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Alkylation of benzene with ethanol over modified HZSM-5 zeolite catalysts

机译:改性的HZSM-5沸石催化剂上苯与乙醇的烷基化

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Alkylation of benzene with ethanol was analysed using unmodified as well as modified shape selective HZSM-5 (Si/Al?=?31) zeolite catalysts. The reaction was carried out in a continuous fixed bed flow reactor in the temperature range of 300–500?°C at atmospheric pressure to investigate the activity of various catalysts for the selectivity and yield of ethylbenzene (the desired product). The alkylation of benzene with ethanol (2:1 by volume) produces ethyl benzene as primary product and others like diethylbenzene, triethylbenzene and xylene mixtures as secondary products. The modification of HZSM-5 was done by impregnation using boron and magnesium. The modification caused changes in the surface area, acidity and pore volume of zeolite sample. The physiochemical properties of catalysts were characterised by XRD, TEM, BET, TGA, FTIR, NH3-TPD and SEM. The feed and products were analysed by gas chromatography. The conversion of benzene was found to be better in bi metallic (B and Mg) modified HZSM-5 followed by unmodified HZSM-5. The modified catalysts gave better selectivity (72.8?%) and yield (38.1?%) of ethylbenzene.
机译:用未改性的和形状选择性的HZSM-5(Si / Al 2 = 31)沸石催化剂分析苯与乙醇的烷基化反应。该反应在大气压下于300-500℃的连续固定床流动反应器中进行,以研究各种催化剂对乙苯(所需产物)的选择性和收率的活性。苯与乙醇(体积比为2:1)的烷基化产生乙苯作为主要产物,而其他二乙苯,三乙苯和二甲苯混合物则作为次要产物。 HZSM-5的改性是通过使用硼和镁进行浸渍来完成的。改性引起沸石样品的表面积,酸度和孔体积的变化。通过XRD,TEM,BET,TGA,FTIR,NH3-TPD和SEM对催化剂的理化性质进行了表征。通过气相色谱分析进料和产物。发现在双金属(B和Mg)改性的HZSM-5中苯的转化率更高,其次是未改性的HZSM-5。改性的催化剂具有较好的选择性(72.8%)和乙苯的产率(38.1%)。

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