School of Chemical Engineering, Universiti Sains Malaysia, Nibong Tebal, Penang, Malaysia.
Bioresour Technol. 2011 Feb;102(3):2659-64. doi: 10.1016/j.biortech.2010.10.119. Epub 2010 Oct 30.
In this study, methyl ester (ME) was produced by transesterification of palm oil (CPO) (cooking grade) using activated carbon supported calcium oxide as a solid base catalyst (CaO/AC). Response surface methodology (RSM) based on central composite design (CCD) was used to optimize the effect of reaction time, molar ratio of methanol to oil, reaction temperature and catalyst amount on the transesterification process. The optimum condition for CPO transesterification to methyl ester was obtained at 5.5 wt.% catalyst amount, 190°C temperature, 15:1 methanol to oil molar ratio and 1 h 21 min reaction time. At the optimum condition, the ME content was 80.98%, which is well within the predicted value of the model. Catalyst regeneration studies indicate that the catalyst performance is sustained after two cycles.
本研究采用活性炭负载氧化钙(CaO/AC)作为固体碱催化剂,通过酯交换反应由棕榈油(CPO)(烹饪级)制备甲酯(ME)。基于中心复合设计(CCD)的响应面法(RSM)用于优化反应时间、甲醇与油的摩尔比、反应温度和催化剂用量对酯交换过程的影响。在 5.5wt%催化剂用量、190°C温度、15:1甲醇与油摩尔比和 1h21min 反应时间的最佳条件下,CPO 转化为 ME 的甲酯含量达到 80.98%,这与模型的预测值吻合良好。催化剂再生研究表明,催化剂在经过两个循环后仍保持良好的性能。