RIGOROUS INDUSTRIAL DYNAMIC SIMULATION OF A CRUDE DISTILLATION UNIT CONSIDERED VALVE TRAY RATING PARAMETERS

Citation
B. Chang et al., RIGOROUS INDUSTRIAL DYNAMIC SIMULATION OF A CRUDE DISTILLATION UNIT CONSIDERED VALVE TRAY RATING PARAMETERS, Computers & chemical engineering, 22, 1998, pp. 863-866
Citations number
5
Categorie Soggetti
Computer Science Interdisciplinary Applications","Engineering, Chemical","Computer Science Interdisciplinary Applications
ISSN journal
00981354
Volume
22
Year of publication
1998
Supplement
S
Pages
863 - 866
Database
ISI
SICI code
0098-1354(1998)22:<863:RIDSOA>2.0.ZU;2-K
Abstract
A rigorous dynamic simulation is performed to find optimal operating c onditions of a crude distillation unit with 56 trays and 65,000 barrel per day capacity. The model includes not only mass and energy balance equations but also nonlinear equations capturing the fluid behavior i n the column such as downcomer load;jet flooding, hole velocity limit and downcomer backup. Discrete behavior of pump and heater on/off, val ve open/close are also included. Hundreds of thousand differential alg ebraic equations(DAEs) are set up and solved by gPROMS simultaneously. As a result, the dynamic behavior of the unit during the starting and shutdown procedure is fully understood. (C) 1998 Published by Elsevie r Science Ltd. All rights reserved.