Continuous biodiesel production using a fixed-bed Lewis-based catalytic system

被引:18
作者
da Silva, Fabio M. [1 ]
Pinho, David M. M. [1 ]
Houg, Guilherme P. [1 ]
Reis, Ivan B. A. [1 ]
Kawamura, Mayume [1 ]
Quemel, Mariana S. R. [1 ]
Montes, Pedro R. [1 ]
Suarez, Paulo A. Z. [1 ]
机构
[1] Univ Brasilia, Inst Quim, Lab Mat & Combust, BR-70910900 Brasilia, DF, Brazil
关键词
Biodiesel; Process development; Pilot plant; Fixed bed; Heterogeneous catalysts; Zinc oxide; SOYBEAN OIL; TRANSESTERIFICATION; PYROLYSIS; SURFACE;
D O I
10.1016/j.cherd.2014.04.024
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
It was developed a fixed bed tubular continuous reactor to produce biodiesel, using pellets of aluminum oxide doped with zinc oxide. The pellets were placed into a tubular reactor as a 30 cm long column (2.65 kg). The reactor was feed with soybean oil (168 g h(-1)) and methanol or ethanol (89 g h(-1)) with the temperature fixed at 100 degrees C. Under these conditions it was possible to convert soybean oil into biodiesel in up to 75% yield in the case of methanol and 35% for ethanol. Increasing the temperature to 180 degrees C, it was possible to ethanolise soybean oil with yields up to 78%. It is important to note that after a steady state is achieved the conversions remained approximately constant with time. It is also worth to mention that the fixed bed remained active for more than 120 h, showing no catalyst leaching or deactivation, and so far it was not possible to determine its overall productivity. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1463 / 1469
页数:7
相关论文
共 23 条
[1]   Heats of combustion of biofuels obtained by pyrolysis and by transesterification and of biofuel/diesel blends [J].
DeOliveira, Edimar ;
Quirino, Rafael L. ;
Suarez, Paulo A. Z. ;
Prado, Alexandre G. S. .
THERMOCHIMICA ACTA, 2006, 450 (1-2) :87-90
[2]   Heterogeneous catalysts for biodiesel production [J].
Di Serio, Martino ;
Tesser, Riccardo ;
Pengmei, Lu ;
Santacesaria, Elio .
ENERGY & FUELS, 2008, 22 (01) :207-217
[3]   Comparing biofuels obtained from pyrolysis, of soybean oil or soapstock, with traditional soybean biodiesel: Density, kinematic viscosity, and surface tensions [J].
Doll, Kenneth A. ;
Sharma, Brajendra K. ;
Suarez, Paulo A. Z. ;
Erhan, Sevim Z. .
ENERGY & FUELS, 2008, 22 (03) :2061-2066
[4]   Tetramethylguanidine covalently bonded onto silica gel surface as an efficient and reusable catalyst for transesterification of vegetable oil [J].
Faria, Elaine A. ;
Ramalho, Hugo F. ;
Marques, Jessica S. ;
Suarez, Paulo A. Z. ;
Prado, Alexandre G. S. .
APPLIED CATALYSIS A-GENERAL, 2008, 338 (1-2) :72-78
[5]   TRANSESTERIFICATION KINETICS OF SOYBEAN OIL [J].
FREEDMAN, B ;
BUTTERFIELD, RO ;
PRYDE, EH .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1986, 63 (10) :1375-1380
[6]   VARIABLES AFFECTING THE YIELDS OF FATTY ESTERS FROM TRANSESTERIFIED VEGETABLE-OILS [J].
FREEDMAN, B ;
PRYDE, EH ;
MOUNTS, TL .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1984, 61 (10) :1638-1643
[7]  
Hillion G., 2004, US Pat., Patent No. 0234448
[8]   Continuous production of biodiesel in a packed-bed reactor using shell-core structural Ca(C3H7O3)2/CaCO3 catalyst [J].
Hsieh, Li-Shan ;
Kumar, Umesh ;
Wu, Jeffery C. S. .
CHEMICAL ENGINEERING JOURNAL, 2010, 158 (02) :250-256
[9]   Production of algae-based biodiesel using the continuous catalytic Mcgyan® process [J].
Krohn, Brian J. ;
McNeff, Clayton V. ;
Yan, Bingwen ;
Nowlan, Daniel .
BIORESOURCE TECHNOLOGY, 2011, 102 (01) :94-100
[10]  
Macedo CCS, 2006, J BRAZIL CHEM SOC, V17, P1291