Optimization of the process of phenol alkylation by isoprene cyclodimer in the presence of KU-23 catalyst at a continuous operation plant

R. Jafarov, Ch. K. Rasulov, I. I. Alekperova, Z. Z. Aghamali̇yev, A. M. Dadasheva
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Abstract

Determining the theoretical optimal conditions for the phenol alkylation process creates the basis for evaluating the prospects of this process as well. For the alkylation process used phenol and isoprene cyclodimers as feedstock. To determine the optimal reaction conditions for the catalytic alkylation of phenol with isoprene cyclodimers in a continuous pilot plant, the effects of temperature, molar ratio of initial reagents, and space velocity on the yield and selectivity of the target product were studied. The study was carried out in the temperature range of 80 – 1500C, the molar ratio of phenol to CDI was 0.5:1 – 2:1 and the space velocity was within 0.25 – 1.0 h-1. To develop a regression model of the process, it is necessary to identify the functional relationship between the process parameters and use it for further process prediction. Considering that the number of experiments is m=13, and the output variables are n=3, the functional relationship can be represented as a non-linear polynomial. To determine the coefficients of the equation, the S-pluse 2000 Professional program was used, which allows us to automatically calculate statistical analysis data: regression model coefficients and pair correlation coefficients, as well as quadratic effect coefficients. Applying Student's criterion, significant and insignificant coefficients of the equation were found. To test the adequacy of the model, the Fisher criterion was used, which makes it possible to prove the adequacy of the description of the response surface by regression equations. When comparing the found values of Fes of the criterion with the tabular ones at the chosen confidence probability of 95% and the numbers of degrees of freedom f1=6 and f2=2, it can be seen that the calculated values of Fes are less than Ft=19.3, and this indicates the adequacy of the description of the response surface by regression equations. Using the developed regression model on a PC, calculations were made to study the influence of each input factor on the output parameters. To solve the optimization problem, the Matlab-6.5 program was used, which contains modern algorithms for solving the linear programming problem. As a result, the solution of the optimization problem was found that at a temperature of 1400C, a ratio of components of 1:0.5 and a space velocity of 0.25 h-1, the selectivity value is 91%, while the yield of the target product reaches 69%.
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在KU-23催化剂存在下,异戊二烯环二聚体苯酚烷基化工艺的优化
确定苯酚烷基化工艺的理论最佳条件,也为评价该工艺的前景奠定了基础。烷基化工艺以苯酚和异戊二烯环二聚体为原料。为了确定苯酚与异戊二烯环二聚体催化烷基化的最佳反应条件,研究了反应温度、初始试剂摩尔比、空速对目标产物收率和选择性的影响。研究的温度范围为80 ~ 1500C,苯酚与CDI的摩尔比为0.5:1 ~ 2:1,空速为0.25 ~ 1.0 h-1。为了建立工艺的回归模型,有必要确定工艺参数之间的函数关系,并将其用于进一步的工艺预测。考虑实验次数m=13,输出变量n=3,函数关系可以表示为非线性多项式。为了确定方程的系数,我们使用S-pluse 2000 Professional程序,该程序可以自动计算统计分析数据:回归模型系数和配对相关系数,以及二次效应系数。应用学生准则,发现方程的系数有显著性和不显著性。为了检验模型的充分性,采用Fisher准则,从而可以证明回归方程对响应面描述的充分性。在选取的置信概率为95%,自由度为f1=6和f2=2的情况下,将准则的Fes的求得值与表中Fes的求得值进行比较,可以看出,Fes的计算值小于Ft=19.3,说明回归方程对响应面描述的充分性。利用所建立的回归模型在PC机上进行了计算,研究了各输入因素对输出参数的影响。为了解决优化问题,使用了Matlab-6.5程序,该程序包含了求解线性规划问题的现代算法。结果表明,在温度为1400C,组分比为1:0.5,空速为0.25 h-1的条件下,选择性值为91%,目标产物收率达到69%。
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