High-pressure hydrothermal dope Ce into MoVTeNbOx for one-step oxidation of propylene to acrylic acid

IF 3.4 3区 化学 Q2 CHEMISTRY, PHYSICAL
Yiwen Wang, Shuangming Li, Jiao Song, Haonan Qu, Sansan Yu
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Abstract

A high-pressure hydrothermal method was employed to introduce Ce element facilely into MoVTeNbOx catalysts in 0.5 h. It was indicated that Ce atoms were doped into the framework of MoVTeNbOx without changing the unique crystal structure of MoVTeNbOx. The introduction of Ce could facilitate the formation of oxygen vacancies and improve the redox ability of surfacial V. However, it was worth noting that the doping amount of Ce was negatively related to the content of M1 active phase. Within a certain range, the catalytic performance could be improved by sacrificing an appropriate amount of M1 phase. In the conversion of propylene to acrylic acid, the highest yield of 58.2% was obtained under catalyst MoVTeNbCeOx (V: Ce =1: 0.05) at 380 °C with the M1 phase content of 81.6%. The appropriate amount of Ce doping improved the propylene conversion by more than 20% compared to undoped. Moreover, the changes in Gibbs free energy of the rate-limiting step of direct oxidation of propylene before and after Ce doping were evaluated by Density functional theory (DFT). It is illustrated that the doping of Ce is thought to affect the main reason for the reduction of Gibbs free energy.

Abstract Image

Abstract Image

高压水热掺杂 Ce 到 MoVTeNbOx 中,用于丙烯到丙烯酸的一步氧化反应
采用高压水热法在 0.5 小时内将铈元素方便地引入 MoVTeNbOx 催化剂中。结果表明,在不改变 MoVTeNbOx 独特晶体结构的情况下,Ce 原子被掺杂到 MoVTeNbOx 的框架中。但值得注意的是,掺入量与 M1 活性相的含量呈负相关。在一定范围内,可以通过牺牲适量的 M1 相来提高催化性能。在丙烯转化为丙烯酸的过程中,催化剂 MoVTeNbCeOx(V:Ce =1:0.05)在 380 ℃ 下的最高产率为 58.2%,M1 相含量为 81.6%。与未掺杂相比,适量的掺杂 Ce 使丙烯转化率提高了 20% 以上。此外,密度泛函理论(DFT)评估了掺杂 Ce 前后丙烯直接氧化限速步骤的吉布斯自由能的变化。结果表明,掺杂 Ce 被认为是影响吉布斯自由能降低的主要原因。
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来源期刊
Catalysis Communications
Catalysis Communications 化学-物理化学
CiteScore
6.20
自引率
2.70%
发文量
183
审稿时长
46 days
期刊介绍: Catalysis Communications aims to provide rapid publication of significant, novel, and timely research results homogeneous, heterogeneous, and enzymatic catalysis.
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