摘要
研究钯催化体系在不同温度、压力、时间下对乙炔环三聚制苯反应的影响,提出催化反应机理。结果表明,以(Ph_3P)_2PdCl_2/CuCl为催化体系,N-甲基吡咯烷酮为溶剂,在反应压力2.5 MPa、反应温度140℃、反应时间2 h条件下,乙炔转化率99.8%,苯收率26.3%,副产物主要是聚乙炔、乙炔铜和少量芳香族化合物。此催化体系具有反应条件温和、反应进料组分简单、成本低等优点。
Acetylene cyclotrimerization were investigated at different temperature, pressure and reaction time with different palladium catalytic systems. Reaction mechanism was proposed. The results showed that yield of benzene could reach 26.3% and conversion of acetylene was 99.8% under 2.5 MPa at 150 ℃ for 2 h, while catalyst were (Ph3P)2PdCl2/CuCl and N- methyl pyrrolidone used as solvent. By- prod- ucts were polyacetylene, copper acetylide and few aromatic compounds. The catalytic system had advanta- ges of mild reaction conditions, simple reaction feed composition and low cost.
作者
黄伟
明瑞光
史雪君
史权
吴道洪
Huan Wei;Ming Ruiguang;Shi Xuejun;Shi Quan;Wu Daohong(Shenwu Technology Group Corp,Beijing 102200,China;Hubei Industrial Polytechnic,Shiyan 442000,Hubei,China;College of Chemical Engineering,China University of Petroleum,Beijing 102249,China)
出处
《工业催化》
CAS
2018年第6期53-56,共4页
Industrial Catalysis
关键词
精细化学工程
乙炔
环三聚
钯催化剂
苯
芳烃
fine chemical engineering
acetylene
cyclotrimerization
palladium catalyst
benzene
aromatic hydrocarbons