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Polycarbonate unit-containing polylactic acid copolymer and preparation method thereof

A polylactic acid copolymer and polycarbonate technology, which is applied in the field of polylactic acid copolymer and the preparation of polylactic acid composition containing aliphatic polycarbonate units, can solve the problem of low molecular weight of the copolymer, high production cost, non-biological origin, etc. question

Inactive Publication Date: 2012-06-06
TORAY FIBER RES INST(CHINA) CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the problems that the monomers in the existing polylactic acid copolymer preparation method with higher Tg are non-biological sources, the production cost is higher, and the molecular weight of the obtained copolymer is lower, the present invention discloses a method of using sulfuric acid, sulfonic acid or sulfonic acid / Metal compound composite system is the polymerization process of preparing polylactic acid copolymer by polycondensation of lactic acid or lactic acid prepolymer, polycarbonate prepolymer and functional group regulator with catalyst

Method used

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  • Polycarbonate unit-containing polylactic acid copolymer and preparation method thereof
  • Polycarbonate unit-containing polylactic acid copolymer and preparation method thereof
  • Polycarbonate unit-containing polylactic acid copolymer and preparation method thereof

Examples

Experimental program
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preparation example 1

[0065] After pouring 200 g of 90 wt % L-lactic acid aqueous solution into a 500 mL four-necked flask, the flask was placed in an oil bath. Install a stirrer on the four-neck flask, insert a thermocouple thermometer, connect the vacuum pipeline and the nitrogen pipeline and replace with nitrogen for 3 times, then raise the temperature of the oil bath to 120°C for dehydration. The system pressure gradually decreased from normal pressure to 5KPa within 60 minutes from the start of dehydration; then continued dehydration at 5KPa for 1.5 hours (total dehydration 2.5 hours); at this time, after returning the system pressure to normal pressure with nitrogen, add 107mg (300ppm) of stannous acetate and 363mg (632ppm) of 1,3-propanedisulfonic acid. Then the temperature of the system was raised to 160°C, the pressure was gradually reduced from normal pressure to 0.3KPa within 2 hours, and the pressure was kept at 0.3KPa for 4 hours (6 hours in total) after melt polymerization, poured out...

preparation example 2

[0068] 100g isosorbide and 500ml pyridine are added in the 1000ml round bottom flask, dissolve isosorbide at room temperature. Another 300ml of 0.76g / mol triphosgene in dichloromethane was added dropwise to the above isosorbide solution at 0°C and stirred at 0°C for 3h. 200mlH 2 O was added to the above reaction system to quench the terminal acid chloride group, and chloroform was added to remove pyridine in the system by azeotropic distillation. Methanol was added to the residual oil, and the precipitated polymer was filtered and washed four times with methanol and water. After filtration, the polymer was dried at 50° C. in a nitrogen atmosphere to obtain 105.8 g of a polycarbonate prepolymer. By testing the product samples, the following main properties are obtained:

[0069] Weight average molecular weight Mw: 3857. Glass transition temperature Tg: 124°C.

preparation example 3

[0071] Add 100 g of isosorbide and 500 ml of pyridine into a 1000 ml round bottom flask, and dissolve the isosorbide at room temperature. Another 300ml of 0.76g / mol triphosgene in dichloromethane was added dropwise to the above isosorbide solution at 0°C and stirred at 0°C for 10h. 200mlH 2 O was added to the above reaction system to quench the terminal acid chloride group, and chloroform was added to remove pyridine in the system by azeotropic distillation. Methanol was added to the residual oil, and the precipitated polymer was filtered and washed four times with methanol and water. After filtration, the polymer was dried at 50° C. in a nitrogen atmosphere to obtain 105.8 g of a polycarbonate prepolymer. By testing the product samples, the following main properties are obtained:

[0072] Weight average molecular weight Mw: 12973. Glass transition temperature Tg: 141°C.

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Abstract

The invention discloses a polycarbonate unit-containing polylactic acid copolymer and a preparation method thereof. The preparation method is characterized in that one or more polycarbonate prepolymers, a function group conditioning agent and lactic acid or a lactic acid prepolymer undergo a polycondensation reaction in the presence of sulfuric acid, sulfonic acid or a sulfonic acid-metal compound composite catalyst system as a catalyst to produce the polycarbonate unit-containing polylactic acid copolymer. The polycarbonate unit-containing polylactic acid copolymer obtained by the preparation method comprises a polycarbonate unit, a dicarboxylic acid unit and a polylactic acid unit, utilizes organisms as monomers, can be prepared easily, has a low production cost, high molecular weight and high Tg, and can be utilized for the fields such as blister package materials, disposable food boxes and the like having high heat-resistant requirements.

Description

technical field [0001] The invention belongs to the field of polymer materials, and in particular relates to a method for preparing a polylactic acid composition containing aliphatic polycarbonate units and the polylactic acid copolymer. Background technique [0002] Polylactic acid (PLA) is a degradable material derived from renewable resources that is currently researched and applied relatively more. It is a non-toxic and non-irritating material prepared from lactic acid obtained from starch fermentation (or chemical synthesis) Environmentally friendly material, it not only has good physical properties, but also has good biocompatibility and degradation performance. At present, there are two main factors that limit the wide application of polylactic acid: one factor is the high production cost and high price. The main reason for the high production cost is that the polymerization route adopted by the vast majority of applied polylactic acid is an indirect (ring-opening) m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G63/64C08G63/87C08G63/85C08G63/83C08G63/84
Inventor 左璞晶叶子浓牟世伟筒井英之何勇
Owner TORAY FIBER RES INST(CHINA) CO LTD