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Catalysis Communications
journal homepage: www.elsevier.com/locate/catcom
Short communication
N
2
O-assisted methanol selective oxidation to formaldehyde on cobalt oxide
catalysts derived from layered double hydroxides
Oséas S. Santos
a
, Artur J.S. Mascarenhas
a,b
, Heloysa M.C. Andrade
a,b,
⁎
a
Laboratório de Catálise e Materiais, Departamento de Química Geral e Inorgânica, Instituto de Química, Universidade Federal da Bahia, Trav. Barão de Jeremoabo, 147,
Campus de Ondina, 40170-280 Salvador, BA, Brazil
b
Instituto Nacional de Ciência e Tecnologia em Energia e Ambiente (INCT – E&A), Centro Interdisciplinar de Energia e Ambiente (CIENAM), Campus de Ondina, 40170-
115 Salvador, BA, Brazil
ARTICLE INFO
Keywords:
Nitrous oxide (N
2
O)
Selective oxidation of methanol
Formaldehyde
Layered double hydroxides (LDH)
ABSTRACT
Cobalt-magnesium-aluminum oxides derived from layered double hydroxides were used as catalysts for the
conversion of methanol to formaldehyde in the presence of nitrous oxide. The catalysts were characterized by
XRD, FTIR, UV–vis DRS, TPR-H
2
, NH
3
- and CO
2
-TPD and N
2
adsorption. 100% methanol conversion and 91%
selectivity to formaldehyde were simultaneously obtained with 100% N
2
O conversion at 440 °C over a Co,Mg,Al-
mixed oxide catalyst. Higher hydrogen yields and lower CO and CO
2
yields were obtained than when air was
used as oxidizing agent, under the same conditions. These findings suggest that the reaction occurs on a com-
bination of redox and basic catalytic sites.
1. Introduction
Nitrous oxide (N
2
O) is an environmental pollutant that contributes
to the greenhouse effect and destruction of ozone in the stratosphere.
Due to the high thermal decomposition temperature of N
2
O, which
occurs above 600 °C [1,2], the use of efficient catalysts is necessary to
conduct this reaction, thus ensuring the minimization of atmospheric
emissions from anthropogenic sources, such as nitric acid and adipic
acid industrial plants. Alternatively, the use of N
2
O as oxidant agent for
hydrocarbon conversion to useful products is an interesting strategy to
mitigate these emissions and develop new technologies [3–5].
About 32% of the methanol produced worldwide is consumed in the
production of formaldehyde [6], therefore the use of N
2
O as oxidant
agent to selectively produce formaldehyde is of great technological and
environmental interest.
Two main classes of catalysts are employed in the partial oxidation
of methanol to formaldehyde: (i) silver catalysts, operating in the
temperature range of 580–650 °C; or (ii) iron-molybdenum catalysts
operating in the temperature range of 400 °C [7–10]. Based on a DFT
study, M.F. Fellah [11] showed that the direct oxidation of methanol to
formaldehyde using N
2
O would be possible on [Fe-O]
+
species in Fe-
ZSM-5. Khan et al. [4] reported on the use of Co-ZSM-5 catalysts to
partially oxidize methane to synthesis gas using N
2
O as oxidant. In early
papers, Co-ZSM-5 and Co-oxides derived from hydrotalcites (LDH) were
reported as efficient catalysts for decomposition of N
2
O[12,13]. Gen-
nequin et al. [14] used Co,Mg,Al-hydrotalcites as catalyst precursors for
the total oxidation of volatile organic compounds and showed that the
high activity for toluene oxidation of the Co-rich catalysts was related
to the presence of easily reducible Co
3
O
4
particles.
Thus, considering that cobalt catalysts are active both for N
2
O de-
composition and for oxidation reactions, the selective conversion of
methanol to formaldehyde was investigated using N
2
O as oxidant and
Co-oxides derived from hydrotalcites as catalysts in the present study.
2. Experimental
2.1. Catalysts preparation
MgAl (1:1), CoAl (1:1), CoMgAl (1:2:1) and CoMgAl (2:1:1) LDH
samples were prepared by coprecipitation, using solutions of the metal
nitrates and Na
2
CO
3
/NaOH solution, at pH = 11 [14]. The gels were
aged at 80 °C for 24 h, then filtered and washed with distilled water
until the pH was 10. The LDH samples were calcined at 600 °C in air for
4 h before reaction, obtaining the mixed oxide, respectively named as
MgAl, CoAl, CoMgAl-1 and CoMgAl-2.
https://doi.org/10.1016/j.catcom.2018.05.014
Received 7 April 2018; Received in revised form 21 May 2018; Accepted 22 May 2018
⁎
Corresponding author at: Laboratório de Catálise e Materiais, Departamento de Química Geral e Inorgânica, Instituto de Química, Universidade Federal da Bahia, Trav. Barão de
Jeremoabo, 147, Campus de Ondina, 40170-280 Salvador, BA, Brazil.
E-mail address: handrade@ufba.br (H.M.C. Andrade).
Catalysis Communications 113 (2018) 32–35
Available online 23 May 2018
1566-7367/ © 2018 Elsevier B.V. All rights reserved.
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