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Recycled poly(ethylene terephthalate) chain extension by a reactive extrusion process

机译:通过反应挤出工艺回收的聚对苯二甲酸乙二醇酯扩链

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摘要

A commercial-scale reactive extrusion processing system for recycled poly(ethylene terephthalate) (PET) flakes with an added chain extender, pyromellitic dianhydride (PMDA), was investigated. The PMDA concentration was varied with the intention of reaching a higher recycled PET intrinsic viscosity ([eta]). The effect of changing the extruder residence time on the system's stability and the recycled PET [eta] was also investigated. Reactive extruded PET with a PMDA concentration up to 0.3 wt% was found to have a higher [eta] and lower carboxyl content than recycled PET processed in a normal extrusion system. A shift in [eta] of about 0.18 dl/g was obtained with a 0.3 wt% PMDA concentration. A PMDA concentration above 0.3 wt% produced chemical. thermal and hydrodynamic instability in the system, causing crosslinking reactions and gel formation. The reactive extrusion system was stable at low residence time (45 s) and moderate (0.15 wt%) PMDA concentration; however, using 0.2 wt% PMDA produced higher reactive extruded recycled PET [eta] with lower carboxyl content than other PMDA concentration levels examined. Residence times higher than 45 s produced higher reactive extruded recycled PET [eta]. Reactive extruded recycled PET was also tested for mechanical properties. (C) 2004 Society of Plastics Engineers.
机译:研究了一种商业规模的反应型挤出加工系统,该系统用于回收的聚对苯二甲酸乙二酯(PET)片,并添加了扩链剂均苯四甲酸二酐(PMDA)。为了达到更高的再循环PET特性粘度(η),改变PMDA浓度。还研究了改变挤出机停留时间对系统的稳定性和回收的PETη的影响。发现PMDA浓度高达0.3重量%的反应性挤出PET具有比在常规挤出系统中加工的再生PET更高的η和更低的羧基含量。在0.3重量%的PMDA浓度下,获得约0.18dl / g的η位移。 PMDA浓度超过0.3 wt%会产生化学物质。系统中的热和流体动力学不稳定,导致交联反应和凝胶形成。反应挤出系统在低停留时间(45 s)和中等(0.15 wt%)PMDA浓度下稳定;然而,使用0.2重量%的PMDA比所检查的其他PMDA浓度水平产生更高的反应性挤出的再生PET,其羧基含量更低。高于45秒的停留时间产生更高的反应性挤出再生PETη。还对反应挤出的再生PET的机械性能进行了测试。 (C)2004年塑料工程师学会。

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