CATEGORY: HYDROCRACKING
Journal of Process Control, Volume 22, Issue 10,
December 2012, Pages 1956–1965
A
dynamic non-isothermal model for a hydrocracking reactor: Model development by
the method of continuous lumping and application to an industrial unit
Hasan Sildir a, Yaman Arkun a, Berna Cakal b, Dil a Gokce b, Emre
Kuzu b
a Department of Chemical and Biological Engineering, Koc University, Rumeli
Feneri Yolu, 34450 Sariyer, Istanbul, Turkey
b Tupras Izmit Refinery, Kocaeli, Turkey
Abstract
Modeling
of hydrocracking is a challenging task due to the large number of species and
complex reactions involved. Authors present a dynamic, non-isothermal reactor
model, constructed using the method of continuous lumping which treats the
complex reactive mixture as a continuum.
The model characterizes concentrations in terms of reactivity, which
is a monotonic function of the true boiling point of the mixture. They develop
material and energy balances in the form of integro-differential equations. They
identify and estimate significant modeling parameters using data from an
industrial reactor.
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