Successive optimisation of waste cooking oil transesterification in a continuous microwave assisted reactor

被引:15
作者
Ali, M. A. Mohd. [1 ]
Yunus, R. M. [1 ]
Cheng, C. K. [2 ]
Gimbun, J. [2 ]
机构
[1] Univ Malaysia Pahang, Fac Chem & Nat Resources Engn, Gambang 26300, Pahang, Malaysia
[2] Univ Malaysia Pahang, Ctr Excellence Adv Res Fluid Flow CARIFF, Gambang 26300, Pahang, Malaysia
来源
RSC ADVANCES | 2015年 / 5卷 / 94期
关键词
RESPONSE-SURFACE METHODOLOGY; BIODIESEL PRODUCTION; IRRADIATION; CATALYST;
D O I
10.1039/c5ra15834f
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This paper presents an optimization study of waste cooking oil (WCO) transesterification in a continuous microwave assisted reactor (CMAR). The custom-built CMAR employed an integrated proportional-integral-derivative controller for accurate control of temperature and reactant flowrate. The fatty acid methyl ester contents in the sample were determined using gas chromatography mass spectrometry (GC-MS). The results from two-level factorial design showed that the methanol to oil molar ratio, amount of NaOCH3 catalyst and reaction time influenced markedly the biodiesel conversion, with the significance of 45.99%, 6.76% and 3.21%, respectively. Further analysis using a successive optimization method generated by the Box-Behnken design predicted an optimum biodiesel conversion of circa 97.13% at 0.68 wt% of catalyst loading, 11.62 : 1 of methanol to oil molar ratio and 4.47 min of reaction time. Experimental validation of the optimum conditions showed an excellent agreement, with a minimum deviation of 0.18% from three replicates. The biodiesel produced in this work also met the specification of ASTM D6751.
引用
收藏
页码:76743 / 76751
页数:9
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