Article ID Journal Published Year Pages File Type
61173 Journal of Catalysis 2013 11 Pages PDF
Abstract

•One-pot process for α-pinene isomerization.•Total conversion and reasonable catalyst recyclability was demonstrated.•Valuable ρ-cymene produced in high yield (77 wt%).•Kinetic modeling was carried out for the proposed reaction network.

The aim of this work was to demonstrate the feasibility to produce ρ-cymene, an important commodity chemical, in a continuous, one-pot reaction system from abundant α-pinene, available e.g. as a by-product of pulping industry. The isomerization reactions of α-pinene over bimetallic heterogeneous catalysts, 3 and 5 wt% Pd–Zn (1:1, 1:4, 4:1, 1:0, and 0:1), supported on Al-SBA15 were studied. The principal reaction products were identified as ρ- and m-cymenes, limonene, camphene, and ρ-menthene, respectively. The highest concentration of ρ-cymene reached 77 wt% under the optimized reaction conditions: 300 °C and α-pinene feed of 0.03 mL/min. Two main reaction pathways toward ρ- and m-cymenes were described, and a mechanistic kinetic model, based on a plausible reaction network in line with Langmuir–Hinshelwood approach, was developed. The catalyst characterization revealed the reduction in Pd(II) sites, catalyst coking, and decline of surface area over the course of time. The catalyst recovery and reuse was addressed.

Graphical abstractIn this paper, the development of a continuous process for the production of renewable p-cymene has been reported.Figure optionsDownload full-size imageDownload high-quality image (88 K)Download as PowerPoint slide

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
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