Wei Zeyue, Zhang Hanzhi, Bai Yunxing, Zhang Xuanyu, Huang Weixin
State Key Laboratory of Precision and Intelligent Chemistry, iChEM, Key Laboratory of Surface and Interface Chemistry and Energy Catalysis of Anhui Higher Education Institutes and Department of Chemical Physics, University of Science and Technology of China, Hefei 230026, P. R. China.
Precis Chem. 2025 Jan 30;3(4):206-213. doi: 10.1021/prechem.4c00089. eCollection 2025 Apr 28.
Hydrothermally synthesized mixed-phase MoVTeNbO catalysts are active for catalyzing the selective oxidation of propane to acrylic acid but suffer from the presence of the amorphous phase and low specific surface areas. Herein we report that HCl treatment preferentially dissolves the amorphous phase in hydrothermally synthesized mixed-phase MoVTeNbO catalysts and increases the catalytic performance. An optimal HCl treatment significantly increases the CH conversion from 38.9% to 58.2% without changing the acrylic acid selectivity in the selective oxidation of propane to acrylic acid at 380 °C. The original and HCl treated catalysts exhibit similar apparent activation energies, while HCl treatment increases the specific surface area, surface acid sites, surface V density, and CH and CH irreversible adsorption amounts but decreases the CH and CH irreversible adsorption heats. The CH conversion rate is proportional to the surface V density and CH irreversible adsorption amount, and the TOF is measured as 3.31 ± 0.08 × 10 s at 340 °C. Thus, HCl treatment enhances the catalytic performance of mixed-phase MoVTeNbO catalysts mainly by increasing the active site density rather than by increasing the active site activity. Our results provide an effective approach to prepare highly active mixed-phase MoVTeNbO catalysts for the selective oxidation of propane to acrylic acid.
水热合成的混合相MoVTeNbO催化剂对丙烷选择性氧化制丙烯酸具有催化活性,但存在非晶相且比表面积较低。在此我们报道,盐酸处理优先溶解水热合成的混合相MoVTeNbO催化剂中的非晶相,并提高催化性能。在380℃下丙烷选择性氧化制丙烯酸的反应中,最佳的盐酸处理显著提高了丙烷转化率,从38.9%提高到58.2%,同时不改变丙烯酸选择性。原始催化剂和经盐酸处理的催化剂表现出相似的表观活化能,而盐酸处理增加了比表面积、表面酸性位点、表面钒密度以及丙烷和丙烯的不可逆吸附量,但降低了丙烷和丙烯的不可逆吸附热。丙烷转化率与表面钒密度和丙烷不可逆吸附量成正比,在340℃下测得的TOF为3.31±0.08×10⁻⁵ s⁻¹。因此,盐酸处理主要通过增加活性位点密度而非提高活性位点活性来增强混合相MoVTeNbO催化剂的催化性能。我们的结果为制备用于丙烷选择性氧化制丙烯酸的高活性混合相MoVTeNbO催化剂提供了一种有效方法。