Use of renewables for the production of chemicals: Glycerol oxidation over carbon supported gold catalysts
Introduction
Oxidation reactions are of industrial importance for the synthesis of fine chemicals, even though stoichiometric oxidizing agents (e.g. permanganate) or biotechnological processes are used and a large number of by-products are often formed which decrease the selectivity to the desired oxidation product. An environmentally friendly alternative is the oxidation in the presence of a heterogeneous catalyst and oxygen. Because of the intrinsic reactivity of nanoscaled gold particles (dAu = 1–10 nm), supported gold catalysts are used for liquid-phase oxidations, e.g. in the glucose oxidation to gluconic acid [1]. In the present work, we report on the heterogeneously catalyzed liquid-phase oxidation of glycerol performed under atmospheric pressure and at constant pH. Because of the high functionality of this molecule a complex reaction pathway exists (Fig. 1), whose single steps can be controlled via the catalyst properties and the reaction conditions. This reaction has been already investigated with classical oxidation catalysts like palladium or platinum supported on carbon [2], [3], [4], [5], [6], [7] and since the last few years also with gold catalysts [6], [7], [8], [9], [10], [11], [12]. Hutchings and co-workers [6], [7] performed the glycerol oxidation in an autoclave reactor under oxygen pressures up to 6 bar without pH control and obtained 100% selectivity to glyceric acid (Fig. 1) at 56% conversion with a 1 wt.% Au/C catalyst. The highest yield of 84% is obtained at 6 bar oxygen pressure and with a glycerol/metal molar ratio of 214. The group of Prati and co-workers [12] could improve this result to 92% at full conversion by optimizing both the catalyst preparation method (1 wt.% Au/C prepared by citrate-protected gold-sol method) and the reaction conditions (, glycerol/Au molar ratio = 500) but also without pH control (glycerol/NaOH molar ratio = 4). However, the oxidation reaction of glycerol undergoes an oxidative dehydrogenation mechanism, in which the first step consists on the dehydrogenation of the substrate molecule [5], [15]. We could confirm in a previous study of the Au/C catalyzed glycerol oxidation performed in a batch reactor under pressures up to 10 bar that (i) this first step is only occurring in presence of a base and (ii) the base concentration plays a significant role on the reaction course [13]. Consequently, we focused our following studies on the aerobic glycerol oxidation, so that the pH can be controlled during the reaction. In order to improve the catalyst properties we investigated, amongst others, the promotor effect of platinum on Au/C catalysts. It has been reported in the literature that bimetallic gold catalysts show an improved activity in the glycerol oxidation compared to the corresponding monometallic gold catalysts [14]. But these reactions have been carried out without pH control, so that the pH decreases during the reaction as a function of the product formation rate, which is proportional to the pH depending reaction rate. In this work, we report on the improvement of the Au/C catalyst properties by platinum promoting, obtained at constant pH. To the best of our knowledge, this is the first study of the influence of Pt on the catalyst performance of Au/C under atmospheric pressure and at constant pH.
Section snippets
Materials
NaOH (0.2 M), NaOH (>99%), Tetrakis-(hydroxymethyl)-phosphonium chloride (THPC, 78 wt.%), formaldehyde (35% solution), polyvinyl alcohol 72000 (>98%) from Merck, HAuCl4·3H2O (99.99% ACS, Au 49.5% min.) and H2PtCl6 (>99.9%) from Alfa Aesar were used. The carbon black “Black Pearls 2000” (BP) was purchased from Cabot GmbH; glycerol (>99%) and NaBH4 (99%) from Sigma–Aldrich; KOH (86%) from Fluka. The activated carbons (AC) NSX1, NSX1G, NSXU and NSXP were from Norit.
Monometallic gold catalysts
The gold catalysts were prepared
Investigation of the glycerol oxidation with monometallic gold catalysts
The aim of this work is to produce highly interesting chemicals like glyceric acid from the environmentally friendly oxidation of a biosustainable source with high yields. For that purpose, the catalyst properties as well as the reaction conditions have to be optimized. The first test experiments carried out at atmospheric pressure confirm the assumption that the reaction rate does not drastically decrease with decreasing oxygen pressure. In addition, the semi-batch-wise operation presents the
Conclusions
We focus our investigations on an environmentally friendly way to produce useful chemicals from a biosustainable source, namely on the heterogeneously catalyzed oxidation of glycerol performed under atmospheric pressure with molecular oxygen as oxidizing agent and under pH controlled conditions. Attention has been paid to the catalyst design. The catalyst preparation method has been studied and optimized to the gold-sol method with THPC as reducing agent. The influence of the pore system of the
Acknowledgements
The authors gratefully acknowledge Dipl.-Ing. Björn Schichtel for the physisorption measurements and Dr. H. Ehrenberg for XRD analysis.
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