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Application of Calcium Methoxide as Solid Base Catalyst for Biodiesel Production from Waste Cooking Oil

机译:甲氧化钙作为固体碱催化剂从废料烹饪油中生产生物柴油生产

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In this study, the biodiesel production of waste cooking oil using calcium methoxide as solid base catalyst was investigated. The calcium methoxide catalyst was synthesized from calcined quick lime reacted with methanol. The XRD result showed that the catalyst was successfully synthesized with sufficient purity. The strength of catalyst was examined on the transesterification reaction of waste cooking oil and methanol. Parameters affecting on transesterification such as the catalyst concentration, methanol-to-oil-molar ratio, reaction time and reaction temperature were investigated. The results showed that the percentage of fatty acid methyl ester conversion of 99.06%. The optimum conditions were achieved within 3 h using 3wt% catalyst concentration, 12:1 methanol-to-oil molar ratio and 65°C reaction temperature. In addition, the kinetic study of transesterification reaction was carried out at the temperature from 30°C to 65°C. The pseudo-first order was good agreement with the experiment results. The reaction rate constant (k) and activated energy (Ea) were determined as 0.023 min~(-1) and 55.77 kJ/mol, respectively.
机译:在本研究中,研究了使用甲醇钙作为固体碱催化剂的废物烹饪油的生物柴油生产。用煅烧的快速石灰合成甲醇钙催化剂,与甲醇反应。 XRD结果表明,催化剂成功合成,具有足够的纯度。在废物烹饪油和甲醇的酯交换反应上检查催化剂的强度。研究了影响酯交换的参数,例如催化剂浓度,甲醇 - 油摩尔比,反应时间和反应温度。结果表明,脂肪酸甲酯转化率为99.06%的百分比。在3小时内实现最佳条件,使用3wt%催化剂浓度,12:1甲醇 - 油摩尔比和65℃反应温度。此外,酯交换反应的动力学研究在30℃至65℃的温度下进行。伪第一顺序与实验结果吻合良好。反应速率常数(k)和活性能量(EA)分别测定为0.023min〜(-1)和55.77 kJ / mol。

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