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Selective Production of Aromatics by Catalytic Fast Pyrolysis of Furan with In Situ Dehydrogenation of Propane

机译:用丙烷催化快速热解的选择性生产芳烃,原位脱氢丙烷

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Catalytic fast pyrolysis (CFP) of furan was studied with the co-feeding of propane over ZSM-5,CrOx/ Al2O3,and mixed catalysts with both ZSM-5 and CrOx/Al2O3 to combine the dehydrogenation of propane and CFP of furan in the presence of in situ generated propylene.With 15 vol % propane co-feeding,a slight increase in aromatic yield was observed over ZSM-5 catalyst.These enhancement was further improved by using mixed catalysts consisting of CrOx/Al2O3 and ZSM-5 with different weight ratios.Over the best mixed catalyst with CrOx/Al2O3 to ZSM-5 weight ratio of 2,a nearly 2-fold increase in the aromatic yield was obtained.The toluene selectivity was also increased from 37% to 50%.The increase in aromatic yield is directly dependent on the propane to total flow volume ratio.Moreover,the coke formation within ZSM-5 was also reduced,leading to a slower catalyst deactivation.From mechanistic studies,a two-step cascade reaction pathway was observed over the bifunctional mixed catalysts.It was proposed that propane dehydrogenates to propylene over CrOx/Al2O3.The propylene then reacts with furan within ZSM-5 catalyst to selectively form aromatics.This work demonstrates a simple and economical strategy to further improve the CFP technique.
机译:用ZSM-5,CROX / AL2O3和ZSM-5和CROX / AL2O3的混合催化剂的共送丙烷的催化快速热解(CFP)用ZSM-5和CROX / AL2O3的混合催化剂来结合丙烷丙烷和CFP的脱氢在原位生成的丙烯中存在。在15体积%的丙烷共同喂养,通过ZSM-5催化剂观察到芳族产率的略微增加。通过使用由Crox / Al2O3和ZSM-5组成的混合催化剂,进一步提高了增强的增强重量比率。获得最佳的混合催化剂与克罗伯/ al2O3至Zsm-5重量比,得到芳族产率的几乎2倍。甲苯选择性也从37%增加到50%。增加芳族产率直接依赖于总流量比的丙烷。罗姆-5内的焦炭形成也降低,导致催化剂失活较慢。从机械研究中,在双功能上观察到两步级联反应途径混合催化剂。是pr用克罗伯/ Al 2 O 3对丙烯脱氢丙烷脱氢。然后丙烯在ZSM-5催化剂内与呋喃反应,以选择性地形成芳烃。本工作证明了一种简单且经济的策略,以进一步提高CFP技术。

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