Effects of water on the esterification of free fatty acids by acid catalysts

被引:118
作者
Park, Ji-Yeon [1 ]
Wang, Zhong-Ming [2 ]
Kim, Deog-Keun [1 ]
Lee, Jin-Suk [1 ]
机构
[1] Korea Inst Energy Res, Taejon 305343, South Korea
[2] Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
关键词
Soapstock; Esterification; Water production; Amberlyst-15; Sulfuric acid; BIODIESEL PRODUCTION; DIESEL FUEL; HIGH FFA; OIL; METHANOL; OPTIMIZATION;
D O I
10.1016/j.renene.2009.08.007
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
To maximize the production of biodiesel from soybean soapstock, the effects of water on the esterification of high-FFA (free fatty acid) oils were investigated. Oleic acid and high acid acid oil (HAAO) were esterified by reaction with methanol in the presence of Amberlyst-15 as a heterogeneous catalyst or sulfuric acid as a homogeneous catalyst. The yield of fatty acid methyl ester (FAME) was studied at oil to methanol molar ratios of 1:3 and 1:6 and reaction temperatures of 60 and 80 degrees C. The rate of esterification of oleic acid significantly decreased as the initial water content increased to 20% of the oil. The activity of Amberlyst-15 decreased more rapidly than that of sulfuric acid, due to the direct poisoning of acid sites by water. Esterification using sulfuric acid was not affected by water until there was a 5% water addition at a 1:6 molar ratio of oil to methanol. FAME content of HAAO prepared from soapstock rapidly increased for the first 30 min of esterification. Following the 30-min mark, the rate of FAME production decreased significantly due to the accumulation of water. When methanol and Amberlyst-15 were removed from the HAAO after 30 min of esterification and fresh methanol and a catalyst were added, the time required to reach 85% FAME content was reduced from 6 h to 1.8 h. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:614 / 618
页数:5
相关论文
共 20 条
[1]   Liquid phase synthesis of MTBE from methanol and isobutene over acid zeolites and amberlyst-15 [J].
Collignon, F ;
Loenders, R ;
Martens, JA ;
Jacobs, PA ;
Poncelet, G .
JOURNAL OF CATALYSIS, 1999, 182 (02) :302-312
[2]   Continuous zeolite membrane reactor for esterification of ethanol and acetic acid [J].
de la Iglesia, Oscar ;
Mallada, Reyes ;
Menendez, Miguel ;
Coronas, Joaquin .
CHEMICAL ENGINEERING JOURNAL, 2007, 131 (1-3) :35-39
[3]   Process optimization for biodiesel production from mahua (Madhuca indica) oil using response surface methodology [J].
Ghadge, SV ;
Raheman, H .
BIORESOURCE TECHNOLOGY, 2006, 97 (03) :379-384
[4]   A process model to estimate biodiesel production costs [J].
Haas, MJ ;
McAloon, AJ ;
Yee, WC ;
Foglia, TA .
BIORESOURCE TECHNOLOGY, 2006, 97 (04) :671-678
[5]   Improving the economics of biodiesel production through the use of low value lipids as feedstocks: vegetable oil soapstock [J].
Haas, MJ .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (10) :1087-1096
[6]   Simple, high-efficiency synthesis of fatty acid methyl esters from soapstock [J].
Haas, MJ ;
Bloomer, S ;
Scott, K .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2000, 77 (04) :373-379
[7]   Production of FAME from acid oil, a by-product of vegetable oil refining [J].
Haas, MJ ;
Michalski, PJ ;
Runyon, S ;
Nunez, A ;
Scott, KM .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2003, 80 (01) :97-102
[8]   Reduction of energy consumption in biodiesel fuel life cycle [J].
Janulis, P .
RENEWABLE ENERGY, 2004, 29 (06) :861-871
[9]   Using of cotton oil soapstock biodiesel-diesel fuel blends as an alternative diesel fuel [J].
Keskin, Ali ;
Guerue, Metin ;
Altiparmak, Duran ;
Aydin, Kadir .
RENEWABLE ENERGY, 2008, 33 (04) :553-557
[10]  
LEE JS, 2006, 2AB31 RES REC R D, P112