Catalysis Today 198 (2012) 338–344
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Catalysis Today
j ourna l ho me p ag e: www.elsevier.com/lo cate/cattod
Catalytic study of the conversion of ethanol into 1,3-butadiene
E.V. Makshina, W. Janssens, B.F. Sels
∗
, P.A. Jacobs
Centre for Surface Chemistry and Catalysis, Faculty of Bioscience Engineering, KU Leuven, Kasteelpark Arenberg, 23, Box 2461, 3001 Heverlee, Belgium
a r t i c l e i n f o
Article history:
Received 27 February 2012
Received in revised form 2 May 2012
Accepted 5 May 2012
Available online 21 June 2012
Keywords:
Ethanol
1,3-Butadiene
Biomass conversion
Magnesia–silica catalyst
Silver catalysts
Multifunctional catalysis
a b s t r a c t
Direct synthesis of 1,3-butadiene (BD) from ethanol has been studied using magnesia–silica catalysts
doped with transition metal(oxide)s. The effects of Mg/Si ratio, the synthesis procedure, and the dopant
concentration were studied. It was demonstrated that modification of the magnesia–silica binary system
using a consecutive impregnation step significantly increases the ethanol conversion rate and BD yield.
The BD yield higher than 55 mol.% was obtained at full ethanol conversion for materials containing Cu
and Ag modifiers. The influence of the reaction temperature and the ethanol concentration in the feed
was also investigated. This investigation led to high BD productivity (>0.15 g
BD
g
cat
-1
h
-1
) and high BD
concentration in the product stream (>10,000 Vppm).
© 2012 Elsevier B.V. All rights reserved.
1. Introduction
Today 1,3-butadiene (BD) is an important building block
for the chemical industry. The polymerization of BD with
itself and with other olefin monomers represents its largest
commercial use. The commercially most important polymers
are styrene–butadiene rubbers, polybutadiene, styrene–butadiene
latex, acrylonitrile–butadiene–styrene polymer and nitrile rubber.
Since the early seventies, the dominant technology for producing
BD is the cracking of naphtha, where BD is obtained as a co-
product. As the growth of ethylene production outpaced the growth
of BD demand, the oversupply of BD led to shut down of the all
on-purpose BD production technologies. The recent trends in light-
ening of the feedstock of steam crackers reduce BD supply and may
potentially lead to a shortage in BD production in coming years.
Currently a lot of attention is paid to the usage of alternative
and renewable resources for fuels and chemicals. Due to politi-
cal incitements as well as emerging tax policies, there is a huge
incentive to use monomers from biological origin. Ethanol is one of
the most relevant potential sources of “bio”-carbon today [1]. Pro-
duction of bioethanol occurs via fermentation and is industrially
applied with sugar and corn feedstocks, while the second genera-
tion bioethanol from lignocellulosic feedstock is under extensive
development [2]. Catalytic conversion of ethanol into BD is an
old industrially proven route. From the 1920s to the early 1960s,
∗
Corresponding author. Tel.: +32 16321593; fax: +32 16321998.
E-mail addresses: ekaterina.makshina@biw.kuleuven.be (E.V. Makshina),
bert.sels@biw.kuleuven.be (B.F. Sels), pierre.jacobs@biw.kuleuven.be (P.A. Jacobs).
ethanol was converted to BD, hydrogen, and water at 400–450
◦
C
according to a one-step process developed by Sergey Lebedev using
a variety of (mixed) oxide catalysts [3–5]. High yields with selec-
tivity to BD up to 72 mol.% have been reported [6]. Unfortunately,
these reports did not disclose details concerning the composition of
the catalyst. Simultaneously, Carbide and Carbon Chemicals Corpo-
ration performed the industrial manufacturing of BD from ethanol
in the USA using a two-step process over 2% of tantalum oxide on
silica [7]. This technology, which is also known as Ostromyslen-
sky’s process, included the partial ethanol dehydrogenation to
acetaldehyde, followed by transformation of the mixture of ethanol
and acetaldehyde into BD with 30–35% yield with selectivity
60%.
The mechanism of the ethanol to BD transformation is extremely
complicated and is still subject of debate. However, one gener-
ally accepts the involvement of the following five principal steps
(Fig. 1) [6,8–12]: (1) acetaldehyde formation from ethanol; (2)
aldol condensation of acetaldehyde to acetaldol; (3) dehydration of
acetaldol to crotonaldehyde; (4) Meerwein–Ponndorf–Verley reac-
tion between crotonaldehyde and ethanol to obtain crotyl alcohol
and acetaldehyde; and (5) dehydration of crotyl alcohol to BD. A
possible reaction scheme of the main molecular transformations
is summarized in Fig. 1 [9]. Obviously, such complex reaction net-
work of different reaction types (e.g., dehydration, MPV reduction
and aldol condensation) entails a multifunctional heterogeneous
catalyst with a subtle balance of the amount and strength, and the
ideal proximity of acid/base and redox sites, in order to provide the
ideal kinetics.
Various materials have been proposed as catalysts to per-
form this reaction [9–11,13–31]. Among all catalysts that were
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http://dx.doi.org/10.1016/j.cattod.2012.05.031