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Methyl transesterification of waste cooking oil using a laboratory synthesized reusable heterogeneous base catalyst: Process optimization and homogeneity study of catalyst

机译:使用实验室合成的可重复使用的非均相基础催化剂对食用油进行甲基酯交换反应:催化剂的工艺优化和均质性研究

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摘要

A novel heterogeneous base catalyst, potassium impregnated zinc oxide was synthesized via precipitation method. It was modified by impregnation method and was used for synthesis of biodiesel using waste cooking oil as feedstock. The synthesized catalyst was characterized using various sophisticated techniques. The catalyst having a K/Zn atomic ratio of 60:40 was calcined at 900 degrees C, provided the highest catalytic activity. Effect of different reaction parameters on biodiesel conversion efficiency were scrutinized. The experimental results showed that highest biodiesel conversion of 98% was achieved at optimized reaction conditions, at catalyst loading of 2.5 wt%, oil: methanol molar ratio of 1:18, 600 rpm and 65 degrees C for 50 min reaction time. Kinetics of the transesterification reaction was studied at varying reaction temperature (45-65 degrees C) and the reaction marked the highest rate constant at 65 degrees C. The activation energy of the reaction was 14.54 kJ/mol. The reusability and homogeneous contribution of the catalyst was examined and it was investigated that leaching of active components from catalyst into the reaction media was responsible for catalyst deactivation and homogeneity. The synthesis of biodiesel was ascertained by ATR-FTIR and NMR (H-1 and C-13) analysis. (c) 2017 Elsevier Ltd. All rights reserved.
机译:通过沉淀法合成了一种新型的非均相碱催化剂,即浸渍钾的氧化锌。通过浸渍法对其进行了改性,并以废食用油为原料用于生物柴油的合成。使用各种复杂的技术对合成的催化剂进行了表征。 K / Zn原子比为60:40的催化剂在900℃下煅烧,提供了最高的催化活性。考察了不同反应参数对生物柴油转化效率的影响。实验结果表明,在最佳反应条件下,催化剂负载量为2.5 wt%,油:甲醇摩尔比为1:18、600 rpm和65摄氏度下反应50分钟,可实现最高98%的生物柴油转化率。在变化的反应温度(45-65℃)下研究了酯交换反应的动力学,反应在65℃下标记出最高速率常数。反应的活化能为14.54kJ / mol。检查了催化剂的可重用性和均相性,并研究了活性成分从催化剂浸出到反应介质中是造成催化剂失活和均质性的原因。通过ATR-FTIR和NMR(H-1和C-13)分析确定了生物柴油的合成。 (c)2017 Elsevier Ltd.保留所有权利。

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