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One Step Formation of Propene from Ethene or Ethanol through Metathesis on Nickel Ion-loaded Silica

机译:通过镍离子负载二氧化硅上的复分解反应从乙烯或乙醇一步形成丙烯

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Increased propene production is presently one of the most significant objectives in petroleum chemistry. Especially the one-step conversion of ethene to propene (ETP reaction, 3C2H4 ? 2C3H6) is the most desired process. In our efforts, nickel ion-loaded mesoporous silica could turn a new type of ETP reaction into reality. The one-step conversion of ethene was 68% and the propene selectivity was 48% in a continuous?gas-flow system at 673 K and atmospheric pressure. The reactivity of lower olefins and the dependences of the ETP reaction on the contact time and the partial pressure of ethene were consistent with a reaction mechanism involving dimerization of ethene to 1-butene, isomerization of 1-butene to 2-butene, and metathesis of 2-butene and ethene to yield propene. The reaction was then expanded to an ethanol-to-propene reaction on the same catalyst, in which two possible reaction routes are suggested to form ethene from ethanol. The catalysts were characterized mainly by EXAFS and TPR techniques. The local structures of the nickel species active for the ETP reaction were very similar to that of layered nickel silicate, while those on the inert catalysts were the same as that of NiO particles.?
机译:丙烯产量的增加目前是石油化学中最重要的目标之一。尤其是乙烯一步一步转化为丙烯(ETP反应,3C 2 H 4 ?2C 3 H 6 )是最需要的过程。在我们的努力下,负载镍离子的中孔二氧化硅可能将新型的ETP反应变为现实。在673 K和大气压下的连续气流系统中,乙烯的一步转化率为68%,丙烯选择性为48%。低级烯烃的反应性和ETP反应对接触时间和乙烯分压的依赖性与涉及乙烯二聚为1-丁烯,1-丁烯异构化为2-丁烯以及复分解的反应机理相一致。 2-丁烯和乙烯生成丙烯。然后在相同的催化剂上将反应扩展为乙醇-丙烯反应,其中提出了两种可能的反应路线,由乙醇形成乙烯。催化剂主要通过EXAFS和TPR技术进行表征。对ETP反应有活性的镍物种的局部结构与层状硅酸镍非常相似,而在惰性催化剂上的局部结构与NiO颗粒相同。

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