2023
DOI: 10.1016/j.apcatb.2023.122362
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Selective dehydroisomerization of cyclic monoterpenes to p-cymene over silica-supported CdO

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Cited by 2 publications
(1 citation statement)
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“…In recent decades, a variety of heterogeneous catalysts have been prepared and applied to the dehydrogenation reaction of terpene to p-cymene in the liquid or gas phase [20]. These catalysts include Ti/SBA-15 (liquid phase, 160 °C, 56% pcymene yield) [21], Pd/HZSM-5 (liquid phase, 260 °C, 8 bar, 82% yield) [22], Pd/Al2O3 (supercritical ethanol, 300 °C, 65 bar, 80% yield) [23], Zn/SBA-15 (gas phase, 450 °C, 86.7% pcymene yield) [24], TiO2 (gas phase, 300 °C, 90% yield) [25], Pd/SiO2 (gas phase, 300 °C, in H2 flow, 99% yield) [26], ZnO/SiO2 (gas phase, 370 °C, 90% yield) [27], and CdO/SiO2 (gas phase, 200-250 °C, 91-100% yield) [28]. When zeolites and alkali metals are used as catalysts for liquid-phase dehydrogenation, the reaction conditions for liquid phase dehydrogenation are milder, but the yield of p-cymene is not ideal.…”
Section: Introductionmentioning
confidence: 99%
“…In recent decades, a variety of heterogeneous catalysts have been prepared and applied to the dehydrogenation reaction of terpene to p-cymene in the liquid or gas phase [20]. These catalysts include Ti/SBA-15 (liquid phase, 160 °C, 56% pcymene yield) [21], Pd/HZSM-5 (liquid phase, 260 °C, 8 bar, 82% yield) [22], Pd/Al2O3 (supercritical ethanol, 300 °C, 65 bar, 80% yield) [23], Zn/SBA-15 (gas phase, 450 °C, 86.7% pcymene yield) [24], TiO2 (gas phase, 300 °C, 90% yield) [25], Pd/SiO2 (gas phase, 300 °C, in H2 flow, 99% yield) [26], ZnO/SiO2 (gas phase, 370 °C, 90% yield) [27], and CdO/SiO2 (gas phase, 200-250 °C, 91-100% yield) [28]. When zeolites and alkali metals are used as catalysts for liquid-phase dehydrogenation, the reaction conditions for liquid phase dehydrogenation are milder, but the yield of p-cymene is not ideal.…”
Section: Introductionmentioning
confidence: 99%