Terminal composition control of a binary distillation column

1973 ◽  
Vol 28 (9) ◽  
pp. 1707-1717 ◽  
Author(s):  
R.K. Wood ◽  
M.W. Berry
1988 ◽  
Vol 21 (7) ◽  
pp. 193-198 ◽  
Author(s):  
C.S. Nielsen ◽  
H.W. Andersen ◽  
H. Brabrand ◽  
S.B. Jørgensen

2012 ◽  
Vol 40 ◽  
pp. 157-170 ◽  
Author(s):  
J. Fernandez de Canete ◽  
P. del Saz-Orozco ◽  
S. Gonzalez ◽  
I. Garcia-Moral

2011 ◽  
Vol 6 (1) ◽  
Author(s):  
Kulchanat Prasertsit ◽  
Chakrit Tongurai ◽  
Chokchai Mueanmas

The temperature control and the composition control for the production process was used to evaluated a method to control the quality of methyl ester production in a reactive distillation column. The optimum condition at steady state was selected as the base case condition for the control study by using Aspen Dynamic Simulation. In this work, two controller settings for PID controller of each control loop were based on the Zeigler-Nichol and the Tyreus-Luyben tuning formulae. The controllability and performance of both control structures were compared. The result shows that the control loop using the Ziegler-Nichols setting gave better control performance than the other using the Tyreus-Luyben setting. It also found that the control structure based on temperature control gives the same control performance as the other based on composition control, but less expensive and less complicated to implement.


2001 ◽  
Vol 40 (20) ◽  
pp. 4377-4390 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Jose Alvarez-Ramirez

Sign in / Sign up

Export Citation Format

Share Document