环己醇催化环戊二烯烷基化工艺的优化

A. Gasanov, R. Jafarov, I. G. Ayyubov, F. S. Qurbanova, O.M. Farzalizde
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引用次数: 0

摘要

以实验数据为基础,建立了环戊二烯与环己醇催化烷基化制环烷基取代环戊二烯过程的回归数学模型,反映了主要工艺因素(起始试剂配比、温度、催化剂用量)对目标产物收率的影响。对所建立的模型进行了统计分析,证明了所建立的模型与实验数据的充分性。在此条件下,环烷基化环戊二烯的产率达到最大值。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Optimization of the process of catalytic alkylation of cyclopentadiene by cyclohexyl alcohol
Based on the experimental data, a regression mathematical model has been developed for the process of obtaining cycloalkyl-substituted cyclopentadienes by catalytic alkylation of cyclopentadiene with cyclohexyl alcohol, reflecting the influence of the main technological factors (the ratio of the starting reagents, temperature, the amount of catalyst) on the yield of the target product. The statistical analysis of the obtained model is carried out, the adequacy of the developed model to the experimental data is proved. The optimal values of the input parameters are found, at which the maximum value of the yield of cycloalkylated cyclopentadienes is reached.
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