酯交换
对苯二甲酸二甲酯
四氢呋喃
1,4-丁二醇
动力学
等温过程
材料科学
聚对苯二甲酸乙二醇酯
催化作用
有机化学
高分子化学
化学
热力学
复合材料
物理
量子力学
溶剂
作者
Lourdes Yurramendi,Marı́a J. Barandiaran,José M. Asúa
出处
期刊:Polymer
[Elsevier BV]
日期:1988-05-01
卷期号:29 (5): 871-874
被引量:11
标识
DOI:10.1016/0032-3861(88)90146-2
摘要
The kinetics of transesterification of dimethyl terephthalate with 1,4-butanediol have been studied in a semibatch reactor under non-isothermal conditions. Also, the kinetics of tetrahydrofuran production by side reactions were studied. Models were fitted by using an algorithm of parameter estimation in differential equations based on the Gauss-Newton method. It was found that the transesterification reaction had an overall order of three, with one order each for dimethyl terephthalate (DMT), 1,4-butanediol (BD) and catalyst concentration, whereas the formation of tetrahydrofuran (THF) involved reactions with fractional reaction order.
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