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Kinetics of liquid phase synthesis of tert-amyl ethyl ether from tert-amyl alcohol and ethanol over Amberlyst 16

机译:在Amberlyst 16上由叔戊醇和乙醇液相合成叔戊醚的动力学

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摘要

This work concerns catalyst screening for the synthesis of tert-amyl ethyl ether (TAEE) from a liquid-phase reaction between tert-amyl alcohol (TAA) and ethanol (EtOH). Various commercial catalysts, i.e., Amberlyst 15, Amberlyst 16, Amberlyst 36, Amberlyst 131, β-zeolite with Si/Al = 13.5 and 40, and Dowex 50WX8, were tested by performing the reaction in a semi-batch reactor operated at temperature of 353 K and pressure of 810.4 kPa. The dehydration of TAA to IA was found to be a major side reaction in this system. Amberlyst 16 shows the best performance in terms of selectivity and yield. Therefore, it was further investigated in the kinetic study. Three temperature levels of 333,343 and 353 K were performed to obtain the parameters in the Arrhenius's equation of the reaction rate constant and the Van't Hoff equation of water and ethanol sorption equilibrium. Two activity-based kinetic models of Langmuir-Hinshelwood (L-H) and Power Law (PL) were fitted with the experimental results. It was observed that the L-H model showed the best reaction rate description. The mole fraction-based PL model is also included in this study to follow the requirement of the ASPEN PLUS program.
机译:这项工作涉及从叔戊醇(TAA)和乙醇(EtOH)之间的液相反应合成叔戊基乙醚(TAEE)的催化剂筛选。通过在温度为200℃的半间歇反应器中进行反应,测试了各种商业催化剂,即Amberlyst 15,Amberlyst 16,Amberlyst 36,Amberlyst 131,Si / Al = 13.5和40的β沸石和Dowex 50WX8。 353 K,压力为810.4 kPa。发现TAA脱水成IA是该系统中的主要副反应。 Amberlyst 16在选择性和产率方面显示出最佳性能。因此,在动力学研究中作了进一步研究。在333,343和353 K的三个温度水平下进行,以获得反应速率常数的Arrhenius方程和水和乙醇吸附平衡的Van't Hoff方程中的参数。 Langmuir-Hinshelwood(L-H)和幂律(PL)的两个基于活动的动力学模型均符合实验结果。观察到L-H模型显示出最佳的反应速率描述。基于摩尔分数的PL模型也包括在本研究中,以遵循ASPEN PLUS程序的要求。

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