High-purity fatty acid methyl ester production from canola, soybean, palm, and yellow grease lipids by means of a membrane reactor

被引:112
作者
Cao, Peigang [1 ]
Dube, Marc A. [1 ]
Tremblay, Andre Y. [1 ]
机构
[1] Univ Ottawa, Dept Chem Engn, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
biodiesel; membrane reactor; transesterification;
D O I
10.1016/j.biombioe.2008.01.020
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
High-purity fatty acid methyl ester (FAME) was produced from different lipids, such as soybean oil, canola oil, a hydrogenated palm oil/palm oil blend, yellow grease, and brown grease, combined with methanol using a continuous membrane reactor. The membrane reactor combines reaction and separation in a single unit, provides continuous mixing of raw materials, and maintains a high molar ratio of methanol to lipid in the reaction loop while maintaining two phases during the reaction. It was demonstrated that the membrane reactor can be operated using a very broad range of feedstocks at highly similar operating conditions to produce FAME. The total glycerine and free glycerine contents of the FAME produced were below the ASTM D6751 standard after a single reaction step. Under essentially the same reaction conditions, a conventional batch reaction was not able to achieve the same degree of FAME purity. The effect of the fatty acid composition of the lipid feedstocks on the FAME purity was also shown. it was demonstrated that, due to the fatty acid composition, FAME from virgin soybean oil and virgin canola oil was produced in the membrane reactor within ASTM specifications even without a water washing step. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1028 / 1036
页数:9
相关论文
共 33 条
[1]   EVALUATION OF TURKISH SULFUR OLIVE OIL AS AN ALTERNATIVE DIESEL FUEL [J].
AKSOY, HA ;
KAHRAMAN, I ;
KARAOSMANOGLU, F ;
CIVELEKOGLU, H .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1988, 65 (06) :936-938
[2]  
Allen D.T., 2001, Green engineering: environmentally conscious design of chemical processes
[3]  
[Anonymous], 2006, Biodiesel Magazine
[4]   Optimisation of biodiesel production by sunflower oil transesterification [J].
Antolín, G ;
Tinaut, FV ;
Briceño, Y ;
Castaño, V ;
Pérez, C ;
Ramírez, AI .
BIORESOURCE TECHNOLOGY, 2002, 83 (02) :111-114
[5]   Single-phase and two-phase base-catalyzed transesterification of canola oil to fatty acid methyl esters at ambient conditions [J].
Ataya, Fadi ;
Dube, Marc A. ;
Ternan, Marten .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (15) :5411-5417
[6]   Fast formation of high-purity methyl esters from vegetable oils [J].
Boocock, DGB ;
Konar, SK ;
Mao, V ;
Lee, C ;
Buligan, S .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1998, 75 (09) :1167-1172
[7]  
Canakci M, 1999, T ASAE, V42, P1203, DOI 10.13031/2013.13285
[8]   Methanol recycling in the production of biodiesel in a membrane reactor [J].
Cao, Peigang ;
Dube, Marc A. ;
Tremblay, Andre Y. .
FUEL, 2008, 87 (06) :825-833
[9]   Effect of membrane pore size on the performance of a membrane reactor for biodiesel production [J].
Cao, Peigang ;
Tremblay, Andre Y. ;
Dube, Marc A. ;
Morse, Katie .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (01) :52-58
[10]   Continuous production of palm methyl esters [J].
Darnoko, D ;
Cheryan, M .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2000, 77 (12) :1269-1272