Sub- and supercritical esterification of palm fatty acid distillate with carbohydrate-derived solid acid catalyst

被引:45
作者
Lokman, Ibrahim M. [1 ,2 ,3 ]
Goto, Motonobu [4 ]
Rashid, Umer [5 ]
Taufiq-Yap, Yun Hin [1 ,2 ]
机构
[1] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Upm Serdang 43400, Selangor, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Dept Chem, Upm Serdang 43400, Selangor, Malaysia
[3] Univ Teknol MARA, Fac Sci Appl, Sch Chem, Shah Alam 40450, Selangor, Malaysia
[4] Nagoya Univ, Dept Chem Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
[5] Univ Putra Malaysia, Inst Adv Technol, Upm Serdang 43400, Selangor, Malaysia
关键词
Esterification; Supercritical methanol; Palm fatty acid distillate; Carbohydrate-derived solid acid catalyst; Fatty acid methyl ester; BIODIESEL PRODUCTION; CARBON CATALYST; VEGETABLE-OILS; METHYL-ESTERS; RAPESEED OIL; TRANSESTERIFICATION; CONVERSION; METHANOL; FUEL; OPTIMIZATION;
D O I
10.1016/j.cej.2015.08.102
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The esterification of palm fatty acid distillate (PFAD) in supercritical methanol was investigated by using carbohydrate-derived solid acid catalyst. The catalysts were prepared by sulfonation of incomplete carbonized glucose and starch, which had been coded as sulfonated-ICG and sulfonated-ICS, respectively. The contents of fatty acid methyl ester (FAME) and its yield were determined by using gas chromatography techniques. The effects of sub- and supercritical operating conditions such as methanol/PFAD molar ratio, catalyst amount, reaction temperature and reaction time were analyzed to determine their optimum operating conditions. At optimum reaction temperature of 290 degrees C, methanol/PFAD molar ratio of 6/1, catalyst amount of 1 wt.% and 5 min reaction time, the esterification of PFAD in supercritical methanol with the presence of sulfonated-ICS and -ICG catalysts resulted 97.3% and 95.4% of FAME; both catalysts yield significantly higher percentages compared to uncatalyzed reaction. Alongside of its potential in enhancing the efficiency of production process, the utilization of carbohydrate-derived solid acid catalyst in supercritical methanol method had also resulting fast reaction and energy saving. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:872 / 878
页数:7
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