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BASIC KINETIC MODEL FOR THE REACTION YIELDING LINEAR POLYURETHANES .2.

机译:反应生成线性聚氨酯的基本动力学模型2。

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摘要

On the basis of the gradual polyaddition kinetic model developed earlier, an attempt was made to provide a generalized mathematical model for the set of reactions yielding linear polyurethanes. The model is a system of first-order ordinary differential equations. It was assumed at the present stage of this model that the rate constants for the reaction considered do not change. The model developed was then solved numerically Average molecular weight of the polymer and composition data for oligomers were calculated for a constant volume batch reactor and varied process parameters. The GPC method, which was tested for model urethane oligomers, was employed to verify the model developed. The reaction of 2,4-TDI with 1,4-butanediol proceeding in a solution was investigated. It was concluded that the model was applicable to a limited degree in describing the linear polyurethane manufacturing process which is more complex. However, it was suggested that the algorithms adopted could be utilized in developing further models which could assume changing rate constants for the polymer chain growth reactions. (C) 1995 John Wiley & Sons, Inc. [References: 16]
机译:基于较早开发的逐步加聚动力学模型,尝试为生成线性聚氨酯的一组反应提供通用的数学模型。该模型是一阶常微分方程组。在该模型的现阶段,假定所考虑的反应的速率常数不变。然后用数值方法解决开发的模型的问题。对于恒定体积的间歇式反应器和变化的工艺参数,计算出聚合物的平均分子量和低聚物的组成数据。采用GPC方法对模型氨基甲酸酯低聚物进行了测试,以验证所开发的模型。研究了在溶液中进行的2,4-TDI与1,4-丁二醇的反应。得出的结论是,该模型在描述线性聚氨酯制造过程中的适用性有限,该过程更为复杂。但是,建议采用的算法可以用于开发其他模型,这些模型可以假定聚合物链生长反应的速率常数发生变化。 (C)1995 John Wiley&Sons,Inc. [参考:16]

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