TWI582161B - Producing method of a biodegradable polylactic acid based composite - Google Patents
Producing method of a biodegradable polylactic acid based composite Download PDFInfo
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- TWI582161B TWI582161B TW104126439A TW104126439A TWI582161B TW I582161 B TWI582161 B TW I582161B TW 104126439 A TW104126439 A TW 104126439A TW 104126439 A TW104126439 A TW 104126439A TW I582161 B TWI582161 B TW I582161B
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- 239000004626 polylactic acid Substances 0.000 title claims description 50
- 229920000747 poly(lactic acid) Polymers 0.000 title claims description 47
- 239000002131 composite material Substances 0.000 title claims description 30
- 239000004368 Modified starch Substances 0.000 claims description 29
- 229920000881 Modified starch Polymers 0.000 claims description 29
- 235000019426 modified starch Nutrition 0.000 claims description 29
- 238000004898 kneading Methods 0.000 claims description 27
- 239000012745 toughening agent Substances 0.000 claims description 20
- 239000003484 crystal nucleating agent Substances 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 238000000855 fermentation Methods 0.000 claims description 15
- 230000004151 fermentation Effects 0.000 claims description 15
- 239000003607 modifier Substances 0.000 claims description 15
- 238000002156 mixing Methods 0.000 claims description 13
- 229920000728 polyester Polymers 0.000 claims description 11
- 239000004594 Masterbatch (MB) Substances 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 5
- 230000008018 melting Effects 0.000 claims description 5
- 239000002667 nucleating agent Substances 0.000 claims description 2
- 229920002472 Starch Polymers 0.000 description 14
- 239000000463 material Substances 0.000 description 14
- 235000019698 starch Nutrition 0.000 description 14
- 239000008107 starch Substances 0.000 description 14
- UTOPWMOLSKOLTQ-UHFFFAOYSA-N octacosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCC(O)=O UTOPWMOLSKOLTQ-UHFFFAOYSA-N 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000003921 oil Substances 0.000 description 10
- 235000019198 oils Nutrition 0.000 description 10
- -1 polyethylene Polymers 0.000 description 10
- 229920003023 plastic Polymers 0.000 description 9
- 239000004033 plastic Substances 0.000 description 9
- 229920001971 elastomer Polymers 0.000 description 7
- 239000000806 elastomer Substances 0.000 description 7
- 231100000614 poison Toxicity 0.000 description 7
- 239000003440 toxic substance Substances 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 6
- 235000013305 food Nutrition 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- PYSRRFNXTXNWCD-UHFFFAOYSA-N 3-(2-phenylethenyl)furan-2,5-dione Chemical compound O=C1OC(=O)C(C=CC=2C=CC=CC=2)=C1 PYSRRFNXTXNWCD-UHFFFAOYSA-N 0.000 description 5
- 229920000147 Styrene maleic anhydride Polymers 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 5
- 229920000299 Nylon 12 Polymers 0.000 description 4
- 159000000007 calcium salts Chemical group 0.000 description 4
- 229920006026 co-polymeric resin Polymers 0.000 description 4
- 229920006346 thermoplastic polyester elastomer Polymers 0.000 description 4
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 3
- HYCSHFLKPSMPGO-UHFFFAOYSA-N 3-hydroxypropyl dihydrogen phosphate Chemical compound OCCCOP(O)(O)=O HYCSHFLKPSMPGO-UHFFFAOYSA-N 0.000 description 3
- GUOCOOQWZHQBJI-UHFFFAOYSA-N 4-oct-7-enoxy-4-oxobutanoic acid Chemical compound OC(=O)CCC(=O)OCCCCCCC=C GUOCOOQWZHQBJI-UHFFFAOYSA-N 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 3
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 3
- 235000019482 Palm oil Nutrition 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000001073 acetylated oxidized starch Substances 0.000 description 3
- 235000013770 acetylated oxidized starch Nutrition 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 239000001361 adipic acid Substances 0.000 description 3
- 235000011037 adipic acid Nutrition 0.000 description 3
- 238000003915 air pollution Methods 0.000 description 3
- 239000004359 castor oil Substances 0.000 description 3
- 235000019438 castor oil Nutrition 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 239000003240 coconut oil Substances 0.000 description 3
- 235000019864 coconut oil Nutrition 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 3
- 239000001341 hydroxy propyl starch Substances 0.000 description 3
- 235000013828 hydroxypropyl starch Nutrition 0.000 description 3
- 239000002540 palm oil Substances 0.000 description 3
- 229920001707 polybutylene terephthalate Polymers 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- 239000005020 polyethylene terephthalate Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000000454 talc Substances 0.000 description 3
- 229910052623 talc Inorganic materials 0.000 description 3
- 235000012222 talc Nutrition 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 229920001225 polyester resin Polymers 0.000 description 2
- 239000004645 polyester resin Substances 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical group 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 1
- RAMLHCQVJWEUAO-UHFFFAOYSA-N 3-phenylpyrrole-2,5-dione;styrene Chemical compound C=CC1=CC=CC=C1.O=C1NC(=O)C(C=2C=CC=CC=2)=C1 RAMLHCQVJWEUAO-UHFFFAOYSA-N 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920003012 Hydroxypropyl distarch phosphate Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- MKRNVBXERAPZOP-UHFFFAOYSA-N Starch acetate Chemical compound O1C(CO)C(OC)C(O)C(O)C1OCC1C(OC2C(C(O)C(OC)C(CO)O2)OC(C)=O)C(O)C(O)C(OC2C(OC(C)C(O)C2O)CO)O1 MKRNVBXERAPZOP-UHFFFAOYSA-N 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 1
- 229920000704 biodegradable plastic Polymers 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 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 description 1
- 239000010696 ester oil Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000001310 hydroxy propyl distarch phosphate Substances 0.000 description 1
- 235000013825 hydroxy propyl distarch phosphate Nutrition 0.000 description 1
- DVROLKBAWTYHHD-UHFFFAOYSA-N hydroxy propyl distarch phosphate Chemical compound OC1C(O)C(OC)OC(CO)C1OC(O)CCOC1C(OC2C(C(O)C(OC3C(C(OP(O)(=O)OC4C(C(O)C(OC)OC4CO)O)C(C)OC3CO)O)OC2COC2C(C(O)C(OC)C(CO)O2)O)O)OC(CO)C(OC)C1O DVROLKBAWTYHHD-UHFFFAOYSA-N 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920005906 polyester polyol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920005996 polystyrene-poly(ethylene-butylene)-polystyrene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000013826 starch sodium octenyl succinate Nutrition 0.000 description 1
- 239000001334 starch sodium octenyl succinate Substances 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-L succinate(2-) Chemical compound [O-]C(=O)CCC([O-])=O KDYFGRWQOYBRFD-UHFFFAOYSA-L 0.000 description 1
- 229920002725 thermoplastic elastomer Polymers 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Description
一種生物可分解材料,特別是一種聚乳酸類生物可分解複合材料。 A biodegradable material, in particular a polylactic acid biodegradable composite.
目前拋棄式食物餐具依然是以泛用塑膠為主,如聚乙烯(Polyethylene,PE)、聚丙烯(Polypropylene,PP)、聚苯乙烯(Polystyrene,PS)、美耐皿或是保麗龍等,此種泛用塑膠雖具有低成本之優勢,但其生物不可分解性則對地球環境產生大幅危害,燃燒產生的有毒物質更會影響後代子孫的健康。 At present, disposable food tableware is still based on general-purpose plastics, such as polyethylene (Polyethylene, PE), polypropylene (PP), polystyrene (PS), melamine or styrofoam. Although this kind of general-purpose plastic has the advantage of low cost, its biodegradability has a great harm to the global environment, and the toxic substances produced by combustion will affect the health of future generations.
由於石油能源末日將至,替代性的塑膠為一發展趨勢,其中,聚乳酸(Poly Lactic Acid,PLA),號稱「生物塑膠」,利用生物原料來源的塑膠產品更是主流開發材料。但目前聚乳酸(PLA)雖具有生物可分解性的優勢,但耐熱性、機械強度不足,遇熱容易變形,難以取代一般石化泛用塑膠,若應用於拋棄式食物餐具更是限制重重。 As the end of petroleum energy is approaching, alternative plastics are a trend. Among them, Poly Lactic Acid (PLA), known as "bioplastics", is a mainstream development material using plastic materials derived from biological raw materials. However, although polylactic acid (PLA) has the advantages of biodegradability, it has insufficient heat resistance and mechanical strength, and is easily deformed by heat. It is difficult to replace the general petrochemical plastic. If it is used in disposable food and tableware, it is more restrictive.
為了解決既有聚乳酸(PLA)材料無法具有一定耐熱性或機械強度之種種缺點,本發明為一種生物可分解之聚乳酸複合材料的製造方法,其步驟包含有:利用一修飾澱粉及一聚酯油類產生一自然發酵反應形成一改 質澱粉;將上述該改質澱粉與一聚乳酸共同熔融混練;添加一增韌劑、一晶核劑以及一耐熱改質劑於該改質澱粉及該聚乳酸中一同熔融混練;將混練完成之該改質澱粉、該聚乳酸、該增韌劑、該晶核劑以及該耐熱改質劑自混練機擠出於水中降溫並進一步除水去濕形成一聚乳酸複合材料母料,其中:該自然發酵反應的反應溫度為常溫25℃~30℃開始至溫度介於60℃~65℃之間時結束;該混練溫度介於170℃~270℃;以及該增韌劑、該晶核劑以及該耐熱改質劑係於融熔混練溫度達平衡時添加。 In order to solve the disadvantages that the polylactic acid (PLA) material cannot have certain heat resistance or mechanical strength, the present invention is a method for producing a biodegradable polylactic acid composite material, which comprises the steps of: using a modified starch and a polymerization. Ester oil produces a natural fermentation reaction to form a change Starch; the above-mentioned modified starch and a polylactic acid are co-melted and kneaded; a toughening agent, a crystal nucleating agent and a heat-resistant modifier are melted and kneaded together in the modified starch and the polylactic acid; The modified starch, the polylactic acid, the toughening agent, the crystal nucleating agent and the heat-resistant modifier are extruded from a kneader in water to cool down and further dehydrated to form a polylactic acid composite masterbatch, wherein: The reaction temperature of the natural fermentation reaction is from a normal temperature of 25 ° C to 30 ° C until the temperature is between 60 ° C and 65 ° C; the kneading temperature is between 170 ° C and 270 ° C; and the toughening agent, the crystal nucleating agent And the heat-resistant modifier is added when the melting and kneading temperature reaches equilibrium.
其中,利用一混練機進行熔融混練。 Among them, a kneading machine is used for melt kneading.
其中,該增韌劑、該晶核劑以及該耐熱改質劑係自該混練機之側端開口入料。 Wherein, the toughening agent, the crystal nucleating agent and the heat-resistant modifying agent are fed from the side end opening of the kneading machine.
其中,將該聚乳酸複合材料母料進一步加工成形為耐熱溫度120℃之盛裝容器。 Among them, the polylactic acid composite masterbatch is further processed into a container having a heat-resistant temperature of 120 ° C.
本發明進一步提供一種生物可分解之聚乳酸複合材料,其包含有均勻熔融混練之聚乳酸50wt%~90wt%、修飾澱粉0.1wt%~40wt%、聚酯油類0.5wt%~35wt%、增韌劑0wt%~40wt%、晶核劑0wt%~5wt%以及耐熱改質劑0wt%~50wt%,該生物可分解之聚乳酸複合材料耐熱溫度達120℃。 The present invention further provides a biodegradable polylactic acid composite material comprising 50% to 90% by weight of polylactic acid uniformly melt-kneaded, 0.1% to 40% by weight of modified starch, and 0.5% to 35% by weight of polyester oil. The toughener is 0 wt% to 40 wt%, the crystal nucleating agent is 0 wt% to 5 wt%, and the heat resistant modifier is 0 wt% to 50 wt%, and the biodegradable polylactic acid composite material has a heat resistance temperature of 120 °C.
其中,該修飾澱粉是醋酸澱粉、乙醯化己二酸澱粉、羥丙基澱粉、羥丙基磷酸二澱粉、辛烯基丁二酸酯澱粉或是乙醯化氧化澱粉;該聚酯油類包含棕櫚油、蓖麻油或椰子油;該增韌劑是多元醇聚酯樹脂、乙烯基樹脂、甲基丙烯酸縮水甘油酯樹脂、聚對苯二甲酸乙二酯、聚對苯二甲酸丁二酯、苯乙烯-馬來酸酐共聚樹脂、熱可塑性聚酯彈性體、苯乙烯-乙烯-丁 烯-苯乙烯彈性體或是尼龍12彈性體;該晶核劑是蒙旦酸鈣鹽、蒙旦酸鈉鹽或是滑石粉;以及該耐熱改質劑是苯乙烯-苯基馬來醯亞胺共聚物。 Wherein, the modified starch is acetic acid starch, acetylated adipic acid starch, hydroxypropyl starch, hydroxypropyl phosphate diamyl starch, octenyl succinate starch or acetylated oxidized starch; the polyester oil Contains palm oil, castor oil or coconut oil; the toughening agent is a polyol polyester resin, a vinyl resin, a glycidyl methacrylate resin, polyethylene terephthalate, polybutylene terephthalate , styrene-maleic anhydride copolymer resin, thermoplastic polyester elastomer, styrene-ethylene-butyl An styrene elastomer or a nylon 12 elastomer; the crystal nucleating agent is a calcium salt of montanic acid, a sodium salt of montan or a talc; and the heat-resistant modifier is a styrene-phenyl malayan Amine copolymer.
本發明更進一步提供一種醫療用生物可吸收縫合線,其包含有均勻熔融混練之聚乳酸50wt%~90wt%、修飾澱粉0.1wt%~40wt%、聚酯油類0.5wt%~35wt%、增韌劑0wt%~40wt%、晶核劑0wt%~5wt%以及耐熱改質劑0wt%~50wt%。 The present invention further provides a medical bioabsorbable suture comprising 50% to 90% by weight of polylactic acid uniformly melt-kneaded, 0.1% to 40% by weight of modified starch, and 0.5% to 35% by weight of polyester oil. The toughener is 0 wt% to 40 wt%, the crystal nucleating agent is 0 wt% to 5 wt%, and the heat resistant modifier is 0 wt% to 50 wt%.
其中,該修飾澱粉是醋酸澱粉、乙醯化己二酸澱粉、羥丙基澱粉、羥丙基磷酸二澱粉、辛烯基丁二酸酯澱粉或是乙醯化氧化澱粉;該聚酯油類包含棕櫚油、蓖麻油或椰子油;該增韌劑是多元醇聚酯樹脂、乙烯基樹脂、甲基丙烯酸縮水甘油酯樹脂、聚對苯二甲酸乙二酯、聚對苯二甲酸丁二酯、苯乙烯-馬來酸酐共聚樹脂、熱可塑性聚酯彈性體、苯乙烯-乙烯-丁烯-苯乙烯彈性體或是尼龍12彈性體;該晶核劑是蒙旦酸鈣鹽、蒙旦酸鈉鹽或是滑石粉;以及該耐熱改質劑是苯乙烯-苯基馬來醯亞胺共聚物。 Wherein, the modified starch is acetic acid starch, acetylated adipic acid starch, hydroxypropyl starch, hydroxypropyl phosphate diamyl starch, octenyl succinate starch or acetylated oxidized starch; the polyester oil Contains palm oil, castor oil or coconut oil; the toughening agent is a polyol polyester resin, a vinyl resin, a glycidyl methacrylate resin, polyethylene terephthalate, polybutylene terephthalate , styrene-maleic anhydride copolymer resin, thermoplastic polyester elastomer, styrene-ethylene-butylene-styrene elastomer or nylon 12 elastomer; the crystal nucleating agent is calcium salt of montanic acid, montanic acid a sodium salt or talc; and the heat-resistant modifier is a styrene-phenyl maleimide copolymer.
依據上述說明可知,本發明具有以下優點: According to the above description, the present invention has the following advantages:
1.本發明因添加發酵後之改質澱粉,使得材料結構強度與韌性增強,提昇本發明之耐熱溫度達120℃,應用於食品餐具或是嬰兒奶瓶時,可耐高溫且不會釋放有毒物質,使用上安全無慮。 1. The invention improves the structural strength and toughness of the material by adding the modified starch after fermentation, and improves the heat-resistant temperature of the invention to 120 ° C. When used in food tableware or baby bottle, it can withstand high temperature and does not release toxic substances. , use safe and secure.
2.本發明回收燃燒時,主要添加物聚乳酸與澱粉皆為生物來源材料,燃燒不會產生有毒物質如戴奧辛,主要燃燒產物為水氣,不會造成空氣污染,燃燒後產生的煤瘩主要成份皆為有機物質,更可進一步當做植物、農作物的肥料。 2. When the invention recovers and burns, the main additives, polylactic acid and starch, are biologically derived materials, and the combustion does not produce toxic substances such as dioxin, and the main combustion product is water gas, which does not cause air pollution, and the coal slag generated after combustion is mainly The ingredients are all organic substances, and can be further used as fertilizer for plants and crops.
3.既有泛用塑膠回收後無法分解以及燃燒產生污染環境物質等種 種缺點,本發明之聚乳酸複合材料可取代既有泛用塑膠達到環境保護並減少碳足跡之功效。 3. It can be decomposed after recycling of general-purpose plastics and burned to produce environmentally harmful substances. Disadvantages, the polylactic acid composite material of the present invention can replace the utility of existing general-purpose plastics to achieve environmental protection and reduce carbon footprint.
圖1為本發明較佳實施例的製造流程圖。 1 is a flow chart of a manufacturing process in accordance with a preferred embodiment of the present invention.
一種生物可分解之聚乳酸複合材料的製造方法,其步驟包含有: A method for producing a biodegradable polylactic acid composite material, the steps comprising:
步驟1:利用一修飾澱粉及一聚酯油類產生一自然發酵反應形成一改質澱粉。其中,該自然發酵反應的反應溫度與反應時間係利用發酵反應之溫度上升判斷,自室溫開始混合該修飾澱粉及該聚酯油類,介於60℃~65℃之間時結束。該發酵反應之目的係為了增加該修飾澱粉之韌性與強度,於後續加工時可使本發明之複合材料之結構增強,韌性增加,以達到耐高溫之特性。 Step 1: Using a modified starch and a polyester oil to produce a natural fermentation reaction to form a modified starch. The reaction temperature and the reaction time of the natural fermentation reaction are judged by the increase in the temperature of the fermentation reaction, and the modified starch and the polyester oil are mixed from room temperature, and are completed between 60 ° C and 65 ° C. The purpose of the fermentation reaction is to increase the toughness and strength of the modified starch, and the structure of the composite material of the present invention can be enhanced and the toughness is increased in the subsequent processing to achieve high temperature resistance.
步驟2:將上述該改質澱粉與一聚乳酸共同熔融混練。熔融混練係利用一混練機於溫度170℃~270℃熔融混練。進一步地可於該混練機之側端開口添加一增韌劑、一晶核劑以及一耐熱改質劑於該改質澱粉及該聚乳酸中一同熔融混練。 Step 2: The above modified starch is co-melted and kneaded together with a polylactic acid. The melt kneading system is melt-kneaded at a temperature of 170 ° C to 270 ° C using a kneading machine. Further, a toughening agent, a crystal nucleating agent and a heat-resistant modifying agent may be added to the side end opening of the kneading machine to melt and knead together in the modified starch and the polylactic acid.
上述於該混練劑側端開口入料之原因,是由於一般混練機之側端開口多半係設置於混練機之中段,因該混練機原入料端之溫度相對於混練機中段低或是原入料端混練溫度因入料的因素而持續改變,若該增韌劑、該晶核劑以及該耐熱改質劑於原入料端入料可能會因為溫度不足或不均而無法均勻混合,故由混練機中段溫度較高處(混練溫度達平衡處)將該 增韌劑、該晶核劑以及該耐熱改質劑投入,可促進混練更加均勻,且因該增韌劑、該晶核劑以及該耐熱改質劑添加量相對該改質澱粉與該聚乳酸少,故自混練機中段處添加不會對混練溫度造成劇烈改變。 The reason for the above-mentioned opening at the side end of the kneading agent is that the side opening of the general kneading machine is mostly disposed in the middle of the kneading machine, because the temperature of the original feeding end of the kneading machine is lower than that of the middle of the kneading machine or the original The mixing temperature at the feed end is continuously changed due to the feeding factor. If the toughening agent, the crystal nucleating agent and the heat-resistant modifier are fed at the original feed end, the mixing may not be uniform due to insufficient or uneven temperature. Therefore, the temperature in the middle of the kneading machine is higher (the mixing temperature reaches the equilibrium) The toughening agent, the crystal nucleating agent and the heat-resistant modifier can promote the mixing more uniformly, and the amount of the toughening agent, the crystal nucleating agent and the heat-resistant modifier is increased relative to the modified starch and the polylactic acid. Less, so adding from the middle of the mixing machine will not cause drastic changes in the mixing temperature.
步驟3:將混練完成之該改質澱粉、該聚乳酸、該增韌劑、該晶核劑以及該耐熱改質劑自混練機擠出於水中降溫並進一步除水去濕形成一聚乳酸複合材料母料。該增韌劑、該晶核劑及該耐熱改質劑進一步輔助本發明之聚乳酸複合材料增韌、耐熱以及結晶特性。 Step 3: the modified starch, the polylactic acid, the toughening agent, the crystal nucleating agent and the heat-resistant modifier are extruded from the kneading machine in water to cool down and further remove water to form a polylactic acid composite. Material masterbatch. The toughening agent, the crystal nucleating agent and the heat resistant modifying agent further assist in the toughening, heat resistance and crystallization characteristics of the polylactic acid composite material of the present invention.
步驟4:將該聚乳酸複合材料母料進一步加工成形。一般聚乳酸材料耐熱溫度約60℃,若超過此溫度則產生形變。本發明因添加發酵後之改質澱粉,使得材料結構強度與韌性增強,可提昇耐熱溫度可達120℃。本發明除了可製造一般不需耐熱之物品,如文具、電子用品外殼、拋棄式醫療用具、醫療用生物可吸收縫合線或是嬰兒用品外,本發明可耐熱達120℃,更可應用於食品餐具或是嬰兒奶瓶等需要盛裝高溫食品之用具,本發明之聚乳酸複合材料可耐高溫且不會釋放有毒物質,使用上安全無慮。本發明回收燃燒時,主要添加物聚乳酸與澱粉皆為生物來源材料,燃燒不會產生有毒物質如戴奧辛,主要燃燒產物為水氣,不會造成空氣污染,燃燒後產生的煤瘩主要成份皆為有機物質,更可進一步當做植物、農作物的肥料。 Step 4: The polylactic acid composite masterbatch is further processed into a shape. Generally, the polylactic acid material has a heat resistance temperature of about 60 ° C, and if it exceeds this temperature, deformation occurs. The invention improves the structural strength and toughness of the material by adding the modified starch after fermentation, and can improve the heat resistance temperature up to 120 °C. In addition to the manufacture of articles which generally do not require heat resistance, such as stationery, electronic article casings, disposable medical appliances, medical bioabsorbable sutures or baby products, the present invention can be used for heat resistance up to 120 ° C, and can be applied to foods. The tableware or the baby bottle and the like which are required to hold the high-temperature food, the polylactic acid composite material of the invention can withstand high temperature and does not release toxic substances, and is safe to use. When the invention recovers and burns, the main additives, polylactic acid and starch, are biologically derived materials, and the combustion does not produce toxic substances such as dioxin, and the main combustion product is moisture, which does not cause air pollution, and the main components of the coal gangue produced after combustion are For organic matter, it can be further used as a fertilizer for plants and crops.
上述之該修飾澱粉添加比例佔該聚乳酸複合材料約為0.1~40wt%,該聚酯油類添加比例佔該聚乳酸複合材料約0.5~35wt%,該修飾澱粉可以是醋酸澱粉(Starch acetate)、乙醯化己二酸澱粉(Acetylated distrach adipate)、羥丙基澱粉(Hydroxypropyl starch)、羥丙基磷酸二澱粉 (Hydroxypropyl distarch phosphate)、辛烯基丁二酸酯澱粉(Starch sodium octenyl succinate)或是乙醯化氧化澱粉(Acetylated oxidized starch),該聚酯油類包含棕櫚油、蓖麻油或椰子油。上述之該增韌劑添加比例佔該聚乳酸複合材料約為0~40wt%,該增韌劑可以是多元醇聚酯樹脂(Polyester polyol)、乙烯基樹脂(Vinyl ester resin)、甲基丙烯酸縮水甘油酯樹脂(Glycol methanlacrylate acrylic resin)、聚對苯二甲酸乙二酯(Polyethylene terephthalate)、聚對苯二甲酸丁二酯(Polybutylene terephthalate)、苯乙烯-馬來酸酐共聚樹脂(Styrene-Maleic Anhydride Copolymer Resin)、熱可塑性聚酯彈性體(Theromplastic elastomer ester resin)、苯乙烯-乙烯-丁烯-苯乙烯彈性體(Styrene ethylene/butylene styrene elastomer)或是尼龍12彈性體(Polyamide 12 elastomer)。該晶核劑添加比例佔該聚乳酸複合材料約為0~5wt%,該晶核劑可以是蒙旦酸鈣鹽(Calcium soap of montanic acids)、蒙旦酸鈉鹽(Sodium soap of montanic acids)或是滑石粉(Talc)。該耐熱改質劑添加比例佔該聚乳酸複合材料約為0~50wt%,該耐熱改質劑可以是苯乙烯-苯基馬來醯亞胺共聚物(Styrene-phenyl maleimide copolymer)。 The modified starch is added in an amount of about 0.1 to 40% by weight of the polylactic acid composite, and the polyester oil is added in an amount of about 0.5 to 35 wt% of the polylactic acid composite. The modified starch may be Starch acetate. , Acetylated distrach adipate, Hydroxypropyl starch, Hydroxypropyl phosphate (Hydroxypropyl distarch phosphate), Starch sodium octenyl succinate or Acetylated oxidized starch, the polyester oil comprising palm oil, castor oil or coconut oil. The toughening agent is added in an amount of about 0-40% by weight of the polylactic acid composite material, and the toughening agent may be a polyester polyol, a vinyl resin, or a methacrylic acid shrinkage. Glycol methanlacrylate acrylic resin, polyethylene terephthalate, polybutylene terephthalate, styrene-maleic anhydride copolymer (Styrene-Maleic Anhydride Copolymer) Resin), Thermoplastic elastomer ester resin, Styrene ethylene/butylene styrene elastomer or Polyamide 12 elastomer. The nucleating agent is added in an amount of about 0 to 5 wt% of the polylactic acid composite material, and the crystal nucleating agent may be Calcium soap of montanic acids or sodium soap of montanic acids. Or talcum powder (Talc). The heat-resistant modifier is added in an amount of about 0 to 50% by weight of the polylactic acid composite, and the heat-resistant modifier may be a Styrene-phenyl maleimide copolymer.
本發明第一較佳實施例: A first preferred embodiment of the invention:
聚乳酸-----------------------65wt% Polylactic acid-----------------------65wt%
棕櫚油-----------------------0.5~30wt% Palm oil-----------------------0.5~30wt%
辛烯基丁二酸酯澱粉----------------------10wt% Octenyl succinate starch----------------------10wt%
熱可塑性聚酯彈性體----------------------15wt% Thermoplastic Polyester Elastomer --------------------- 15wt%
苯乙烯-苯基馬來醯亞胺共聚物-----------------------10wt% Styrene-phenylmaleimide copolymer-----------------------10wt%
蒙旦酸鈣鹽-----------------------0.5phr Montan acid calcium salt-----------------------0.5phr
均勻混合辛烯基丁二酸酯澱粉以及聚酯油類進行自然發酵反應,至自然發酵反應的反應溫度達60℃~65℃形成改質澱。將改質澱粉添加至混練機中與聚乳酸一同融熔混練,混練溫度約介於170℃~270℃,混練同時自混練機側端開口將熱可塑性聚酯彈性體、苯乙烯-苯基馬來醯亞胺共聚物以及蒙旦酸鈣鹽加入一起融熔混練。混練完成後將所有材料自混練機擠出至冷卻水中,加以除水去濕後形成聚乳酸複合材料母料,將該聚乳酸複合材料母料進一步造粒成形。 The octene succinate starch and the polyester oil are uniformly mixed for natural fermentation reaction, and the reaction temperature of the natural fermentation reaction reaches 60 ° C to 65 ° C to form a modified lake. The modified starch is added to the kneading machine and melted and mixed with the polylactic acid. The mixing temperature is about 170 ° C ~ 270 ° C. The kneading at the same time from the side end of the mixing machine will be a thermoplastic polyester elastomer, styrene-phenyl horse. The quinone imine copolymer and the calcium salt of montanic acid are added together for melting and kneading. After the mixing is completed, all the materials are extruded from the kneading machine into the cooling water, dehydrated by water to form a polylactic acid composite masterbatch, and the polylactic acid composite masterbatch is further granulated and formed.
本發明第二較佳實施例:
均勻混合乙醯化己二酸澱粉以及聚酯油類進行自然發酵反應,至自然發酵反應的反應溫度達60℃~65℃形成改質澱粉。將改質澱粉添加至混練機中與聚乳酸一同融熔混練,混練溫度約介於170℃~270℃,混練同時自混練機側段開口將尼龍12彈性體、苯乙烯-馬來酸酐共聚樹脂、苯乙烯-苯基馬來醯亞胺共聚物以及蒙旦酸鈣鹽加入一起融熔混練。混練完成後將所有材料自混練機擠出至冷卻水中,加以除水去濕後形成聚乳酸複合材料母料,將該聚乳酸複合材料母料進一步造粒成形。 The acetylated adipic acid starch and the polyester oil are uniformly mixed for natural fermentation reaction, and the reaction temperature of the natural fermentation reaction reaches 60 ° C to 65 ° C to form a modified starch. The modified starch is added to the kneading machine and melted and mixed with the polylactic acid. The mixing temperature is about 170 ° C ~ 270 ° C, and the nylon 12 elastomer and styrene-maleic anhydride copolymer resin are mixed at the side of the mixing machine. The styrene-phenyl maleimide copolymer and the calcium salt of montanic acid are added together for melting and kneading. After the mixing is completed, all the materials are extruded from the kneading machine into the cooling water, dehydrated by water to form a polylactic acid composite masterbatch, and the polylactic acid composite masterbatch is further granulated and formed.
藉由上述說明可知,本發明具有以下優點: As can be seen from the above description, the present invention has the following advantages:
1.本發明因添加發酵後之改質澱粉,使得材料結構強度與韌性增強,提昇本發明之耐熱溫度達120℃,應用於食品餐具或是嬰兒奶瓶時,可耐高溫且不會釋放有毒物質,使用上安全無慮。 1. The invention improves the structural strength and toughness of the material by adding the modified starch after fermentation, and improves the heat-resistant temperature of the invention to 120 ° C. When used in food tableware or baby bottle, it can withstand high temperature and does not release toxic substances. , use safe and secure.
2.本發明回收燃燒時,主要添加物聚乳酸與澱粉皆為生物來源材料,燃燒不會產生有毒物質如戴奧辛,主要燃燒產物為水氣,不會造成空氣污染,燃燒後產生的煤瘩主要成份皆為有機物質,更可進一步當做植物、農作物的肥料。 2. When the invention recovers and burns, the main additives, polylactic acid and starch, are biologically derived materials, and the combustion does not produce toxic substances such as dioxin, and the main combustion product is water gas, which does not cause air pollution, and the coal slag generated after combustion is mainly The ingredients are all organic substances, and can be further used as fertilizer for plants and crops.
3.既有泛用塑膠回收後無法分解以及燃燒產生污染環境物質等種種缺點,本發明之聚乳酸複合材料可取代既有泛用塑膠達到環境保護並減少碳足跡之功效。 3. The polylactic acid composite material of the present invention can replace the existing general-purpose plastics to achieve environmental protection and reduce the carbon footprint by having various disadvantages such as the inability to decompose after the recovery of the general-purpose plastic and the pollution of the environment.
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