Please cite this article in press as: H. Pérez, et al., Evaluation of manganese OMS-like cryptomelane supported on SBA-15 in the oxidation of ethyl
acetate, Catal. Today (2012), http://dx.doi.org/10.1016/j.cattod.2012.09.022
ARTICLE IN PRESS
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CATTOD-8249; No. of Pages 8
Catalysis Today xxx (2012) xxx–xxx
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Catalysis Today
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Evaluation of manganese OMS-like cryptomelane supported on SBA-15 in the
oxidation of ethyl acetate
Hermicenda Pérez
a,b
, Paloma Navarro
a,∗
, Gilberto Torres
b
, Oihane Sanz
a
, Mario Montes
a
a
Department of Applied Chemistry, University of the Basque Country (UPV-EHU), Apdo. 1072, 20080 San Sebastián, Spain
b
Academic Division of Basic Science, Autonomous University Juárez of Tabasco, Km. 1, Road Cuanduacán-Jalpa de Méndez, A.P. 24, C.P. 86690, Cuanduacán, Tabasco, Mexico
a r t i c l e i n f o
Article history:
Received 15 March 2012
Received in revised form
14 September 2012
Accepted 24 September 2012
Available online xxx
Keywords:
Catalytic VOC abatement
Cryptomelane
Manganese oxides
Supported manganese catalysts
SBA-15
a b s t r a c t
We report the synthesis of four manganese catalysts supported on SBA-15 via a multistep impregnation
method. The successive impregnations allowed as much as 13.8% manganese to be deposited without
loss of the mesoporous structure of the SBA-15, although the surface area of the catalysts and their pore
size distributions were lower than those of the pure SBA-15. The data obtained using different analysis
techniques indicate that the manganese was incorporated into the pure SBA-15 in different positions:
grafted onto the internal surface of the walls, incorporated into the framework of the SBA-15 and on the
external surface and at the pores mouth of the SBA-15, which partially blocked the porosity. The XRD
results showed that cryptomelane phase was formed in all of the catalysts; the remaining P123 in the
SBA-15 structure and the presence of K
+
during the impregnation most likely favored the formation of
the cryptomelane phase. Total oxidation of ethyl acetate in air was obtained at temperatures less than
350
◦
C for all of the catalysts.
© 2012 Elsevier B.V. All rights reserved.
1. Introduction
Volatile organic compounds (VOCs) are major organic atmo-
spheric pollutants. The emission of VOCs is being subjected to
stricter legislation, and, although the prevention of emissions
would be the most desirable strategy to control VOCs, such pre-
vention is often not feasible; thus, the destruction of VOCs is an
alternative. Incineration and catalytic oxidation are the most com-
monly used techniques to treat VOC-contaminated streams. Simple
incineration requires high temperatures (800–1150
◦
C) and can
produce incomplete oxidation products that are also dangerous.
In contrast, catalytic oxidation can typically be achieved in the
temperature range of 200–500
◦
C depending on the nature of the
molecule. Furthermore, this technique can be applied effectively
at low cost to a wide concentration range of VOCs. Therefore, cat-
alytic oxidation appears to be a good alternative for the complete
elimination of VOCs.
Noble metals like Pt or Pd supported on alumina or silica are
widely used for VOC abatement. However, these catalysts are not
only expensive, but are also susceptible to sintering and poison-
ing. An additional difficulty in the treatment of VOCs arises from
∗
Corresponding author. Present address: Institute of Catalysis and Petroleochem-
istry of the Spanish Council for Scientific Research (ICP-CSIC), Marie Curie Street 2,
Cantoblanco, 28049 Madrid, Spain. Tel.: +34 91 585 4793.
E-mail address: pnavarro@icp.csic.es (P. Navarro).
the fact that streams generally contain a mixture of organic com-
pounds of different chemical nature, and the catalyst must be able
to oxidize them simultaneously. Therefore, because the activity
of a catalyst largely depends on the nature of the molecule to be
oxidized, the design of adequate catalysts for specific processes
has been the focus of numerous investigations. Investigations that
involve metal-oxide catalysts instead of the more commonly used
noble-metal catalysts are becoming relevant, and such investiga-
tions have focused on manganese because of its low cost and good
performance in the oxidation of some VOCs [1,2]. For example, ethyl
acetate has been reported to be more readily oxidized on MnO
2
than
on Pt/Al
2
O
3
[3,4].
The synthesis of MnO
x
phases have been studied for a long time,
and the literature shows that the nature of these MnO
x
catalysts
depends strongly on the precursor used, the thermal treatment
given and the support itself [5,6]. Nevertheless, the synthesis and
characterization of these materials still attract considerable atten-
tion from both academia and industry [7,8].
Catalytic supports should have a high surface area to improve
dispersion of the active phase, which is why mesoporous molecular
sieves (MMSs) have attracted so much interest since their discov-
ery [9,10]. Mesoporous materials, such as MCM-41 and SBA-15,
exhibit high surface areas (500–1000 m
2
/g) and a hexagonal array
of uniform cylindrical mesopores with diameters that can be tailo-
red from 5 nm to 30 nm. However, the purely siliceous MMS show
limited catalytic applications because they lack acidity. Therefore,
the incorporation of various metals into their frameworks has been
0920-5861/$ – see front matter © 2012 Elsevier B.V. All rights reserved.
http://dx.doi.org/10.1016/j.cattod.2012.09.022