Monday, November 14, 2016

Experimental and kinetic study of catalytic cracking of heavy fuel oil over E-CAT/MCM-41 catalyst



Type
Journal Article
Author
A. A. Ebrahimi
Author
S. Tarighi
URL
Volume
57
Issue
5
Pages
610-616
Publication
Kinetics and Catalysis
Date
2016/09/01
Abstract
Reports a study of the catalytic cracking of heavy fuel oil over the equilibrium fluid catalytic cracking catalyst (E-Cat) as a base component with the mesoporous MCM-41 as an additive. Researchers examined the catalytic performance of the E-Cat/MCM-41 system in a fixed-bed MAT unit. The yields of products including light olefins, liquefied petroleum gas (LPG), gasoline, dry gas, coke and also the conversions obtained over different temperatures were reported and some generalities discussed.
The maximum yield of propylene (17.5%) was obtained at 550°C whereas the highest conversion and gasoline yield was gained at 530°C. An eight-lump kinetic model containing 11 kinetic parameters was considered. Those parameters were estimated based on experimental data at specific temperatures by fourth order Runge–Kutta algorithm and the least square method. In addition, Arrhenius equation was used to calculate apparent activation energies.

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