Rigorous Dynamic Simulation of an Industrial Tray Column, Considered Liquid Flow Regime and Efficiency of Trays

Author:

Mahdipoor H.R.,Shirvani M.,Jafari Nasr M.R.,Shakiba S.

Publisher

Elsevier BV

Subject

General Chemical Engineering,General Chemistry

Reference14 articles.

1. Principles and modern applications of mass transfer operations;Benitez,2002

2. New correlation for sieve-tray point efficiency, entrainment, and section efficiency;Bennett;AIChE J,1997

3. Rigorous industrial dynamic simulation of a crude distillation unit considered valve tray rating parameters;Chang;Computers Chem Eng,1998

4. A generalized model for distillation columns—I;Gani;Comput Chem Engng,1986

5. Distillation Design;Kister,1989

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2. Dynamic models for safety shutdown of distillation columns;Chemical Engineering Research and Design;2015-07

3. Application of Mirror Model for Dynamic Behavior of Tray Efficiency to Revise Control Loops in Distillation Systems;Journal of Chemical Engineering of Japan;2015

4. A Hybrid Discrete/Continuous Dynamic Model of Trayed Tower Hydraulics;12th International Symposium on Process Systems Engineering and 25th European Symposium on Computer Aided Process Engineering;2015

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