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FULL PAPER
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2012 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim 1
www.MaterialsViews.com
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Danny Verboekend, Tobias C. Keller, Sharon Mitchell, and Javier Pérez-Ramírez*
1. Introduction
Zeolites are a class of aluminosilicate catalysts of paramount
importance to the chemical and petrochemical industries. Their
unique properties, e.g., strong Brønsted acidity, high surface
area, high (hydro)thermal stability, and shape selectivity, com-
bined with an extensive tunability, render them the catalyst of
choice in many catalyzed reactions.
[1,2]
Nevertheless, often only
a fraction of their potential is exploited, due to diffusion and
access limitations. The size of the micropores (0.3–1 nm) is
similar to that of many molecules, enforcing an intracrystalline
“single file” diffusion. The latter regime is associated with dif-
fusivities orders of magnitude lower compared to outside the
pores, implying an underutilization of the zeolite volume.
[3]
To alleviate diffusion limitations, wide-pore zeolites and hier-
archical zeolites were conceived.
[3–6]
Whereas the former class
aims at enhancing diffusion in the micropores,
[7]
hierarchical
zeolites facilitate access to the active sites
in the micropores using a secondary net-
work of meso- or macropores.
[8–13]
The
increased external surface associated with
hierarchical zeolites renders the crystal
interior more accessible to large mol-
ecules,
[14]
which is particularly advanta-
geous in the catalytic processing of bulky
substrates.
[15]
Hierarchical zeolites can be
obtained by reducing the zeolite crystal
in one or more dimensions, resulting in
nanometer-sized,
[8]
two-dimensional,
[9,10]
or lamellar zeolites,
[11]
or by introducing
intracrystalline mesopores and thereby
forming mesoporous crystals.
[12,13]
Of the plethora of bottom-up and top-
down methods available to prepare hier-
archical zeolites,
[3–13]
base leaching, or
desilication, is widely applied owing to
its experimental simplicity and to the
efficiency of the resulting multiporous
crystal.
[13]
Nevertheless, in many cases, desilication by aqueous
NaOH should be considered only part of the post-synthetic
modification strategy.
[13]
For example, in the case of Y zeo-
lites,
[16]
the execution of a dealumination step prior to base
leaching facilitates the desired formation of intracrystalline
mesopores. Additionally, mild acid washing has proved of cru-
cial importance to remove Al-rich species residual from alka-
line treatment. In the case of steamed and acid-leached USY
zeolites,
[16,17]
the inclusion of pore-directing agents (PDAs) in
the alkaline solution permits the introduction of extensive mes-
oporosity while preventing amorphization. The premeditated
use of these tools has enabled the preparation of hierarchical
zeolites of numerous framework types over a wide composi-
tional range (i.e., from pure silica down to Si/Al ≈ 4).
[13,16]
Con-
sequently, Al-rich zeolites, e.g., X or A (Si/Al ≈ 1), pose the last
compositional challenge to be amended to hierarchical form by
post-synthetic strategies.
Hierarchical X
[18]
and A
[19]
zeolites have been obtained using
bottom-up strategies, involving costly organic templates that
after the synthesis need to be thermally removed. However, it
should be emphasized that the commercial synthesis of zeolites
with Si/Al < 5 does not involve the use of organic templates as
structure-directing agents, which significantly reduces manu-
facturing expenses (ca. 2–5 USD per kg).
[20]
The resulting eco-
nomic constraints infer that most preferably affordable routes,
e.g., post-synthetic modifications, should be used to derive their
mesoporous analogues.
Hierarchical FAU- and LTA-Type Zeolites by Post-Synthetic
Design: A New Generation of Highly Efficient Base
Catalysts
Hierarchical FAU- and LTA-type catalysts are prepared by post-synthetic
modifications and evaluated in the base-catalyzed Knoevenagel condensa-
tion of benzaldehyde with malononitrile. A novel route to attain mesoporous
Al-rich zeolites (A and X) is demonstrated, while mesoporous Y and USY
zeolites are prepared using recently developed methods. Base functionality is
introduced by alkali ion exchange (Cs, Na) or by high-temperature nitridation
in ammonia. A thorough characterization of the zeolites’ structure, composi-
tion, porosity, morphology, and basicity demonstrates that the presence of a
secondary mesopore network enhances the ion-exchange efficiency and the
structural incorporation of nitrogen. The modified USY zeolites display twice
the conversion, while the hierarchical A, X, and Y are up to 10 times more
active based on the enhanced accessibility. These results demonstrate that
the Knoevenagel condensation takes place predominately at the external sur-
face, highlighting secondary porosity as a key criterion in the design of basic
zeolite catalysts.
DOI: 10.1002/adfm.201202320
D. Verboekend, T. C. Keller, Dr. S. Mitchell,
Prof. J. Pérez-Ramírez
Institute for Chemical and Bioengineering
Department of Chemistry and Applied Biosciences
ETH Zurich, Wolfgang-Pauli-Strasse 10
CH 8093, Zurich, Switzerland
E-mail: jpr@chem.ethz.ch
Adv. Funct. Mater. 2012,
DOI: 10.1002/adfm.201202320