TY - GEN
T1 - Production of biodiesel in supercritical methanol and related correlation on phase equilibrium
AU - Zeng, Dan
AU - Li, Yang
AU - Fang, Tao
PY - 2012
Y1 - 2012
N2 - Biodiesel was prepared by methyl esterification and effects of different reaction conditions on the yield of fatty acid methyl esters (FAMEs) were investigated. The result of the orthogonal experiment analysis shows that the order of influential factors is ranked as reaction temperature > methanol-to-soybean-oil (M/O) ratio > reaction time. The maximum yield of 94.8 % has been achieved by reacting supercritical methanol and soybean oil in M/O ratio 4:2 (v/v) at 573 K for 45 min. Moreover, the higher M/O ratio, the higher yield of FAMEs will be obtained. At the temperature ranging from 533 k to 573 k, the yield rises significantly; however, since soybean oil decomposes over 573 K, the yield decreases oppositely. Time longer than 45 min has less effect on the final yield. In addition, the phase equilibrium data of supercritical methanol + C12 methyl esters and supercritical methanol + C18 methyl esters were separately correlated using the Peng-Robinson (PR) equation of state (EOS) with the Adachi-Sugie (AS) mixing rule.
AB - Biodiesel was prepared by methyl esterification and effects of different reaction conditions on the yield of fatty acid methyl esters (FAMEs) were investigated. The result of the orthogonal experiment analysis shows that the order of influential factors is ranked as reaction temperature > methanol-to-soybean-oil (M/O) ratio > reaction time. The maximum yield of 94.8 % has been achieved by reacting supercritical methanol and soybean oil in M/O ratio 4:2 (v/v) at 573 K for 45 min. Moreover, the higher M/O ratio, the higher yield of FAMEs will be obtained. At the temperature ranging from 533 k to 573 k, the yield rises significantly; however, since soybean oil decomposes over 573 K, the yield decreases oppositely. Time longer than 45 min has less effect on the final yield. In addition, the phase equilibrium data of supercritical methanol + C12 methyl esters and supercritical methanol + C18 methyl esters were separately correlated using the Peng-Robinson (PR) equation of state (EOS) with the Adachi-Sugie (AS) mixing rule.
KW - Biodiesel
KW - Methyl esterification
KW - Phase equilibrium
KW - Supercritical methanol
UR - https://www.scopus.com/pages/publications/84867263231
U2 - 10.4028/www.scientific.net/AMR.560-561.555
DO - 10.4028/www.scientific.net/AMR.560-561.555
M3 - 会议稿件
AN - SCOPUS:84867263231
SN - 9783037854600
T3 - Advanced Materials Research
SP - 555
EP - 562
BT - Material Sciences and Technology
T2 - 2012 Spring International Conference on Material Sciences and Technology, MST-S
Y2 - 27 May 2012 through 30 May 2012
ER -