Selective Ring Opening of Ethylbenzene on Bifunctional Catalyst Pt-Ir over Hierarchical USY Zeolite

被引:1
|
作者
Elena Perez-Guevara [1 ,2 ,3 ]
Molinillo, Jose M. G. [2 ]
Martinez de la Ossa, Enrique J. [3 ]
Frontela, Juana [1 ]
Lazaro, Jesus [1 ]
Franco, Maria Jose [1 ]
机构
[1] Compania Espanola Petr SAU, Cepsa Res Ctr, Madrid 28850, Spain
[2] Univ Cadiz, Inst Biomol INBIO, Sch Sci, Dept Organ Chem, Cadiz 11510, Spain
[3] Univ Cadiz, Sch Sci, Dept Chem Engn & Food Technol, Cadiz 11510, Spain
关键词
selective ring opening; noble metal; hierarchical zeolite; ion exchange; cetane number; COUPLED HYDROGENATION; CETANE NUMBER; DECALIN; DIESEL; METAL; METHYLCYCLOHEXANE; METHYLCYCLOPENTANE; HYDROCONVERSION; HYDROCARBONS; SUPPORT;
D O I
10.1134/S0965544120010119
中图分类号
O62 [有机化学];
学科分类号
070303 ; 081704 ;
摘要
A bifunctional catalyst for selective ring opening (SRO) has been designed using a hierarchical zeolite as support. This material was prepared introducing additional mesoporosity in the microporous structure of a USY zeolite, by surfactant-templating post-synthetic mesostructuring process. Monometallic and bimetallic Pt(x)-Ir(y) catalysts with different metal loadings and Pt/Ir mole ratio have been prepared. In addition, to optimise the acid-metal balance, the acidity of the support has been modulated via ion-exchange process with Na+. The catalytic behaviour of the prepared materials has been evaluated with ethylbenzene hydrogenation and SRO simultaneous reaction in a continuous-flow fixed-bed reactor, at 275 degrees C and 3 MPa. Pt(2)-Ir(1) resulted the most promising metallic combination. The high hydrogenolytic activity of Ir, along with the high hydrogenation activity and cracking limitation of Pt attained a high paraffins production. This behaviour was improved modulating the acidity of the support. Thus, Pt(2)-Ir(1)/Na-FAU-CTAB catalyst maximized the yield to paraffins which improve the cetane number of fuels.
引用
收藏
页码:104 / 112
页数:9
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