<p>In this study, a silicon-bridged diphosphine/CrCl<sub>3</sub>(C<sub>4</sub>H<sub>8</sub>O)<sub>3</sub>/modified methylaluminoxane catalytic system (PNSiP/CrCl<sub>3</sub>(THF)<sub>3</sub>/MMAO) was constructed, to explore the possibility of producing high-carbon olefins via ethylene/light <i>α</i>-olefins co-oligomerization. The choice of <i>α</i>-olefin monomer, ethylene pressure, and reaction temperature played crucial roles in determining the distribution of products. In presence of ethylene and 1-hexene, the primary high-carbon products are C<sub>10</sub> olefins. In contrast, when ethylene and 1-octene are present, the main high-carbon products are C<sub>12</sub> olefins. Increasing temperature and reducing pressure can promote the oligomerization of <i>α</i>-olefins with ethylene, thereby significantly improving the selectivity of high-carbon products. Detailed identities of C<sub>10</sub>-C<sub>14</sub> olefins, assigned by gas chromatographic and mass spectrometric, strongly supported a mechanism involves five-, seven- and nine-membered metallacyclic intermediates composed by ethylene and <i>α</i>-olefins units. Mechanistic analysis of C<sub>12</sub> and C<sub>14</sub> isomers revealed that co-trimerization and co-tetramerization reactions occurred concurrently during the reaction process. Furthermore, the concentration of specific carbon-number olefins, along with the reaction conditions, influenced the relative probability of the two pathways.</p> Graphical abstract <p></p>

错误:搜索内容不能为空,请输入英文关键词
错误:关键词超出字数限制,请精简
高级检索

Ethylene selective oligomerization to C10-C20 olefins catalyzed by silicon-bridged diphosphines /CrCl3(C4H8O)3/modified methylaluminoxane

  • Xuzhi Zhang,
  • Huijuan Shao,
  • Xiangsheng Mu,
  • Lirong Guo,
  • Yating Wang,
  • Tao Jiang

摘要

In this study, a silicon-bridged diphosphine/CrCl3(C4H8O)3/modified methylaluminoxane catalytic system (PNSiP/CrCl3(THF)3/MMAO) was constructed, to explore the possibility of producing high-carbon olefins via ethylene/light α-olefins co-oligomerization. The choice of α-olefin monomer, ethylene pressure, and reaction temperature played crucial roles in determining the distribution of products. In presence of ethylene and 1-hexene, the primary high-carbon products are C10 olefins. In contrast, when ethylene and 1-octene are present, the main high-carbon products are C12 olefins. Increasing temperature and reducing pressure can promote the oligomerization of α-olefins with ethylene, thereby significantly improving the selectivity of high-carbon products. Detailed identities of C10-C14 olefins, assigned by gas chromatographic and mass spectrometric, strongly supported a mechanism involves five-, seven- and nine-membered metallacyclic intermediates composed by ethylene and α-olefins units. Mechanistic analysis of C12 and C14 isomers revealed that co-trimerization and co-tetramerization reactions occurred concurrently during the reaction process. Furthermore, the concentration of specific carbon-number olefins, along with the reaction conditions, influenced the relative probability of the two pathways.

Graphical abstract