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
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.