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Experimental and Modeling Study of Melt Polycondensation Process of PA-MXD6

机译:PA-MXD6熔融缩聚过程的实验和建模研究

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The main polycondensation reaction of poly(m-xylene adipamide) (PA-MXD6) is a reversible reaction strongly coupled with mass transfer in melt polycondensation process. In this work, a realistic model for melt polycondensation of PA-MXD6 has been proposed taking in to account the kinetics data, equilibrium data and diffusion process for major by-product water in the melts. The characteristics of reaction and the effects of mass-transfer of polycondensation process have been studied by using stagnant film experiments. It is observed that the apparent rate of the polycondensation process increases with higher temperature, lower degree of vacuum and thinner film thickness with reduced specific interfacial area. Based on the experimental data, the model parameters including the kinetics data, equilibrium data and mass transfer coefficient of volatile have been estimated by the nonlinear least squares method. The model predictions are in a quite satisfactory agreement with the experimental data that all of the relative deviations are almost less than 2%.
机译:聚(M-二甲苯酰亚胺)(PA-MXD6)的主要缩聚反应是强烈偶联的可逆反应与熔融缩聚过程中的质量传递。在这项工作中,提出了一种融合PA-MXD6熔融缩聚的现实模型,以考虑熔体中主要副产物水的动力学数据,平衡数据和扩散过程。通过使用停滞薄膜实验,研究了反应的特征和缩聚过程的质量转移的影响。观察到,缩聚过程的表观速率随着更高的温度,较低的真空度和薄膜厚度而增加,具有减少的特异性界面区域。基于实验数据,通过非线性最小二乘法估计包括动力学数据,均衡数据和挥发性传质系数的模型参数。模型预测与实验数据同意相当令人满意,即所有相对偏差几乎小于2%。

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