Synthesis of methyl esters from relevant palm products in near-critical methanol with modified-zirconia catalysts

被引:48
作者
Laosiripojana, N. [1 ]
Kiatkittipong, W. [2 ]
Sutthisripok, W. [3 ]
Assabumrungrat, S. [4 ]
机构
[1] King Mongkuts Univ Technol, Joint Grad Sch Energy & Environm, Thonburi, Thailand
[2] Silpakorn Univ, Dept Chem Engn, Fac Engn & Ind Technol, Nakhon Pathom 73000, Thailand
[3] Prince Songkla Univ, Fac Engn, Dept Min & Mat Engn, Hat Yai, Thailand
[4] Chulalongkorn Univ, Fac Engn, Dept Chem Engn, Bangkok 10330, Thailand
关键词
Transesterification; Esterification; Tungsten zirconia; Palm oil; BIODIESEL FUEL PRODUCTION; SOLID ACID; RAPESEED OIL; SUPERCRITICAL METHANOL; TRANSESTERIFICATION; ESTERIFICATION; WATER; KOH;
D O I
10.1016/j.biortech.2010.05.076
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The transesterification and esterification of palm products i.e. crude palm oil (CPO), refined palm oil (RPO) and palm fatty acid distillate (PFAD) under near-critical methanol in the presence of synthesized SO4-ZrO2, WO3-ZrO2 and TiO2-ZrO2 (with various sulfur- and tungsten loadings, Ti/Zr ratios, and calcination temperatures) were studied. Among them, the reaction of RPO with 20%WO3-ZrO2 (calcined at 800 degrees C) enhanced the highest fatty acid methyl ester (FAME) yield with greatest stability after several reaction cycles; furthermore, it required shorter time, lower temperature and less amount of methanol compared to the reactions without catalyst. These benefits were related to the high acid-site density and tetragonal phase formation of synthesized WO3-ZrO2. For further improvement, the addition of toluene as co-solvent considerably reduced the requirement of methanol to maximize FAME yield, while the addition of molecular sieve along with catalyst significantly increased FAME yield from PFAD and CPO due to the inhibition of hydrolysis reaction. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:8416 / 8423
页数:8
相关论文
共 28 条
[1]  
Anthonsen T, 2000, METH TOOLS BIOSCI ME, P14
[2]  
Canakci M, 1999, T ASAE, V42, P1203, DOI 10.13031/2013.13285
[3]   Solid acid catalysts [J].
Corma, A .
CURRENT OPINION IN SOLID STATE & MATERIALS SCIENCE, 1997, 2 (01) :63-75
[4]   Biodiesel from sunflower oil in supercritical methanol with calcium oxide [J].
Demirbas, Ayhan .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (03) :937-941
[5]   Biodiesel fuel production with solid superacid catalysis in fixed bed reactor under atmospheric pressure [J].
Furuta, S ;
Matsuhashi, H ;
Arata, K .
CATALYSIS COMMUNICATIONS, 2004, 5 (12) :721-723
[6]   Transesterfication of soybean oil catalyzed by sulfated ziconia [J].
Garcia, Camila Martins ;
Teixeira, Sergio ;
Marciniuk, Leticia Ledo ;
Schuchardt, Ulf .
BIORESOURCE TECHNOLOGY, 2008, 99 (14) :6608-6613
[7]   ISOMERIZATION OF ALKANES ON SULFATED ZIRCONIA - PROMOTION BY PT AND BY ADAMANTYL HYDRIDE TRANSFER SPECIES [J].
IGLESIA, E ;
SOLED, SL ;
KRAMER, GM .
JOURNAL OF CATALYSIS, 1993, 144 (01) :238-253
[8]   Biodiesel production from rice bran oil and supercritical methanol [J].
Kasim, Novy Srihartati ;
Tsai, Tsung-Han ;
Gunawan, Setiyo ;
Ju, Yi-Hsu .
BIORESOURCE TECHNOLOGY, 2009, 100 (08) :2399-2403
[9]   Competitive transesterification of soybean oil with mixed methanol/ethanol over heterogeneous catalysts [J].
Kim, M. ;
Yan, S. ;
Salley, S. O. ;
Ng, K. Y. S. .
BIORESOURCE TECHNOLOGY, 2010, 101 (12) :4409-4414
[10]   The heterogeneous advantage: biodiesel by catalytic reactive distillation [J].
Kiss, Anton A. ;
Omota, Florin ;
Dimian, Alexandre C. ;
Rothenberg, Gadi .
TOPICS IN CATALYSIS, 2006, 40 (1-4) :141-150