Monoglycerides reduction in rapeseed oil transesterification for production of high quality biodiesel

被引:1
作者
Islam, Mohammad Shahidul [1 ]
Bundy, Christian [1 ]
Choudhury, M. A. A. S. [1 ]
机构
[1] Bangladesh Univ Engn & Technol, Dept Chem Engn, Dhaka 1000, Bangladesh
关键词
biodiesel; gas chromatography; kinetics; monoglycerides; transesterification; KINETICS;
D O I
10.1504/IJOGCT.2014.064428
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Monoglycerides are intermediate by products in rapeseed oil transesterification. If they are present in the bio-fuel and the bio-fuel is used in vehicles, then they can form crystal at cold climate and block fuel injection system of the vehicles. To solve this problem kinetic study of transesterification of rapeseed oil has been carried out in this study. The process variables such as reaction time, temperature, agitation speed and molar ratio of methanol to oil have been optimised to achieve a reduced level of monoglycerides formation in a batch reactor. These information have been integrated into flow through industrial scale transesterification process. Industrial processes demonstrated a steady performance with reduced level of monoglycerides. Monoglycerides level have been reduced to 0.27% (w/w) using 9:1 molar ratio of methanol to oil in about 40 min reaction time. KOH was used as a catalyst to influence transesterification. Results from this study will be helpful to reduce monoglycerides in the industrial scale transesterification process.
引用
收藏
页码:104 / 116
页数:13
相关论文
共 11 条
[1]  
Cabral M, 2007, WHITE PAPER INT COMP, P29
[2]  
Dhanasekaran Krishnan Dhanasekaran Krishnan, 2012, African Journal of Biotechnology, V11, P9797, DOI 10.5897/AJB12.507
[3]  
Encinar J.M., 2010, 3 INT S EN BIOM WAST, P1
[4]  
Goosen R., 2007, 022007A APEC EWG, P30
[5]   Modeling Cryptosporidium parvum oocyst inactivation and bromate in a flow-through ozone contactor treating natural water [J].
Kim, Jae-Hong ;
Elovitz, Michael S. ;
von Gunten, Urs ;
Shukairy, Hiba M. ;
Marinas, Benito J. .
WATER RESEARCH, 2007, 41 (02) :467-475
[6]  
Ma F, 1998, T ASAE, V41, P1261, DOI 10.13031/2013.17292
[7]   Kinetics of transesterification of soybean oil [J].
Noureddini, H ;
Zhu, D .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1997, 74 (11) :1457-1463
[8]  
Poljansek I., 2011, INFLULENCE MASS TRAN
[9]   OPTIMIZATION OF VANDEVUSSE REACTION-KINETICS USING SEMIBATCH REACTOR OPERATION [J].
RIDLEHOOVER, GA ;
SEAGRAVE, RC .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1973, 12 (04) :444-447
[10]  
Susilo B., 2011, ADV NATURAL APPL SCI, V5, P252