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Kinetic studies of liquid phase ethyl tert-butyl ether (ETBE) synthesis using macroporous and gelular ion exchange resin catalysts

机译:大孔和凝胶离子交换树脂催化剂合成液相乙基叔丁基醚(ETBE)的动力学研究

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Ethyl tert-butyl ether (ETBE) synthesis from ethanol (EtOH) and tert-butyl alcohol (TBA) was studied with different macroporous and gelular ion exchange resin catalysts. Purolite(R) (CT-124, CT-145H, CT-151, CT-175 and CT-275) and Amberlyst(R) (15 and 35) ion exchange resins were used for the present work. Effect of various parameters such as catalyst type, temperature, reactants feed molar ratio and catalyst loading were studied for the optimisation of reaction condition. Among the catalysts studied, Purolite CT-124 gave the best results for TBA conversion and selectivity towards ETBE. Kinetic modelling was performed with this catalyst and activation energy and water inhibition coefficient were determined. Heterogeneous kinetic models [e.g., Eley-Rideal (ER), Langmuir-Hinshelwood-Hougen-Watson (LHHW)] were unable to predict the behaviour of this etherification reaction, whilst the quasi-homogeneous (QH) model represented the system very well over wide range of reaction conditions.
机译:用不同的大孔和凝胶离子交换树脂催化剂研究了乙醇(EtOH)和叔丁醇(TBA)合成乙基叔丁基醚(ETBE)。 Purolite(CT-124,CT-145H,CT-151,CT-175和CT-275)和Amberlyst(15和35)离子交换树脂用于本工作。为了优化反应条件,研究了催化剂类型,温度,反应物进料摩尔比和催化剂负载量等各种参数的影响。在所研究的催化剂中,Purolite CT-124的TBA转化率和对ETBE的选择性给出了最佳结果。用该催化剂进行动力学建模并确定活化能和水抑制系数。异质动力学模型[例如,Eley-Rideal(ER),Langmuir-Hinshelwood-Hougen-Watson(LHHW)]无法预测该醚化反应的行为,而准均质(QH)模型则很好地代表了该系统反应条件范围广。

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