TY - CHAP
T1 - First principle modeling of an industrial fluid catalytic cracking - the adaptation of the model
AU - Raluca, Roman
AU - K. Nagy, Zoltan
AU - S. Agachi, Paul
PY - 2007
Y1 - 2007
N2 - 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.
AB - 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.
UR - http://www.scopus.com/inward/record.url?scp=43049112845&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=43049112845&partnerID=8YFLogxK
U2 - 10.1016/S1570-7946(07)80038-1
DO - 10.1016/S1570-7946(07)80038-1
M3 - Chapter
AN - SCOPUS:43049112845
SN - 9780444531575
T3 - Computer Aided Chemical Engineering
SP - 87
EP - 92
BT - 17th European Symposium on Computer Aided Process Engineering
PB - Elsevier
ER -