Abstract

AbstractAlpha‐phenylethanol (PE) is an essential chemical in the field of medicine and synthetic perfumery. Therefore, in this work, we used a supported Ni–B–P amorphous alloy catalyst (Ni–B–P/SiO2) in the hydrogenation of acetophenone (AP) to α‐PE, which demonstrated excellent catalytic activity and selectivity, compared with Ni–B/SiO2 (KBH4 reduction of nickel salt). Ni–B–P/SiO2 exhibited a high AP hydrogenation conversion of approximately 99%, whereas the PE selectivity reached up to 94%, which is approximately 1.4‐fold higher than that of Ni–B/SiO2 (about 69%), thereby directly proving the unique inhibition of AP hydrogenation over hydrogenation of P in the Ni–B catalytic system. The doped P in Ni–B–P/SiO2 enhances the oxidation resistance and maintains the valence stability of Ni and B. Furthermore, sufficient experimental data were collected to determine the kinetic parameters. Based on the Langmuir–Hinshelwood model, we assumed that (i) AP and H2 compete for adsorption on Ni–B–P/SiO2; (ii) AP has strong adsorptive capacity on Ni–B–P/SiO2; and (iii) PE coverage on the catalyst was negligible. Then, the dynamic equation was derived, which indicated that experimental data agree well with the dynamic model. Finally, the activation energy was confirmed to be 50.73 KJ/mol. This report will open up an avenue for the industrialization of amorphous alloy catalysts.

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