The Complete
51
V MAS NMR Spectrum of Surface Vanadia
Nanoparticles on Anatase (TiO
2
): Vanadia Surface Structure
of a DeNO
x
Catalyst
Ulla Gro Nielsen,
²,§
Nan-Yu Topsøe,
‡
Michael Brorson,
‡
Jørgen Skibsted,
²
and
Hans J. Jakobsen*
,²
Contribution from the Instrument Centre for Solid-State NMR Spectroscopy,
Department of Chemistry, UniVersity of Aarhus, DK-8000 Aarhus C, Denmark, and
Haldor Topsøe A/S, NymølleVej 55, DK-2800 Lyngby, Denmark
Received February 10, 2003; Revised Manuscript Received January 5, 2004; E-mail: hja@chem.au.dk
Abstract: The first observations of the complete manifold of spinning sidebands (ssbs) including both the
central and satellite transitions in
51
V MAS NMR spectra of surface vanadia nanoparticles on titania in
DeNO
x catalysts are presented.
51
V quadrupole coupling and chemical shift anisotropy parameters for the
dominating vanadia structure are determined from
51
V MAS NMR spectra recorded at 9.4 and 14.1 T.
Based on correlations previously established between
51
V NMR parameters and crystal structure data for
inorganic vanadates, the NMR data are consistent with vanadium in a distorted octahedral oxygen
coordination environment for the so-called strongly bonded vanadia species on the surface. The investigation
includes two vanadia-titania model catalysts and six industrial-type DeNO
x catalysts.
1. Introduction
The combustion of fossil fuels and other organic materials
results in the formation of harmful nitrogen oxides (NO
x
) which
greatly contribute to the formation of smog and acid rain. The
reddish-brown smog in urban areas, caused by the photochemi-
cal oxidation of NO to NO
2
, and the damage to forest areas
have revealed the immense environmental problems the world
is facing today. As a result, increasingly stringent local
governmental and global political restrictions are imposed on
the emission of NO
x
from power plants, various industries, and
vehicles. Thus, one of the challenges to research in heteroge-
neous catalysis has been the development of efficient catalysts
for removal of NO
x
from the flue or exhaust gases by the
selective catalytic reduction (SCR) process where NO
x
is
reduced by ammonia to form dinitrogen and water. This has
motivated the need for further understanding the relationships
between chemical structure and catalytic performance of
heterogeneous catalysts. Vanadia supported on the surface of
anatase, a titanium dioxide (TiO
2
) polymorph, is the commonly
employed DeNO
x
catalyst today.
1
Tungsten trioxide (WO
3
) is
often added to enhance the thermal stability and catalytic
performance.
2
Various proposals (see references in ref 1) have previously
been made regarding the mechanism of the DeNO
x
reaction
based on studies of structure-activity relationships of the
catalysts. In particular, combined FTIR and activity studies
3-6
have shown that both V-OH and VdO groups on the titania
surface are required for the reaction, which is initiated by
adsorption of ammonia on Brønsted acid sites (V-OH),
followed by activation of ammonia via reaction with redox sites
(VdO). The activated ammonia then reacts with weakly
adsorbed NO to yield dinitrogen and water. Furthermore, recent
theoretical studies have provided insight into the nature of
adsorption and surface reaction of ammonia with nitric oxide
involving these surface sites.
7-9
Nevertheless, despite various
characterizations of the vanadia-titania catalyst system by
different methods,
10
a controversy still exists regarding the exact
structure around vanadium for the strongly bonded vanadia
nanoparticles on the titania surface.
Solid-state
51
V NMR spectroscopy has been one of the most
popular techniques in studies of vanadia/titania catalyst systems
during the past 15 years.
11-27
Generally, these studies are
performed using magic-angle spinning (MAS) and/or static
²
University of Aarhus.
‡
Haldor Topsøe A/S.
§
Present address: Materials Sciences Division, Lawrence Berkeley
National Laboratory, Berkeley, CA 94720.
(1) Topsøe, N.-Y. CATTECH 1997, 1, 125.
(2) Economidis, N. V.; Pen ˜a, D. A.; Smorniotis, P. G. Appl. Catal. B 1999,
23, 123.
(3) Topsøe, N.-Y. Science 1994, 265, 1217.
(4) Topsøe, N.-Y.; Dumesic, J.; Topsøe, H. J. Catal. 1995, 151, 241.
(5) Topsøe, N.-Y.; Topsøe, H.; Dumesic, J. J. Catal. 1995, 151, 226.
(6) Topsøe, N. Y.; Topsøe, H. Catal. Today 1991, 9, 77.
(7) Topsøe, N.-Y.; Anstrom, M.; Dumesic, J. A. Catal. Lett. 2001, 76, 11.
(8) Anstrom, M.; Dumesic, J. A.; Topsøe, N. Y. Catal. Lett. 2002, 78, 281.
(9) Anstrom, M.; Topsøe, N. Y.; Dumesic, J. A. J. Catal. 2003, 233, 115.
(10) EUROCAT GROUP. Catal. Today 1994, 20.
(11) Lapina, O. B.; Mastikhin, V. M.; Shubin, A. A.; Krasilnikov, V. N.;
Samaraev, K. I. Prog. Nucl. Magn. Reson. Spectrosc. 1992, 24, 457.
(12) Eckert, H.; Wachs, I. E. J. Phys. Chem. 1989, 93, 6796.
(13) Eckert, H.; Deo, G.; Wachs, I. E.; Hirt, A. M. Colloids Surf. 1990, 45,
347.
(14) Eckert, H. In NMR Techniques in Catalysis; Bell, A. T., Pines, A., Eds.;
Marcel Dekker: New York, 1994; pp 195-230.
(15) Pinaeva, L. G.; Lapina, O. B.; Mastikhin, V. M.; Nosov, A. V.; Balzhini-
maev, B. S. J. Mol. Catal. 1994, 88, 311.
(16) Fernandez, C.; Guelton, M. Catal. Today 1994, 20, 77.
(17) Courcot, D.; Bodart, P.; Fernandez, C.; Rigole, M.; Guelton, M. J. Chim.
Phys. 1994, 91, 909.
(18) Mastikhin, V. M.; Terskikh, V. V.; Lapina, O. B.; Filimova, S. V.; Seidl,
M.; Kno ¨zinger, M. J. Catal. 1995, 156, 1.
Published on Web 03/27/2004
4926 9 J. AM. CHEM. SOC. 2004, 126, 4926-4933 10.1021/ja030091a CCC: $27.50 © 2004 American Chemical Society