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 |
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Format: | Artikel |
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. |
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ISSN: | 2046-2069 2046-2069 |
DOI: | 10.1039/d4ra06259k |