PV0.6−0.3[HPAloading/Surface Area of Dried Catalyst]where;PV is the Pore Volume of the dried supported heteropolyacid catalyst (measured in ml/g catalyst); HPA loading is the amount of heteropolyacid present in the dried supported heteropolyacid catalyst (measure in micro moles/g); and Surface Area of Dried Catalyst is the surface area of the dried supported heteropolyacid catalyst (measured in m2/g)."/> Process for producing alkenes oxygenates by using supported heteropolyacid catalysts
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Process for producing alkenes oxygenates by using supported heteropolyacid catalysts

机译:通过使用负载型杂多酸催化剂生产含氧烯烃的方法

摘要

Process for producing alkene(s) from an oxygenate feedstock in a reactor by dehydration in the presence of a supported heteropolyacid catalyst. The pore volume of the supported heteropolyacid catalyst satisfies the following formula:PV0.6−0.3[HPAloading/Surface Area of Dried Catalyst]where;PV is the Pore Volume of the dried supported heteropolyacid catalyst (measured in ml/g catalyst); HPA loading is the amount of heteropolyacid present in the dried supported heteropolyacid catalyst (measure in micro moles/g); and Surface Area of Dried Catalyst is the surface area of the dried supported heteropolyacid catalyst (measured in m2/g).
机译:在负载型杂多酸催化剂存在下,通过脱水从反应器中的含氧化合物原料生产烯烃的方法。负载型杂多酸催化剂的孔体积满足下式:<?in-line-formulae description =“在线公式” end =“ lead”?> PV> 0.6-0.3 [ HPA 干催化剂的加载/表面积] where; <?in-line-formulae description =“ In-line Formulae” end =“ tail”?> PV是干燥的负载型杂多酸催化剂的孔体积(以ml / g催化剂测量) ; HPA含量是干燥的负载型杂多酸催化剂中杂多酸的含量(以微摩尔/ g为单位); “干燥催化剂的表面积”是干燥的负载型杂多酸催化剂的表面积(以m2 / g为单位)。

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