Journal of Molecular Catalysis A: Chemical 379 (2013) 234–242
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Journal of Molecular Catalysis A: Chemical
j ourna l ho me pa g e: www.elsevier.com/locate/molcata
Catalytic properties of spinel-type mixed oxides in transesterification
of vegetable oils
T.M. Sankaranarayanan
a,b,∗
, R. Vijaya Shanthi
a
, K. Thirunavukkarasu
a
,
A. Pandurangan
b
, S. Sivasanker
a
a
National Centre for Catalysis Research, Indian Institute of Technology, Chennai 600 036, India
b
Department of Chemistry, Anna University, Chennai 600 025, India
a r t i c l e i n f o
Article history:
Received 10 July 2013
Received in revised form 23 August 2013
Accepted 24 August 2013
Available online 4 September 2013
Keywords:
Spinels
ZnFe2O4
Biodiesel
Transesterification
Vegetable oils
a b s t r a c t
Crystalline mixed oxides of AB
2
O
4
composition, where A = Co, Ni, Cu and Zn and B = Al, Fe and Co, were
prepared by co-precipitation of hydroxides and calcination at 873 K. The catalytic activity of these mate-
rials in the transesterification of sunflower oil with methanol to produce fatty acid mono esters (FAME;
biodiesel) was investigated. The transesterification activity was found to depend on element A, the order
of activity being: Zn > Cu > Ni > Co. The Zn containing spinels were more active than the others and their
activity was found to go through a maximum with Sanderson’s intermediate electronegativity. Detailed
investigations carried out on ZnFe
2
O
4
revealed it to be a suitable solid catalyst for the transesterification
of used cooking oil and Jatropha oil. The catalyst was reusable many times. The performance of this spinel
was also investigated in a bench-scale (30 g catalyst loading) fixed-bed reactor.
Crown Copyright © 2013 Published by Elsevier B.V. All rights reserved.
1. Introduction
The use of renewable transportation fuels made from biomass,
such as ethanol and fatty acid methyl esters (FAME), is slowly
increasing over the years due to concerns regarding atmospheric
CO
2
build up and depletion of fossil fuels. The transesterification of
vegetable oils is at present mostly carried out using soluble alkali
catalysts. The disadvantages of using alkali catalysts are soap for-
mation, poor quality of byproduct glycerol, waste water generation
and non-suitability for oils containing free fatty acids (FFA). There-
fore, search for solid acid catalysts that can transform non-edible
oils and those with FFA have been on for many years.
Many solid catalysts have been reported to be suitable for
the reaction [1–5]. A few representative, recently reported solid
catalysts are double metal cyanides [6], heteropoly acid/zirconia
[7], Amberlyst, Nafion [8,9], basic zeolites [10], supported metal
hydroxides and salts [11–13] and mixed metal oxides [14–18]. A
fixed-bed process based on zinc-aluminate (ZnAl
2
O
4
) was devel-
oped for transesterification by the Institut Francais du Petrole (IFP)
and was commercialized by Axens [19]. Pugnet et al. and Alves
∗
Corresponding author at: National Centre for Catalysis Research, Indian Institute
of Technology, Chennai 600 036, India. Tel.: +91 44 2257 4238;
fax: +91 44 2257 5245.
E-mail addresses: tmsankaranarayanan@gmail.com,
tms2003@rediffmail.com (T.M. Sankaranarayanan).
et al. have also reported the transesterification of vegetable oil over
ZnAl
2
O
4
[20,21]. Spinel-type oxides possess many advantages, such
as good thermal stability, good chemical stability preventing their
dissolution during reaction, and ease of preparation with reason-
ably large external areas.
We now present our studies on the performance of a number
of other spinels as catalysts for the transesterification of vegetable
oils with and without free fatty acids (FFA) carried out as part of our
continuing research on the transesterification of vegetable oils with
solid oxide catalysts [22]. The spinel-type oxides investigated are
CuAl
2
O
4
, NiAl
2
O
4
, CoAl
2
O
4
, ZnFe
2
O
4
, NiFe
2
O
4
and ZnCo
2
O
4
. Addi-
tionally, a comparison of the catalytic activities of the above spinels
is also made with that of the already reported ZnAl
2
O
4
. All the com-
pounds were prepared by a co-precipitation method and not by
blending of the component oxides [20]. These were characterized
by physicochemical methods and their activity in the transesteri-
fication of sunflower oil with methanol was evaluated in a batch
reactor. The transesterification of used cooking oil and Jatropha
oil was also evaluated over ZnFe
2
O
4
. Additionally, the activity of
ZnFe
2
O
4
was examined using a fixed-bed bench scale reactor.
2. Experimental
2.1. Materials used and preparation of catalysts
Cooking grade sunflower oil, waste (used) sunflower oil and Jat-
ropha oil were procured locally. Their fatty acid compositions are
1381-1169/$ – see front matter. Crown Copyright © 2013 Published by Elsevier B.V. All rights reserved.
http://dx.doi.org/10.1016/j.molcata.2013.08.027