Acetylene selective hydrogenation: a technical review on catalytic aspects

被引:100
作者
Ravanchi, Maryam Takht [1 ]
Sahebdelfar, Saeed [1 ]
Komeili, Samane [2 ]
机构
[1] Petrochem Res & Technol Co, Natl Petrochem Co, Catalyst Res Grp, POB 14358-84711, Tehran, Iran
[2] Iran Univ Sci & Technol, Chem Engn Dept, Tehran, Iran
关键词
acetylene; ethylene; palladium catalyst; selective hydrogenation; ION-EXCHANGED COPPER; SUPPORTED PALLADIUM CATALYSTS; MODIFIED PD CATALYST; ETHENE-RICH STREAMS; PD-AG/AL2O3; CATALYSTS; EXCESS ETHYLENE; SOL-GEL; SURFACE CHARACTERIZATION; PARTICLE-SIZE; AU CATALYSTS;
D O I
10.1515/revce-2016-0036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The catalytic selective hydrogenation of multiunsaturated hydrocarbons, especially in pyrolysis products, to corresponding mono-olefins is a widely exploited way for the large-scale production of polymer-grade olefins as well as fuel upgrading. Thermodynamic and/or kinetic parameters could be effective for selective operation. The latter is primarily influenced by catalyst formulation, including promoters, support type, and metal dispersion and distribution. The solution to achieve an economically attractive commercial implementation lies in defining the optimal catalyst design and operating conditions. The theoretical and practical aspects of catalysis for the selective hydrogenation of acetylene to ethylene are reviewed and the potential new ways to improve catalyst formulation are examined.
引用
收藏
页码:215 / 237
页数:23
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