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Study on kinetics-thermodynamics and environmental parameter of biodiesel production from waste cooking oil and castor oil using potassium modified ceria oxide catalyst

机译:氧化钾改性的氧化铈催化从废食用油和蓖麻油生产生物柴油的动力学-热力学和环境参数的研究

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Research on biodiesel production from waste material and lignocellulosic biomass using heterogeneous catalyst has been studied throughout the world to achieve a sustainable source of fuel. Heterogeneous base-catalyzed transesterification attracts more attention as it overcomes the flaws regarding homogeneous catalysis. In this study, potassium (K) modified ceria oxide (CeO2) was synthesized via auto combustion method and introduced as the heterogeneous base catalyst for transesterification of waste cooking oil and castor oil. It was found that catalyst having K/Ce atomic ratio 2, activated at 800 degrees C showed highest efficiency of 99.09% and 98.49% FAME (fatty acid methyl ester or biodiesel) conversion in methyl esterification of waste cooking oil (WCO) and castor oil (CO) under moderate reaction condition. A robust base-catalyzed transesterification reaction mechanism was proposed based on FTIR result. The rate constants (k(C)) of the reaction at five different temperatures 45 to 65 degrees C with 5 degrees C interval were evaluated by mean of respective kinetic plots for methyl esterification of WCO and CO. Activation energy E-a for WCO and CO transesterification were calculated to be 50.1 kJ mol(-1) & 48.55 kJ mol(-1) with corresponding frequency factor 35.4 x 10 5 min(-1) & 11.9 x 10 5 min(-1). Enthalpy of activation (Delta H-#) was obtained to be 47.35 kJ mol(-1) and 45.989 kJ.mol(-l) with corresponding entropy of activation (Delta S-#) -128.69J.K-1. mol(-1) and -137.21J.K-1 . mol(-1) of methyl ester formation of WCO and CO. The Gibb's free energy of activation (Delta G(#)) for both reactions was evaluated to be 90.85 kJ mol(-1) and 92.66 kJ mol(-1). The positive values of both Delta G(#) and Delta H-# indicates that the reaction followed an endothermic nonspontaneous pathway while the negative Delta S-# value informs the reduction in randomness during transesterification. The catalyst showed high turnover frequency and meager value of Environmentalfactor which implies the catalyst is well efficient for fast production of biodiesel with minute waste generation. (C) 2019 Published by Elsevier Ltd.
机译:全世界已经研究了利用非均相催化剂从废料和木质纤维素生物质生产生物柴油的方法,以实现可持续的燃料来源。碱的非均相酯交换反应克服了均相催化方面的缺陷,因此引起了更多关注。在这项研究中,钾(K)改性的二氧化铈(CeO2)通过自动燃烧法合成,并作为废食用油和蓖麻油的酯交换反应的非均相基础催化剂而引入。发现在800℃下活化的具有K / Ce原子比2的催化剂在废食用油(WCO)和蓖麻油的甲基酯化反应中显示出最高的99.09%和98.49%的FAME(脂肪酸甲酯或生物柴油)转化率。 (CO)在中等反应条件下。基于FTIR结果,提出了一种鲁棒的碱催化的酯交换反应机理。通过WCO和CO的甲基酯化反应的各个动力学图,评估了在五个不同温度(45至65摄氏度,间隔5摄氏度)下反应的速率常数(k(C))。WCO和CO酯交换反应的活化能Ea计算得出为50.1 kJ mol(-1)和48.55 kJ mol(-1),相应的频率系数为35.4 x 10 5 min(-1)和11.9 x 10 5 min(-1)。获得的活化焓(ΔH-#)为47.35kJ mol(-1)和45.989kJ.mol(-1),具有相应的活化熵(ΔS-#)-128.69J.K-1。 mol(-1)和-137.21J.K-1。 WCO和CO形成甲酯的mol(-1)。两个反应的吉布活化活化能(Delta G(#))分别为90.85 kJ mol(-1)和92.66 kJ mol(-1)。 Delta G(#)和Delta H-#的正值表示反应遵循吸热非自发途径,而Delta S-#负值表示酯交换过程中随机性降低。该催化剂显示出高的周转频率和环境因子的微不足道的值,这意味着该催化剂对于快速生产生物柴油并产生微小废物非常有效。 (C)2019由Elsevier Ltd.发布

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