快速结晶聚乳酸复合材料A method for preparing the above-mentioned rapid crystallization polylactic acid composite material is characterized in that the specific steps of the method are as follows: semi-crystalline poly-L-lactic acid, organically modified natural minerals, organic crystallization accelerator, thermally stable Mixing agent, lubricant and antioxidant, stirring evenly after mixing; then extruding and granulating to obtain rapid crystallization polylactic acid composite material
所述的聚乳酸为结晶度高于20%的半结晶型左旋聚乳酸,其中内消旋聚L-乳酸的含量低于5wt%,聚乳酸的粘均分子量为10~30万,玻璃化转变温度范围为40~60℃,熔体流动速率在190℃×2.16Kg为4~15g/10min。The polylactic acid is a semi-crystalline L-lactic acid with a crystallinity higher than 20%, wherein the content of mesogenic poly-L-lactic acid is less than 5wt%, the viscosity-average molecular weight of the polylactic acid is 100,000-300,000, and the glass transition The temperature range is 40-60°C, and the melt flow rate is 4-15g/10min at 190°C×2.16Kg.
与现有技术相比,本发明的优点是:Compared with prior art, the advantage of the present invention is:
(1)本发明选用无机矿物与有机结晶促进剂的协同作用来提高聚乳酸的结晶速率,获得的聚乳酸复合材料显著提高了聚乳酸基体的结晶速率。(1) The present invention uses the synergistic effect of inorganic minerals and organic crystallization accelerators to increase the crystallization rate of polylactic acid, and the obtained polylactic acid composite material significantly improves the crystallization rate of the polylactic acid matrix.
(2)本发明由于添加有机结晶促进剂不仅可以加快聚乳酸的结晶速率,并且对聚乳酸复合材料的力学性能有所提高,避免了单一无机矿物成核剂的加入导致复合材料力学性能下降的缺陷。(2) The present invention can not only accelerate the crystallization rate of polylactic acid owing to adding organic crystallization accelerator, and the mechanical property of polylactic acid composite material is improved, has avoided the addition of single inorganic mineral nucleating agent and causes the decline of composite material mechanical property defect.
(3)本发明采用的矿物价格低,且在复合材料中的含量可高达15wt%而不影响聚乳酸复合材料的力学性能,大大降低了制品的成本。(3) The mineral used in the present invention is low in price, and its content in the composite material can be as high as 15 wt% without affecting the mechanical properties of the polylactic acid composite material, which greatly reduces the cost of the product.
(4)本发明注塑级快速结晶聚乳酸基复合材料的制备技术,工艺流程简单,加工性能强,成本低可实现大规模的工业化生产。(4) The preparation technology of the injection molding grade rapid crystallization polylactic acid-based composite material of the present invention has simple process flow, strong processability, low cost and large-scale industrial production.
具体实施方式 Detailed ways
下面结合实施例对本发明进行详细描述。The present invention will be described in detail below in conjunction with the examples.
在聚乳酸的稳定体系中,主要防止其热降解,因此常常加入热稳定剂,如顺丁烯二酸酐或环氧大豆油。In the stabilization system of polylactic acid, it is mainly to prevent its thermal degradation, so a thermal stabilizer, such as maleic anhydride or epoxidized soybean oil, is often added.
为了进一步增强天然矿物与聚乳酸基体之间的相容性,通常需用偶联剂对天然矿物进行表面处理。所用的偶联剂是一些含有活性官能团的低分子化合物,如硅烷偶联剂、钛酸酯偶联剂、铝酸酯偶联剂等。In order to further enhance the compatibility between natural minerals and PLA matrix, it is usually necessary to use a coupling agent to treat the surface of natural minerals. The coupling agents used are low-molecular compounds containing active functional groups, such as silane coupling agents, titanate coupling agents, aluminate coupling agents, and the like.
实施例一:纯聚乳酸的制备Embodiment one: the preparation of pure polylactic acid
真空干燥的聚乳酸(重均分子量19.5W)100份在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测。其结晶速率和力学性能见表1。100 parts of vacuum-dried polylactic acid (weight-average molecular weight 19.5W) is mixed in a high-speed mixer at room temperature, extruded and granulated in a twin-screw extruder, and the extrusion temperature is 160-185 ° C, and then the composite material particles are injected into impact and tensile splines, to be tested. Its crystallization rate and mechanical properties are listed in Table 1.
实施例二:改性滑石粉/乙撑双硬酸酯酰胺/聚乳酸复合材料的制备方法Embodiment two: the preparation method of modified talcum powder/ethylene bis stearate amide/polylactic acid composite material
改性滑石粉的制备工艺:按重量份计,将滑石粉15份,95%乙醇水溶液84份,硅烷偶联剂γ-缩水甘油醚丙基三甲氧基硅烷1份,0.1mol/L浓盐酸0.03份进行配料,在85℃下进行搅拌混合,再回流3小时;经抽滤,去离子水洗涤后,在105℃下烘干。The preparation process of modified talcum powder: by weight, 15 parts of talcum powder, 84 parts of 95% ethanol aqueous solution, 1 part of silane coupling agent γ-glycidyl ether propyl trimethoxysilane, 0.1mol/L concentrated hydrochloric acid 0.03 parts were batched, stirred and mixed at 85°C, and then refluxed for 3 hours; filtered by suction, washed with deionized water, and dried at 105°C.
真空干燥的半结晶型聚L-乳酸(重均分子量19.5W)81份、改性滑石粉15份、乙撑双硬酸酯酰胺3份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸铝0.3份在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测。其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly L-lactic acid (weight average molecular weight 19.5W) 81 parts, modified talc powder 15 parts, ethylene bis stearate amide 3 parts, heat stabilizer maleic anhydride 0.2 parts, antioxidant 0.5 part of pentaerythritol ester of agent and 0.3 part of lubricant aluminum stearate were mixed in a high-speed blender at room temperature, extruded and granulated in a twin-screw extruder, and the extrusion temperature was 160-185 ° C, and then the composite material particles Injection molded into impact and tensile splines, to be tested. Its crystallization rate and mechanical properties are listed in Table 1.
实施例三:改性滑石粉/芥酸酰胺/聚乳酸复合材料的制备方法Example 3: Preparation method of modified talcum powder/erucamide/polylactic acid composite material
改性滑石粉的制备工艺:将粒径小于150目的滑石粉97份,硬酯酸3份在高速搅拌机中进行混合,混合温度在80℃以上,混合40min,得到干法改性滑石粉。The preparation process of modified talc powder: Mix 97 parts of talc powder with a particle size of less than 150 mesh and 3 parts of stearic acid in a high-speed mixer at a mixing temperature above 80°C for 40 minutes to obtain a dry-process modified talc powder.
真空干燥的半结晶型聚L-乳酸(重均分子量19.5W)86份、改性滑石粉10份、乙撑双硬酸酯酰胺3份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸铝0.3在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测。其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly L-lactic acid (weight average molecular weight 19.5W) 86 parts, modified talc powder 10 parts, ethylene bis stearate amide 3 parts, heat stabilizer maleic anhydride 0.2 parts, antioxidant Agent tetraerythritol ester 0.5 part, lubricant aluminum stearate 0.3 are mixed at room temperature in a high-speed mixer, extruded and granulated in a twin-screw extruder, the extrusion temperature is 160-185 ° C, and then the composite material particles are injected into impact and tensile splines, to be tested. Its crystallization rate and mechanical properties are listed in Table 1.
实施例四:改性高岭土/乙撑双硬酸酯酰胺/聚乳酸复合材料的制备方法Embodiment four: the preparation method of modified kaolin/ethylene bisstearamide/polylactic acid composite material
改性高岭土的制备工艺:按重量份计,将高岭土15份,95%乙醇水溶液84份,硅烷偶联剂γ-缩水甘油醚丙基三甲氧基硅烷1份,0.1mol/L浓盐酸0.03份进行配料,在85℃下进行搅拌混合,再回流3小时;经抽滤,去离子水洗涤后,在105℃下烘干。The preparation process of modified kaolin: by weight, 15 parts of kaolin, 84 parts of 95% ethanol aqueous solution, 1 part of silane coupling agent γ-glycidyl ether propyl trimethoxysilane, 0.03 part of 0.1mol/L concentrated hydrochloric acid Perform batching, stir and mix at 85°C, and then reflux for 3 hours; filter with suction, wash with deionized water, and dry at 105°C.
真空干燥的半结晶型聚L-乳酸(重均分子量19.5W)89份、改性高岭土6份、乙撑双硬酸酯酰胺4份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸钙0.3份在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测。其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly-L-lactic acid (weight average molecular weight 19.5W) 89 parts, modified kaolin 6 parts, ethylene bis stearate amide 4 parts, heat stabilizer maleic anhydride 0.2 parts, antioxidant Mix 0.5 parts of tetraerythritol ester and 0.3 parts of lubricant calcium stearate at room temperature in a high-speed mixer, extrude and granulate in a twin-screw extruder at a temperature of 160-185°C, and then inject the composite material particles into impact and tensile splines, to be tested. Its crystallization rate and mechanical properties are listed in Table 1.
实施例五:改性滑石粉/乙酰柠檬酸三正丁酯/聚乳酸复合材料的制备方法Embodiment five: the preparation method of modified talcum powder/acetyl tri-n-butyl citrate/polylactic acid composite material
改性滑石粉的制备工艺:按重量份计,将滑石粉15份,95%乙醇水溶液84份,硅烷偶联剂γ-缩水甘油醚丙基三甲氧基硅烷1份,0.1mol/L浓盐酸0.03份进行配料,在85℃下进行搅拌混合,再回流3小时;经抽滤,去离子水洗涤后,在105℃下烘干。The preparation process of modified talcum powder: by weight, 15 parts of talcum powder, 84 parts of 95% ethanol aqueous solution, 1 part of silane coupling agent γ-glycidyl ether propyl trimethoxysilane, 0.1mol/L concentrated hydrochloric acid 0.03 parts were batched, stirred and mixed at 85°C, and then refluxed for 3 hours; filtered by suction, washed with deionized water, and dried at 105°C.
真空干燥的半结晶型聚L-乳酸(重均分子量19.5W)74份、改性滑石粉10份、乙酰柠檬酸三正丁酯15份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸铝0.3在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测,其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly L-lactic acid (weight average molecular weight 19.5W) 74 parts, modified talc powder 10 parts, acetyl tri-n-butyl citrate 15 parts, heat stabilizer maleic anhydride 0.2 parts, antioxidant Agent tetraerythritol ester 0.5 part, lubricant aluminum stearate 0.3 are mixed at room temperature in a high-speed mixer, extruded and granulated in a twin-screw extruder, the extrusion temperature is 160-185 ° C, and then the composite material particles are injected into impact and tensile splines to be tested, and their crystallization rate and mechanical properties are shown in Table 1.
实施例六:改性重晶石/乙撑双硬酸酯酰胺/聚乳酸复合材料的制备方法Embodiment 6: Preparation method of modified barite/ethylene bisstearate amide/polylactic acid composite material
改性重晶石的制备工艺:按重量份计,将重晶石15份,95%乙醇水溶液84份,硅烷偶联剂γ-缩水甘油醚丙基三甲氧基硅烷1份,0.1mol/L浓盐酸0.03份进行配料,在85℃下进行搅拌混合,再回流3小时;经抽滤,去离子水洗涤后,在105℃下烘干。The preparation process of modified barite: by weight, 15 parts of barite, 84 parts of 95% ethanol aqueous solution, 1 part of silane coupling agent γ-glycidyl ether propyl trimethoxysilane, 0.1mol/L 0.03 part of concentrated hydrochloric acid is used for batching, stirred and mixed at 85°C, and then refluxed for 3 hours; filtered with suction, washed with deionized water, and dried at 105°C.
真空干燥的半结晶型聚L-乳酸(重均分子量19.5W)89份、改性重晶石5份、乙撑双硬酸酯酰胺5份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸铝0.3份在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测,其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly L-lactic acid (weight average molecular weight 19.5W) 89 parts, modified barite 5 parts, ethylene bis stearate amide 5 parts, heat stabilizer maleic anhydride 0.2 parts, anti Mix 0.5 parts of tetraerythritol ester of oxygen agent and 0.3 parts of aluminum stearate of lubricant in a high-speed blender at room temperature, extrude and granulate in a twin-screw extruder, and the extrusion temperature is 160-185 ° C, and then the composite material The particles were injection molded into impact and tensile splines to be tested. The crystallization rate and mechanical properties are shown in Table 1.
实施例七:改性滑石粉/乙撑双硬酸酯酰胺/聚乳酸复合材料的制备方法Embodiment 7: the preparation method of modified talcum powder/ethylene bis stearate amide/polylactic acid composite material
改性滑石粉的制备工艺:按重量份计,将滑石粉15份,95%乙醇水溶液84份,硅烷偶联剂γ-缩水甘油醚丙基三甲氧基硅烷1份,0.1mol/L浓盐酸0.03份进行配料,在85℃下进行搅拌混合,再回流3小时;经抽滤,去离子水洗涤后,在105℃下烘干。The preparation process of modified talcum powder: by weight, 15 parts of talcum powder, 84 parts of 95% ethanol aqueous solution, 1 part of silane coupling agent γ-glycidyl ether propyl trimethoxysilane, 0.1mol/L concentrated hydrochloric acid 0.03 parts were batched, stirred and mixed at 85°C, and then refluxed for 3 hours; filtered by suction, washed with deionized water, and dried at 105°C.
真空干燥的半结晶型聚L-乳酸88份(重均分子量为12.87W)、改性滑石粉10份、乙撑双硬酸酯酰胺1份、热稳定剂顺丁烯二酸酐0.2份、抗氧剂四季戊四醇酯0.5份、润滑剂硬脂酸铝0.3份在高搅机中常温混匀,在双螺杆挤出机中挤出造粒,挤出温度为160-185℃,然后将复合材料粒子注塑成冲击、拉伸样条,待测,其结晶速率和力学性能见表1。Vacuum-dried semi-crystalline poly L-lactic acid 88 parts (weight average molecular weight is 12.87W), modified talcum powder 10 parts, ethylene bis stearate amide 1 part, thermal stabilizer maleic anhydride 0.2 part, anti- Mix 0.5 parts of tetraerythritol ester of oxygen agent and 0.3 parts of aluminum stearate of lubricant in a high-speed blender at room temperature, extrude and granulate in a twin-screw extruder, and the extrusion temperature is 160-185 ° C, and then the composite material The particles were injection molded into impact and tensile splines to be tested. The crystallization rate and mechanical properties are shown in Table 1.
表1:实施例1~7所制备的聚乳酸组合物的性能Table 1: Properties of the polylactic acid composition prepared in Examples 1-7
从表中可以看出,该发明所制备的无机矿物/有机结晶促进剂协同作用下的快速结晶型聚乳酸基复合材料与纯聚乳酸相比,具有结晶速率快和良好的力学性能,尤其是其快速结晶性能显著缩短聚乳酸的加工成型周期,提高生产效率,降低生产成本,上述对实例的描述是为了便于该技术领域的普通技术人员能理解和应用本发明。熟悉本领域的技术人员可以容易的对这些实施实例做出各种修改,并把在此说明的一般性原理应用在其它应用实例中而不必经过创造性的劳动。因此,本发明不限于这里的实施实例,本领域技术人员根据本发明的揭示,对本发明做出的改进和修改都应该在本发明的保护范围之内。As can be seen from the table, compared with pure polylactic acid, the rapid crystallization type polylactic acid-based composite material prepared by the invention under the synergistic effect of inorganic mineral/organic crystallization accelerator has fast crystallization rate and good mechanical properties, especially Its rapid crystallization performance significantly shortens the processing and molding cycle of polylactic acid, improves production efficiency, and reduces production costs. The above description of the examples is to facilitate the understanding and application of the present invention by those of ordinary skill in the technical field. Those skilled in the art can easily make various modifications to these implementation examples, and apply the general principles described here to other application examples without creative efforts. Therefore, the present invention is not limited to the implementation examples here, and the improvements and modifications made by those skilled in the art according to the disclosure of the present invention should be within the protection scope of the present invention.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200910050364 CN101544813B (en) | 2009-04-30 | 2009-04-30 | Rapid crystallization polylactic acid composite material and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200910050364 CN101544813B (en) | 2009-04-30 | 2009-04-30 | Rapid crystallization polylactic acid composite material and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101544813A true CN101544813A (en) | 2009-09-30 |
CN101544813B CN101544813B (en) | 2012-12-19 |
Family
ID=41192203
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200910050364 Expired - Fee Related CN101544813B (en) | 2009-04-30 | 2009-04-30 | Rapid crystallization polylactic acid composite material and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101544813B (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101857715A (en) * | 2010-05-26 | 2010-10-13 | 上海大学 | Method for quickly crystallizing polylactic acid |
CN102585462A (en) * | 2011-12-08 | 2012-07-18 | 汕头卜高通美实业有限公司 | Heat-resistant polylactic acid composite material and preparation method thereof |
ITMI20111273A1 (en) * | 2011-07-08 | 2013-01-09 | Fond Cariplo | BRILLIANT POLYMERS OF LACTIC ACID WITH HIGH VISCOSITY IN THE MOLTEN AND HIGH SHEAR SENSITIVITY AND THEIR Dwarf COMPOSITE |
CN103467947A (en) * | 2013-09-04 | 2013-12-25 | 上海悦萌环保科技有限公司 | Talcum powder nucleating agent-containing crystallized polylactic acid bioplastic |
CN103772878A (en) * | 2014-01-13 | 2014-05-07 | 杭州伊贝实业有限公司 | Completely biodegradable material and preparation method thereof and cosmetics container |
CN103772925A (en) * | 2013-12-11 | 2014-05-07 | 浙江南益生物科技有限公司 | Liquid nano mica modifier for polylactic acid (PLA) |
US8829097B2 (en) | 2012-02-17 | 2014-09-09 | Andersen Corporation | PLA-containing material |
CN106633724A (en) * | 2016-12-08 | 2017-05-10 | 苏州艾博迈尔新材料有限公司 | Degradable composite biological plastic material and preparation process thereof |
CN109679074A (en) * | 2018-11-30 | 2019-04-26 | 中粮集团有限公司 | A kind of polylactic acid poly shares compound stabilizer and application thereof and application method |
CN110066501A (en) * | 2019-04-22 | 2019-07-30 | 浙江工业大学 | A kind of thickening method of PLA |
CN110204843A (en) * | 2019-05-17 | 2019-09-06 | 许艳辉 | A kind of flame-proof PVC material |
CN110358272A (en) * | 2019-08-02 | 2019-10-22 | 珠海格力新材料有限公司 | Polylactic acid composite material and preparation method and application thereof |
CN110760172A (en) * | 2019-11-05 | 2020-02-07 | 蚌埠学院 | Modification method for rapidly crystallizing high-crystallinity polylactic acid |
CN112048162A (en) * | 2020-08-21 | 2020-12-08 | 江西格林美资源循环有限公司 | Full-biodegradable modified plastic for plastic-uptake thin-wall products and preparation method thereof |
CN112442289A (en) * | 2020-11-10 | 2021-03-05 | 桂林桂广申巴粉体材料有限责任公司 | Modified talcum powder, and preparation method and application thereof |
CN113881203A (en) * | 2021-08-20 | 2022-01-04 | 联泓(江苏)新材料研究院有限公司 | Polylactic acid composition and preparation method and application thereof |
CN114410087A (en) * | 2022-01-19 | 2022-04-29 | 广东奇德新材料股份有限公司 | Barrier polylactic acid composite material and preparation method thereof |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1793228A (en) * | 2005-12-28 | 2006-06-28 | 中国科学院长春应用化学研究所 | Process for preparing complete biological degradation high flexible polyalctic material |
CN1887364A (en) * | 2006-07-20 | 2007-01-03 | 中国科学院长春应用化学研究所 | Biodegradable medical extracorporeal fixing material possessing shape memory function |
CN100577732C (en) * | 2007-04-25 | 2010-01-06 | 上海大学 | Toughened and reinforced polylactic acid nanocomposite material and preparation method thereof |
CN101333331A (en) * | 2008-08-07 | 2008-12-31 | 上海大学 | A polylactic acid composite material filled with high heat resistance talcum powder and its preparation method |
-
2009
- 2009-04-30 CN CN 200910050364 patent/CN101544813B/en not_active Expired - Fee Related
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101857715A (en) * | 2010-05-26 | 2010-10-13 | 上海大学 | Method for quickly crystallizing polylactic acid |
ITMI20111273A1 (en) * | 2011-07-08 | 2013-01-09 | Fond Cariplo | BRILLIANT POLYMERS OF LACTIC ACID WITH HIGH VISCOSITY IN THE MOLTEN AND HIGH SHEAR SENSITIVITY AND THEIR Dwarf COMPOSITE |
WO2013008156A1 (en) * | 2011-07-08 | 2013-01-17 | Universita' Degli Studi Di Milano | Branched lactic acid polymers with high viscosity in the molten state and high shear sensitivity, and nanocomposites thereof |
CN103781834A (en) * | 2011-07-08 | 2014-05-07 | 米兰大学 | Branched lactic acid polymers with high viscosity in the molten state and high shear sensitivity, and nanocomposites thereof |
CN102585462A (en) * | 2011-12-08 | 2012-07-18 | 汕头卜高通美实业有限公司 | Heat-resistant polylactic acid composite material and preparation method thereof |
US9512303B2 (en) | 2012-02-17 | 2016-12-06 | Andersen Corporation | PLA-containing material |
US8829097B2 (en) | 2012-02-17 | 2014-09-09 | Andersen Corporation | PLA-containing material |
CN103467947B (en) * | 2013-09-04 | 2016-06-29 | 上海悦萌环保科技有限公司 | Comprise the crystalline polylactic acid biological plastics of Pulvis Talci nucleator |
CN103467947A (en) * | 2013-09-04 | 2013-12-25 | 上海悦萌环保科技有限公司 | Talcum powder nucleating agent-containing crystallized polylactic acid bioplastic |
CN103772925A (en) * | 2013-12-11 | 2014-05-07 | 浙江南益生物科技有限公司 | Liquid nano mica modifier for polylactic acid (PLA) |
CN103772925B (en) * | 2013-12-11 | 2015-10-14 | 浙江南益生物科技有限公司 | A kind of liquid nano mica modification agent for PLA |
CN103772878B (en) * | 2014-01-13 | 2016-08-17 | 杭州伊贝实业有限公司 | Biodegradable Materials and preparation method thereof and cosmetic packaging box |
CN103772878A (en) * | 2014-01-13 | 2014-05-07 | 杭州伊贝实业有限公司 | Completely biodegradable material and preparation method thereof and cosmetics container |
CN106633724A (en) * | 2016-12-08 | 2017-05-10 | 苏州艾博迈尔新材料有限公司 | Degradable composite biological plastic material and preparation process thereof |
CN109679074A (en) * | 2018-11-30 | 2019-04-26 | 中粮集团有限公司 | A kind of polylactic acid poly shares compound stabilizer and application thereof and application method |
CN110066501B (en) * | 2019-04-22 | 2021-08-24 | 浙江工业大学 | A kind of thickening method of PLA |
CN110066501A (en) * | 2019-04-22 | 2019-07-30 | 浙江工业大学 | A kind of thickening method of PLA |
CN110204843A (en) * | 2019-05-17 | 2019-09-06 | 许艳辉 | A kind of flame-proof PVC material |
CN110358272A (en) * | 2019-08-02 | 2019-10-22 | 珠海格力新材料有限公司 | Polylactic acid composite material and preparation method and application thereof |
CN110760172A (en) * | 2019-11-05 | 2020-02-07 | 蚌埠学院 | Modification method for rapidly crystallizing high-crystallinity polylactic acid |
CN112048162A (en) * | 2020-08-21 | 2020-12-08 | 江西格林美资源循环有限公司 | Full-biodegradable modified plastic for plastic-uptake thin-wall products and preparation method thereof |
CN112048162B (en) * | 2020-08-21 | 2022-12-13 | 江西格林循环产业股份有限公司 | Full-biodegradable modified plastic for plastic-uptake thin-wall products and preparation method thereof |
CN112442289A (en) * | 2020-11-10 | 2021-03-05 | 桂林桂广申巴粉体材料有限责任公司 | Modified talcum powder, and preparation method and application thereof |
CN112442289B (en) * | 2020-11-10 | 2021-09-14 | 桂林桂广申巴粉体材料有限责任公司 | Modified talcum powder, and preparation method and application thereof |
CN113881203A (en) * | 2021-08-20 | 2022-01-04 | 联泓(江苏)新材料研究院有限公司 | Polylactic acid composition and preparation method and application thereof |
CN114410087A (en) * | 2022-01-19 | 2022-04-29 | 广东奇德新材料股份有限公司 | Barrier polylactic acid composite material and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN101544813B (en) | 2012-12-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101544813B (en) | Rapid crystallization polylactic acid composite material and preparation method thereof | |
CN104861210B (en) | A kind of starch base full biodegradable resin of hydrophobic stabilization and preparation method thereof | |
CN103159984B (en) | All-degradable thermoplastic starch/polylactic acid blend material and preparation method thereof | |
CN103304851A (en) | High-starch-content waterproof totally-decomposed composite material and preparation method thereof | |
CN102086299B (en) | Transparent crystallization polylactic acid plastic and preparation method thereof | |
WO2020083049A1 (en) | Tps/pla/pbat blend modified biodegradable resin prepared by using chain extender and preparation method therefor | |
CN102108196A (en) | A kind of preparation method of polylactic acid degradable material | |
CN103205076B (en) | Thermoplastic polyvinyl alcohol-polylactic acid blending material and preparation method thereof | |
CN101857715A (en) | Method for quickly crystallizing polylactic acid | |
CN103421285B (en) | A kind of Environment-friendlyheat-resistant heat-resistant polylactic acid and preparation method thereof | |
CN104072957A (en) | Food grade biodegradable polylactic acid-based composite material and application thereof | |
CN103087484A (en) | Biodegradable composite film material of controllable degradation rate and preparation method thereof | |
CN102731904A (en) | Enhanced master batch filled with modified talc powder, and preparation method thereof | |
CN104387732A (en) | Transparent, tear-resistant and biodegradable polylactic acid thin film and preparation method thereof | |
CN107603168B (en) | Polylactic acid-based film and preparation method thereof | |
CN111621239A (en) | Full-biodegradable adhesive tape and preparation method thereof | |
WO2014056293A1 (en) | Biodegradable material, preparation method and use thereof | |
CN105670191A (en) | Special material for modified starch-polyvinyl alcohol degradable membrane | |
CN101054463A (en) | Preparation method of fast crystallization type polylactic acid composite material | |
CN105038158A (en) | Preparation method of food-grade full-degradable high-temperature-resistant polylactic acid composite material | |
CN108976737A (en) | A kind of lignin makees biodegradable color masterbatch of pigment and preparation method thereof and purposes | |
CN102675841B (en) | Polylactic acid and poly(3-hydroxybutyrate-co-4-hydroxybutyrate) nano modified composite | |
CN109666269A (en) | One kind is containing the modified polyadipate/butylene terephthalate composite material and preparation method of nano micro crystal cellulose | |
CN112143042A (en) | Starch-based degradable film and preparation method thereof | |
CN102268178A (en) | Transparent plasticized polylactic acid nano resin slice with low mobility and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121219 Termination date: 20150430 |
|
EXPY | Termination of patent right or utility model |