Experimental and DFT study on titanium-based half-sandwich metallocene catalysts and their application for production of 1-hexene from ethylene
作者:Sajjad Gharajedaghi、Zahra Mohamadnia、Ebrahim Ahmadi、Mohamadreza Marefat、Gerard Pareras、Sílvia Simon、Albert Poater、Naeimeh Bahri-Laleh
DOI:10.1016/j.mcat.2021.111636
日期:2021.6
8 bar, respectively. During this optimization and under specific reaction conditions, a switching behavior from ethylene trimerization to polymerization was also detected, as an undesired reaction. At the optimized conditions, synthesized catalysts showed the following trend toward both 1-hexene yield and selectivity: C1>C2>C3>C4. Then, to shed light on the possible reaction mechanisms and to confirm
不同类型的[Ind-C(R)-苯基]TiCl 3催化剂基于含茚基(Ind)配体的悬垂芳烃,带有各种类型的桥(R=环-C 5 H 10 (C1), (CH 3 ) 2 ( C2)、4- t Bu-环-C 5 H 9 (C3)和环-C 6 H 12(C4)) 已被合成,并用于在甲基铝氧烷 (MAO) 作为助催化剂存在下乙烯三聚生成 1-己烯。反应条件首先在 C2 催化剂情况下进行优化,其中在催化剂浓度、温度和乙烯压力为 1.5 时获得了最高的 1-己烯产物×分别为 10 -3 M、40 °C 和 8 bar。在此优化过程中和在特定反应条件下,还检测到从乙烯三聚到聚合的转换行为,这是不希望的反应。在优化条件下,合成的催化剂在 1-己烯产率和选择性方面表现出以下趋势:C1>C2>C3>C4。然后,为了阐明可能的反应机制并确认实验部分获得的活性趋势,采用了密度泛函理论 (DFT) 计算。在这条线上,