doi:10.1016/j.jcat.2008.01.003
Copyright © 2008 Elsevier Inc. All rights reserved.
Aqueous-phase biphasic dehydroaromatization of bio-derived limonene into p-cymene by soluble Pd nanocluster catalysts
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Chen Zhaoa, Weijia Gana, Xiaobing Fana, Zhipeng Caia, Paul J. Dysonb,
,
and Yuan Koua,
, 
aPKU Green Chemistry Center, Beijing National Laboratory for Molecular Sciences, College of Chemistry and Molecular Engineering, Peking University, Beijing 100871, China
bInstitut des Sciences et Ingénierie Chimiques, Ecole Polytechnique Fédérale de Lausanne (EPFL), CH-1015 Lausanne, Switzerland
Received 19 October 2007;
revised 24 December 2007;
accepted 2 January 2008.
Available online 31 January 2008.
Abstract
A biphasic approach to the dehydroaromatization of bioderived limonene into water-insoluble p-cymene using soluble Pd nanoparticle catalysts in an aqueous phase (
150 °C, 2 bar H2) was successfully achieved with a conversion of 93% and a selectivity of 82%. The Pd nanoparticles, operating under forcing conditions (180 °C, 2 bar H2), can be recycled at least four times without noticeable degradation. The effects of temperature, pressure, reaction time, pH, catalyst concentration, metal type, the type and amount of polymer stabilizer, and the preparation method were systematically investigated to optimize the process and provide insight into the mechanisms involved.
Keywords: Limonene; p-Cymene; Dehydroaromatization; Palladium; Nanoparticles; Biphasic catalysis; Terpene; Poly(N-vinyl-2-pyrrolidone); Biomass
Scheme 1. Dehydroaromatization of limonene to p-cymene under a hydrogen atmosphere.
Fig. 1. (a) TEM micrograph of Pd nanoparticles protected by PVP-K90 in water before catalysis (scale bar = 20 nm). Nanoparticles were synthesized according to the method described in Section 2.2.1. (b) Histogram showing the particle size distribution from (a). (c) TEM micrograph of Pd nanoparticles after the first run of recycling experiment, as described in Section 2.4. Scale bar = 20 nm. (d) Histogram showing the particle size distribution from (c). (e) TEM micrograph of Pd nanoparticles stabilized by PVP-K15 after reaction under 2 bar H2 at 180 °C for 3 h, stirred at 500 rpm, [Pd]=5×10−3 mol/L, limonene/catalyst = 50/1 mol/mol. Scale bar = 20 nm.
Scheme 2. Proposed mechanism of limonene conversion over (a) heterogeneous Pd/SiO2 and (b) soluble Pd catalysts.
Fig. 2. Product distributions for limonene conversion as a function of temperature. Reaction conditions: Reactions were carried out in an autoclave in water containing Pd nanoparticles under 2 bar H2 for 5 h, stirred at 500 rpm. Further reaction parameters and experimental data are given in Table S1, entries 1–5.
Table 1.
Conversion of limonene using soluble Pd nanoparticles under different conditionsa
a General conditions: PVP:Pd (mol:mol) = 20, Pd (
1×10−3 mol/L, 10 mL), nanoparticles were synthesized by alcohol–water reduction, water as solvent, pH 2, limonene (1.360 g, 0.01 mol), 2 bar H
2, stirred at 500 rpm.
b Tested after 1 h, defined as number of moles of consumed H
2 per mole of Pd per hour, determined by GC.
c Nanoparticle aggregation observed.
Table 2.
Conversion of limonene using hydrogen acceptors and/or using different Pd nanoparticle preparation methodsa
a General conditions: 2 bar H
2, 3 h, stirred at 500 rpm, Pd (
1×10−3 mol/L, 10 mL in entries 1–6;
5×10−3 mol/L, 20 mL in entries 7–9), water as solvent, pH 2.
b Determined after 1 h, defined as number of moles of consumed H
2 per mole of Pd per hour, determined by GC.
c Nanoparticle aggregation observed.
d Pd (
5×10−3 mol/L, 60 mL), limonene (2.040 g, 0.015 mol), recycling data.

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