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- W2015162400 abstract "Abstract The hydroconversion of a n -heptane–methylcyclohexane–toluene mixture representative of FCC gasoline was analyzed through a lumped parameter reaction model that incorporates the main reaction paths and the acid/metal sites ratio of the catalyst as an explicit key parameter. The catalytic experiments were performed at relevant operating conditions using mechanical mixtures of metal/alumina+HZSM5 powders. The catalyst acid/metal sites ratio was modified by changing the type of metal and metal content. The observed main reaction paths were isomerization and cracking of n -heptane, and methylcyclohexane, and aromatic alkylation reactions. The first and last routes were the most sensitive to small changes in the catalyst acid/metal sites balance. It was found that the mathematical model reproduces well the catalytic behavior of the hydroconversion process when the acid/metal sites ratio of the catalyst is varied." @default.
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- W2015162400 date "2004-11-01" @default.
- W2015162400 modified "2023-10-16" @default.
- W2015162400 title "Hydroconversion of model mixtures of FCC gasoline over metal–zeolite catalysts. Reaction study and mathematical modelling" @default.
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- W2015162400 doi "https://doi.org/10.1016/j.ces.2004.07.048" @default.
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