Lactic acid-based resin composition
一种树脂组合物、乳酸基的技术,应用在合成树脂层状产品、化学仪器和方法、分层产品等方向,能够解决再现性不好、反应难以控制、不可能得到聚乳酸层压材料等问题
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[0072] A preferred embodiment of the lactic acid-based resin is polylactic acid resin.
[0073] A preferred embodiment of the polylactic acid resin is the polylactic acid resin of Mitsui Chemicals Co., Ltd., LACEA (trade name).
[0074] LACEA brands include, for example, H-100, H-400, H-440, H-360, H-280, 100J, H-100E, M151S Q04, M151S Q52, etc.
[0075] [Ethylene-unsaturated carboxylic acid copolymer and its ionically crosslinked copolymer]:
[0076] The unsaturated carboxylic acid unit content of the ethylene-unsaturated carboxylic acid copolymer or its ion-crosslinked copolymer used in the present invention preferably falls between 2 and 25% by weight, more preferably between 5 and 20% by weight. If its carboxylic acid unit content is less than the above-defined range, the copolymer or its ionically crosslinked copolymer will be incompatible with polylactic acid; but if it is greater than this range, the copolymer or its ionically crosslinked copolymer will be extremely difficu...
preparation Embodiment 1
[0120] 400 kg of L-lactide, 0.04 kg of stannous zincate, and 0.12 kg of dodecanol were put into a thick-walled column type stainless steel polymerization reactor equipped with a stirrer, and vacuum degassed for 2 hours. Purged with nitrogen, the resulting mixture was heated and stirred at 200°C under 10 mmHg for 2 hours.
[0121] After the reaction, the polylactic acid melt was taken out from the outlet at the bottom, cooled in the air, and cut with a pelletizer. In this way, 340 kg of polylactic acid (yield 85%) was obtained, and the weight average molecular weight (Mw) of this polymer was 138,000.
preparation Embodiment 2
[0123] 100kg of 90% L-lactic acid and 450g of tin powder were put into a reactor equipped with a Dien-Stark soda valve, heated and stirred at 150°C under 50mmHg for 3 hours while evaporating the water, and then further stirred at 30mmHg, 150°C For 2 hours, the oligomerization reaction was carried out. To the oligomer, 210kg of diphenyl ether, 35mmHg, and 150°C were added for azeotropic dehydration. The evaporated water and solvent are separated in the Dien-Stark soda valve, and only the solvent is returned to the reactor. The organic solvent returned to the reactor after 2 hours passes through a column containing 46 kg of 3A molecular sieve and then returns to the reactor. Under these conditions, the reaction was continued at 17 mmHg and 130°C for 20 hours to obtain a polylactic acid solution with a weight average molecular weight (Mw) of 150,000. This solution was diluted by adding 440 kg of anhydrous diphenyl ether, then cooled to 40°C, and the precipitated crystals were taken o...
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