First principle modeling of an industrial fluid catalytic cracking - the adaptation of the model

Roman Raluca, Zoltan K. Nagy, Paul S. Agachi

Research output: Chapter in Book/Report/Conference proceedingChapter

Abstract

A complex dynamic model of the reactor-regenerator-fractionator system of an industrial FCCU is developed. The novelty of the model consists on the complex dynamics of the reactor-regenerator system and it also includes the dynamic model of the fractionator, as well as a new five lumped kinetic model for the riser, and hence it is able to predict the final production rate of the main products (gasoline and diesel). Based on the experimental data comparisons between the simulated output values and industrial data have been done, for certain disturbance scenarios.

Original languageEnglish
Title of host publication17th European Symposium on Computer Aided Process Engineering
EditorsValentin Plesu, Paul Serban Agachi
Pages87-92
Number of pages6
DOIs
Publication statusPublished - Dec 1 2007

Publication series

NameComputer Aided Chemical Engineering
Volume24
ISSN (Print)1570-7946

All Science Journal Classification (ASJC) codes

  • Chemical Engineering(all)
  • Computer Science Applications

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    Raluca, R., K. Nagy, Z., & S. Agachi, P. (2007). First principle modeling of an industrial fluid catalytic cracking - the adaptation of the model. In V. Plesu, & P. S. Agachi (Eds.), 17th European Symposium on Computer Aided Process Engineering (pp. 87-92). (Computer Aided Chemical Engineering; Vol. 24). https://doi.org/10.1016/S1570-7946(07)80038-1