Optimal operation of a pyrolysis reactor

In the present study, the problem of optimization of thermal cracker (pyrolysis) operation is discussed. The main objective in thermal cracker optimization is the estimation of the optimal flow rates of different feeds (such as, Gas-oil, Propane, Ethane and Debutanized natural gasoline) to the crack...

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Published inComputer Aided Chemical Engineering Vol. 37; pp. 827 - 832
Main Authors Jarullah, Aysar T., Hameed, Shemaa A., Hameed, Zina A., Mujtaba, I.M.
Format Book Chapter
LanguageEnglish
Published 2015
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ISBN9780444634290
0444634290
ISSN1570-7946
DOI10.1016/B978-0-444-63578-5.50133-X

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Abstract In the present study, the problem of optimization of thermal cracker (pyrolysis) operation is discussed. The main objective in thermal cracker optimization is the estimation of the optimal flow rates of different feeds (such as, Gas-oil, Propane, Ethane and Debutanized natural gasoline) to the cracking furnace under the restriction on ethylene and propylene production. Thousands of combinations of feeds are possible. Hence the optimization needs an efficient strategy in searching for the global minimum. The optimization problem consists of maximizing the economic profit subject to a number of equality and inequality constraints. Modelling, simulation and optimal operation via optimization of the thermal cracking reactor has been carried out by gPROMS (general PROcess Modelling System) software. The optimization problem is posed as a Non-Linear Programming problem and using a Successive Quadratic Programming (SQP) method for solving constrained nonlinear optimization problem with high accuracy within gPROMS software. New results have been obtained for the control variables and optimal cost of the cracker in comparison with previous studies.
AbstractList In the present study, the problem of optimization of thermal cracker (pyrolysis) operation is discussed. The main objective in thermal cracker optimization is the estimation of the optimal flow rates of different feeds (such as, Gas-oil, Propane, Ethane and Debutanized natural gasoline) to the cracking furnace under the restriction on ethylene and propylene production. Thousands of combinations of feeds are possible. Hence the optimization needs an efficient strategy in searching for the global minimum. The optimization problem consists of maximizing the economic profit subject to a number of equality and inequality constraints. Modelling, simulation and optimal operation via optimization of the thermal cracking reactor has been carried out by gPROMS (general PROcess Modelling System) software. The optimization problem is posed as a Non-Linear Programming problem and using a Successive Quadratic Programming (SQP) method for solving constrained nonlinear optimization problem with high accuracy within gPROMS software. New results have been obtained for the control variables and optimal cost of the cracker in comparison with previous studies.
Author Hameed, Shemaa A.
Mujtaba, I.M.
Jarullah, Aysar T.
Hameed, Zina A.
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Keywords SQP
Mathematical Modeling
Olefins Pyrolysis
Thermal Cracking
Language English
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Joo, Park, Lee (bb0035) 2001; 40
Masoumi, Sadrameli, Towfighi, Niaei (bb0055) 2006; 31
Geddes, Kubera (bb0020) 2000; 2-7
Jarullah, Mujtaba, Wood (bb0025) 2011; 90
Edgar, Himmelblau (bb0015) 2001
Lee, Aitani (bb0045) 1990; 88
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  publication-title: Comput. Chem. Eng.
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  article-title: Kinetic Model Development and Simulation of Simultaneous Hydrodenitrogenation and Hydrodemetallization of Crude Oil in a Trickle-Bed Reactor
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Snippet In the present study, the problem of optimization of thermal cracker (pyrolysis) operation is discussed. The main objective in thermal cracker optimization is...
SourceID elsevier
SourceType Publisher
StartPage 827
SubjectTerms Mathematical Modeling
Olefins Pyrolysis
SQP
Thermal Cracking
Title Optimal operation of a pyrolysis reactor
URI https://dx.doi.org/10.1016/B978-0-444-63578-5.50133-X
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