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reactants (Sigma-Aldrich, 99.5% (2-butanol), 99.8% (1-butanol),
therefore provide a greater range of acid strengths useful in
the practice of Brønsted acid catalysis.
The central atom strongly influences the reactivity of
protons in Keggin-type POMclusters through the combined
99.5% (tert-butanol, anhydrous)) were introduced as a liquid using a
syringe pump (Cole Parmer, 74900 series) and vaporized at 393 K by
injection into flowing He (Praxair, UHP). 1-Butene (Scott Specialty
Gases, 99%) flow rates, liquid 2-butanol introduction rates and He
flow rates were adjusted to give desired reactant pressures and to
keep conversions low (< 10%) and relatively constant among various
catalyst samples. Reactant and product concentrations were mea-
sured by gas chromatography using flame ionization detection
(Agilent 6890N GC, 50 m HP-1 column). Only butene products of
dehydration reactions were detected (1-butene, cis-2-butene, and
trans-2-butene). Brønsted acid sites were titrated by introducing
liquid mixtures of 2-butanol reactants (Sigma-Aldrich, 99.5%,
anhydrous) with pyridine (Aldrich, 99.9%) into flowing He to give
0.5 kPa 2-butanol and 0.9 Pa pyridine. The amount of titrant adsorbed
on the catalyst was measured from measurements of its concentration
in the effluent stream using the chromatographic protocols described
above for 2-butanol dehydration.
ꢀ
effects on the rate constant of C O bond breaking k2 and the
equilibrium constant for the formation of unreactive 2-
butanol dimers K4. Both increased in parallel as the oxidation
state of the central atom X in H8ꢀnXn+W increased (Co < Al <
Si < P) and the deprotonation enthalpy concurrently
decreased, because of the ionic character of the transition
ꢀ
state in C O cleavage and of the 2-butanol dimer. Reaction
rates reflect k2 and K4 values in a manner that leads to
compensating effects and to rates that benefit from stronger
acids at low butanol pressures but from weaker acids at higher
pressures. 2-Butanol dehydration rates (at 0.5 kPa 2-butanol
pressure) increased by a factor of 2.6 as deprotonation
enthalpies decreased by 34 kJmolꢀ1 (H5AlW!H3PW;
Figure 1).
Calculations were carried out using a periodic plane wave density
functional theory code VASP.[15,16] The generalized gradient approx-
imation of the Perdew-Wang form (PW91) was used to correct
exchange energies.[17] A cut off energy of 396.0 eV defined the plane
wave basis set expansion and ultrasoft pseudopotentials[18] were used
to model the electron–ion interactions. The Keggin structure was
Earlier, van Santen and Kramer proposed, based on
electronic structure calculations, a relation between the
stability of cationic species present as transition states and
the deprotonation energies of Brønsted acids.[11] Our study
provides experimental verification for this proposal for the
dehydration of 2-butanol on POMclusters in terms of a
rigorous analysis of turnover rates in terms of rate and
equilibrium constants for elementary steps. The relationship
between the stability of transition states and of intermediates
and the intrinsic acid strength is essential to design materials
with specific reactivity and selectivity in acid catalysis. Indeed,
activation barriers for steps involving ionic transition states
benefit from lower deprotonation enthalpies, but these steps
may not limit overall catalytic rates. Deprotonation enthal-
pies also influence the stability of ionic intermediates of
varying reactivity, leading to compensating effects that cause
rates that increase or decrease with increasing deprotonation
enthalpy depending on the relative concentrations of reactive
and unreactive intermediates.
3
placed in the center of a 20 20 20 supercell to allow for a
sufficient vacuum region between neighboring Keggin structures. A
single G-point was found to be sufficient to sample the first Brillouin
zone.[8] All reported structures were optimized to force values below
0.05 eV per atom. The climbing nudged elastic band method was used
to locate transition states.[19]
Received: March 23, 2007
Revised: July 25, 2007
Published online: September 7, 2007
Keywords: acid catalysis · alcohols · cluster compounds ·
.
dehydration · polyoxometalates
[1] Hammet indicator methods (e.g. T. Okuhara, C. Hu, M.
and liquid phase acid dissociation values (e.g. I. V. Kozhevnikov,
Adv. Catal. 1996, 41, 133; M. N. Timofeeva, Appl. Catal. A 2003,
256, 19, and references therein) are solvent dependent and thus
no measures of intrinsic acid strength. None of the work
summarized in the aforementioned review papers discusses the
effect of central atom on the catalytic function in terms of the
rates of specific elementary steps.
Experimental Section
H3PW12O40 (Aldrich), H4SiW12O40 (Aldrich, 99.9%), H5AlW12O40
(prepared as in Ref. [12]), and H6CoW12O40 clusters (prepared as in
Ref. [13,14]) were deposited onto SiO2 (Cab-O-Sil, 304 m2 gꢀ1, pore
volume 1.5 cmꢀ3 gꢀ1; washed three times in 1m HNO3 and dried in Air
(Praxair, extra-dry, 573 K, 5 h, 20 cm3 gꢀ1)) by incipient wetness
impregnation with 1.5 cm3 of ethanol (Aldrich, anhydrous 99.5%)—
H3PW H4SiW H5AlW, or H6CoW solutions per gram of dry SiO2.
[3] M. Misono, N. Mizuno, K. Katamura, A. Kasai, K. Sakata, T.
[4] K. Y. Lee, T. Arai, S. Nakata, S. Asoka, T. Okuhara, M. Misono,
,
,
Impregnated samples were treated in flowing dry air (Praxair, extra-
dry) at 323 K for 24 h. H-BEA (Zeolyst) with Si/Al 12.5:1 was used.
Catalytic 2-butanol dehydration rates and selectivities were
measured at 343 K in a quartz flow cell (1.0 cm inner diameter)
containing samples (1–100 mg of catalysts (125–180 mm) diluted with
acid-washed quartz ( ꢁ 50 mg, 125–180 mm)) held on a porous quartz
disc. Temperatures were measured using K-type thermocouples and
set using a Watlow controller (Series 982) and a resistively-heated
furnace. Samples were treated in flowing He (80 cm3 minꢀ1, Praxair,
UHP (He), extra-dry (air)) at 343 K for 1 h before catalytic measure-
ments. Thermal treatments in He or air (80 cm3 minꢀ1, Praxair, UHP)
at 373–575 K did not influence measured rates. Transfer lines were
held at 393 K to prevent adsorption or condensation of reactants,
products, and titrants before chromatographic analysis. Butanol
[5] The additional stability gained by the formation of [R1-O-H-O-
R2]+ cationic hydrogen bonds is well known, see Molecular
Structure and Energetics, Vol. 4 (Eds.: J. F. Liebman, A. Green-
berg), VCH, Weinheim, 1987, pp. 74 – 142, and references
+
therein. The well-known H5O2 ion is another example.
[6] H. Noller, K. Thomke, J. Mol. Catal. 1979, 6, 375.
[7] S. Delsarte, P. Grange, Appl. Catal. A 2004, 259, 269.
[8] B. B. Bardin, S. V. Bordawekar, M. Neurock, R. J. Davis, J. Phys.
Bardin, R. J. Davis, M. Neurock, Appl. Catal. A 2003, 256, 51.
[9] I. A. Koppel, P. Burk, I. Koppel, I. Leito, T. Sonoda, M. Mishima,
[10] M. Brꢀndle, J. Sauer, J. Am. Chem. Soc. 1998, 116, 5428.
Angew. Chem. Int. Ed. 2007, 46, 7864 –7868
ꢀ 2007 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim