Abstract

Metal-supported catalyst with high activity and relatively simple preparation method is given priority to industrial production. In this work, this study reported an easily accessible synthesis strategy to prepare Mott-Schottky-type N-doped carbon encapsulated metallic Co (Co@Np+gC) catalyst by high-temperature pyrolysis method in which carbon nitride (g-C3N4) and dopamine were used as support and nitrogen source. The prepared Co@Np+gC presented a Mott-Schottky effect; that is, a strong electronic interaction of metallic Co and N-doped carbon shell was constructed to lead to the generation of Mott-Schottky contact. The metallic Co, due to high work function as compared to that of N-doped carbon, transferred electrons to the N-doped outer shell, forming a new contact interface. In this interface area, the positive and negative charges were redistributed, and the catalytic hydrogenation mainly occurred in the area of active charges. The Co@Np+gC catalyst showed excellent catalytic activity in the hydrogenation of phenylacetylene to styrene, and the selectivity of styrene reached 82.4%, much higher than those of reference catalysts. The reason for the promoted semi-hydrogenation of phenylacetylene was attributed to the electron transfer of metallic Co, as it was caused by N doping on carbon.

Highlights

  • IntroductionThe selective hydrogenation of alkynes to alkenes is one of the most important chemical reactions in the chemical industry [1,2]

  • The X-ray diffraction (XRD) results indicated that metal Co species were directly reduced to metallic Co during high-temperature pyrolysis

  • In the phenylacetylene catalytic hydrogenation reaction, molecules containing benzene rings diffused in the mesoporous channels, which is one of the key steps to ensure the completion of catalytic reactions

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Summary

Introduction

The selective hydrogenation of alkynes to alkenes is one of the most important chemical reactions in the chemical industry [1,2]. Styrene is a very important chemical raw material and is used as a monomer for the production of polystyrene, resin, and styrene butadiene rubber [3]. In the current ethylene cracking unit, styrene as a by-product is unavoidably produced, along with a small amount of phenylacetylene. Different from the physical separation that is of considerable difficulty because of their similar molecular structure, the catalytic hydrogenation could transform phenylacetylene to styrene directly. The selective hydrogenation of phenylacetylene to styrene is in urgent need of being promoted [6,8]

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