to 5 g of silica while mixing with a glass rod for 10 minutes. 8
ml of aqueous NH3 (3%) was then added followed by 10 ml of
an aqueous solution of NaBH4 (60 mg per 10 ml), and the
suspension stirred at 333 K for 10 min. The solid product was
filtered, washed several times with water until the washings
contained no chloride. The presence of metallic gold in the
catalyst dried at 413 K for 5 h, was confirmed by XRPD analysis
(2q = 38.2).
The oxidation of alcohols was carried out in a fixed bed
vertical glass reactor fitted with a glass frit carrying the catalyst
(0.2 g) and provided with an electronically controlled furnace.
The air stream (1.2 mmol min21) was controlled by a mass flow
instrument and the liquid reagent (0.5 mmol min21) was
supplied through a syringe pump. Liquid vaporisation occurred
on the reactor wall prior to the catalytic bed. The condensable
reaction products were collected by bubbling the effluent into a
cold trap (273 K) containing ethanol and an appropriate internal
standard and analysed by GC ( HP Plot Q 30 m silica fused
capillary column ) using helium as a carrier gas. The selectivity
was calculated as mol of carbonyl product per mol of reacted
alcohol and the carbon mass balance was close to 100% in the
case of 100% selectivity. The estimated degree of confidence of
the reported figures is ±3%.
that the mean diameter of gold particles changed from 15 nm
(w0 = 0.52) to 25 nm ( w0 = 0.32) after 18 h and then remained
stable after 60 h. It is worth noting that the catalytic behaviour
here observed is due to relatively large gold particles.
In conclusion, 1% gold on silica represents an innovative
catalyst suitable for the preparation of carbonyl compounds by
clean oxidation of alcohols under mild conditions which could
be relevant also for industrial application. The comparison
between the gas phase oxidation reported here and the
previously reported liquid phase oxidation of the alcoholic
group17 outlines the versatility of supported gold which offers
the possibility of producing carbonyl derivatives in the first
case, and carboxylates in the second case.
Notes and references
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2 R. A. Sheldon and J. K. Kochi, Metal-Catalyzed Oxidations of Organic
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3 G. Cainelli and G. Cardillo, Chromium Oxidant in Organic Chemistry,
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Table 1 reports the results obtained in the experiments and
shows a remarkable selectivity in the oxidation of aliphatic
primary alcohols to aldehydes and secondary alcohols to
ketones. The high chemoselectivity towards the alcoholic group
presented by the gold catalyst minimizes the oxidation of the C–
H and C–C–bonds and the further oxidation of the carbonyl
group. In fact, the conversion of 1-propanal under similar
experimental conditions is low and produces propanoic acid in
very low yields (entry 10). Moreover, the carbon–carbon double
bond in allyl alcohol was inactive to oxygen allowing its
transformation into acrolein with high selectivity (entry 5).
Comparing the reactivity of primary and secondary alcohols
it is evident that the activation of secondary alcohols occurs at
lower temperature. Different conversion values obtained for
homologous alcohols could be due to differences in the purity of
the reagents, particularly in the case of the 98% pure 1-butanol
where relatively low conversions have been observed.
In the case of primary alcohols, 1% gold on the support acts
mainly as a surface modifier allowing a strong increment in the
selectivity to aldehydes with respect to silica alone. In fact, the
acidic centres of the support address the reaction to a deeper
oxidation, as derived by the low yield and the excess of the
formed water (entry 11). In the oxidation of secondary alcohols,
gold acts also as a strong activator of the organic molecules
because the support is almost inactive at low temperature (413
K) (entry 12).
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During a prolonged oxidation test of 1-propanol at 573 K the
catalyst was stable over 60 h. XRPD analysis of gold showed
20 S. Biella, L. Prati and M. Rossi, IV World Congress on Oxidation
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