Title of article :
Xylene transformation over USY zeolite: an experimental and kinetic study Original Research Article
Author/Authors :
A Iliyas، نويسنده , , S Al-Khattaf، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2004
Pages :
12
From page :
225
To page :
236
Abstract :
A systematic study on the influence of reaction conditions (temperature, time, and reactant type) on the selectivity of xylene transformation has been carried out over USY zeolite. Initial product selectivity revealed that both isomerization and disproportionation of xylenes are primary reactions. Higher conversion was observed with p-xylene reactant as compared to m- and o-xylene. The “reactant converted” deactivation model was tested with xylenes as model compounds, using effective, mechanistic kinetic models, developed from the transformation of each xylene isomers. The parameters optimized to the experimental data gave a good prediction of the overall reaction kinetics for the xylene transformations. The results provide significant evidence that the “reactant converted” decay model can be adequately utilized to account for catalyst deactivation of the xylene transformation.
Keywords :
Xylene transformation , Catalyst deactivation model , Kinetic modeling , Fluidized-bed reactor , USY zeolite
Journal title :
Applied Catalysis A:General
Serial Year :
2004
Journal title :
Applied Catalysis A:General
Record number :
1151572
Link To Document :
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