Hydroxyapatite supported molybdenum oxide catalyst for selective dehydrogenation of cyclohexane to cyclohexene: studies of dispersibility and chemical environment

The selective oxidative dehydrogenation of cyclohexane to cyclohexene was conducted using molybdenum oxide (MoO x ) as a catalyst and hydroxyapatite (HAP) and Ca 5 (OH)(PO 4 ) 3 as carriers. Two series of MO x /HAP catalysts with varying MoO x loading capacity and calcination temperature were prepar...

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Veröffentlicht in:RSC advances 2024-11, Vol.14 (49), p.36461-3647
Hauptverfasser: Zheng, Mingxiao, Zhou, Feng, Ma, Huixia, Song, Xuefeng, Wu, Guang
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Sprache:eng
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Zusammenfassung:The selective oxidative dehydrogenation of cyclohexane to cyclohexene was conducted using molybdenum oxide (MoO x ) as a catalyst and hydroxyapatite (HAP) and Ca 5 (OH)(PO 4 ) 3 as carriers. Two series of MO x /HAP catalysts with varying MoO x loading capacity and calcination temperature were prepared via the co-impregnation method. The impact of dispersibility and chemical environment on the catalytic performance of MoO x was investigated. The catalysts were characterized using XRD, XPS, H 2 -TPR, and UV-Vis spectra. These MoO x /HAP catalysts were employed for the oxidative dehydrogenation (ODH) of cyclohexane to cyclohexene. MoO x /HAP catalysts with lower loading capacity exhibited higher dispersion of MoO x and selectivity towards cyclohexane. The calcination temperature directly influenced the chemical environment of MoO x , thereby affecting its catalytic performance. Samples calcinated at lower temperatures (500 °C and 600 °C) demonstrated higher conversion rates for cyclohexane, while samples calcinated at higher temperatures (above 700 °C) displayed greater selectivity towards cyclohexane. At 430 °C, when the conversion rate of cyclohexane reached 13.1%, the selectivity of cyclohexene over MHAP-0.05-800 catalyst reached 58.2%. Highly dispersed MoO x /HAP catalyst shows high selectivity towards cyclohexene.
ISSN:2046-2069
2046-2069
DOI:10.1039/d4ra06259k