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An Original Approach for the Dynamic Simulation of a Crude Oil Distillation Plant : 2. Setting-up and Testing the Simulator

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Radulescu,  G.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Petroleum – Gas University of Ploiesti, Ploiesti, Romania;

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Kienle,  A.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Otto-von-Guericke-Universität Magdeburg, External Organizations;

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Citation

Radulescu, G., Paraschiv, N., & Kienle, A. (2007). An Original Approach for the Dynamic Simulation of a Crude Oil Distillation Plant: 2. Setting-up and Testing the Simulator. Revista de Chimie, 58(3), 349-354.


Cite as: https://hdl.handle.net/11858/00-001M-0000-0013-98E5-4
Abstract
The dynamic simulation of a crude oil unit is useful in understanding the unusual behavior of such a complex plant, which is induced by the dynamics of individual sub-processes in combination with the complex plant topology. Also, it serves to investigate suitable strategies for process control, including closed-loop operation at the nominal operating point, load and specification changes, as well as startup procedures [1]. The model presented in the first part of the study [2] becomes now the simulator kernel - of course, with additional elements in order to respect the physical reality of the crude oil distillation unit, by using the powerful and versatile DIVA software environment [3,4]. Both plant "open-loop" and "closed loop" simulation results are presented, proving good performances as fast simulation and accurate results.