在基于 N-杂芳基取代的 α-二苯基膦甘氨酸的镍络合物存在下催化合成乙烯的均相低聚物中的丁烯-1 和己烯-1

IF 1.3 4区 化学 Q4 CHEMISTRY, PHYSICAL
O. S. Soficheva, G. E. Bekmukhamedov, D. G. Yakhvarov
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引用次数: 0

摘要

摘要 试验表明,N-杂芳基取代的α-二苯基膦甘氨酸,即N-(吡嗪-2-基)α-二苯基膦甘氨酸、N-(吡啶-2-基)α-二苯基膦甘氨酸和N-(嘧啶-2-基)α-二苯基膦甘氨酸,是由二苯基膦的三组分缩合合成的、与 Ni(COD)2(其中 COD 为环辛二烯-1,5)结合后,能够生成活性催化剂,用于乙烯的选择性均相二聚化和三聚化,形成丁烯-1 和己烯-1 作为主要产物。所研究的有机螯合催化剂体系的短链(C4-C6)烯烃产率为 90%,线性 α 烯烃选择性为 97%。研究温度对使用合成化合物进行乙烯均相低聚作用的影响时发现,在 80-105°C 的最佳温度和 20-35 atm 的最佳乙烯压力下运行工艺,丁烯-1 和己烯-1 的选择性最高。在这些条件下,丁烯选择性为 71.4-72.6%(丁烯-1 选择性为 69.3-71.1%),己烯选择性为 20.6-21.2%(己烯-1 选择性为 19.2-19.5%)。丁烯-1 和己烯-1 的形成速率分别为 168.1 和 47.3 golig \({text{g}}_{{text\{Ni}}}}^{ - 1}})h-1。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Catalytic Synthesis of Butene-1 and Hexene-1 in the Homogeneous Oligomerization of Ethylene in the Presence of Nickel Complexes Based on N-Heteroaryl-Substituted α-Diphenylphosphinoglycines

Catalytic Synthesis of Butene-1 and Hexene-1 in the Homogeneous Oligomerization of Ethylene in the Presence of Nickel Complexes Based on N-Heteroaryl-Substituted α-Diphenylphosphinoglycines

Catalytic Synthesis of Butene-1 and Hexene-1 in the Homogeneous Oligomerization of Ethylene in the Presence of Nickel Complexes Based on N-Heteroaryl-Substituted α-Diphenylphosphinoglycines

It has been shown in tests that N-heteroaryl-substituted α-diphenylphosphinoglycines, namely, N-(pyrazin-2-yl) α-diphenylphosphinoglycine, N-(pyridin-2-yl) α-diphenylphosphinoglycine, and N‑(pyrimidin-2-yl) α-diphenylphosphinoglycine, which are synthesized by the three-component condensation of diphenylphosphine, the respective primary amine, and glyoxylic acid monohydrate, being combined with Ni(COD)2, where COD is cyclooctadiene-1,5, are capable of generating active forms of catalysts for the selective homogeneous dimerization and trimerization of ethylene to form butene-1 and hexene-1 as the main products. The studied organonichel catalyst systems provide a yield of short-chain (C4–C6) olefins at a level of 90% with a linear α-olefin selectivity of 97%. Studies of the effect of temperature on the homogeneous oligomerization of ethylene using the synthesized compounds have revealed that the process run at an optimum temperature of 80–105°C and an optimum ethylene pressure of 20–35 atm provides the highest butene-1 and hexene-1 selectivity. Under these conditions, the butene selectivity is recorded at a level of 71.4–72.6% (butene-1 selectivity of 69.3–71.1%), while the hexene selectivity is 20.6–21.2% (hexene-1 selectivity of 19.2–19.5%). The optimum duration of the oligomerization process at a temperature of 105°C is 1.5 h. The butene-1 and hexene-1 formation rate is 168.1 and 47.3 golig \({\text{g}}_{{{\text{Ni}}}}^{{ - 1}}\) h–1, respectively.

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来源期刊
Kinetics and Catalysis
Kinetics and Catalysis 化学-物理化学
CiteScore
2.10
自引率
27.30%
发文量
64
审稿时长
6-12 weeks
期刊介绍: Kinetics and Catalysis Russian is a periodical that publishes theoretical and experimental works on homogeneous and heterogeneous kinetics and catalysis. Other topics include the mechanism and kinetics of noncatalytic processes in gaseous, liquid, and solid phases, quantum chemical calculations in kinetics and catalysis, methods of studying catalytic processes and catalysts, the chemistry of catalysts and adsorbent surfaces, the structure and physicochemical properties of catalysts, preparation and poisoning of catalysts, macrokinetics, and computer simulations in catalysis. The journal also publishes review articles on contemporary problems in kinetics and catalysis. The journal welcomes manuscripts from all countries in the English or Russian language.
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