Modeling and Control of Tray Temperature along with Column Pressure in a Pilot Plant Distillation Column

2019 ◽  
Author(s):  
I. Thirunavukkarasu ◽  
R. Janani ◽  
Eadala Sarath Yadav ◽  
Shanmuga Priya Selvanathan
Keyword(s):  
Pilot Plant ◽  
Distillation Column ◽  
Modeling And Control ◽  
Column Pressure ◽  
And Control

scholarly journals Modeling and Control of Tray Temperature Along with Column Pressure in a Pilot Plant Distillation Column

2020 ◽  
Vol 1 (6) ◽  
Author(s):  
Janani Rajaraman ◽  
Thirunavukkarasu Indiran ◽  
Eadala Sarath Yadav ◽  
Shanmuga Priya Selvanathan
Keyword(s):  
Pilot Plant ◽  
Distillation Column ◽  
Modeling And Control ◽  
Column Pressure ◽  
And Control

Laboratory Pilot Plant for Modeling and Control Education

1988 ◽  
Vol 21 (6) ◽  
pp. 49-52
Author(s):  
B. Zupančič ◽  
R. Karba ◽  
D. Matko ◽  
M. Atanasijević ◽  
S. Strmčnik ◽  
...  
Keyword(s):  
Pilot Plant ◽  
Modeling And Control ◽  
Control Education ◽  
And Control

Object-oriented approach applied to ANFIS modeling and control of a distillation column

2013 ◽  
Vol 40 (14) ◽  
pp. 5648-5660 ◽  
Author(s):  
J. Fernandez de Canete ◽  
A. Garcia-Cerezo ◽  
I. Garcia-Moral ◽  
P. Del Saz ◽  
E. Ochoa
Keyword(s):  
Distillation Column ◽  
Object Oriented ◽  
Modeling And Control ◽  
Object Oriented Approach ◽  
And Control ◽  
Oriented Approach

scholarly journals Modeling and Control of Distillation Column in a Petroleum Process

2009 ◽  
Vol 2009 ◽  
pp. 1-14 ◽  
Author(s):  
Vu Trieu Minh ◽  
Ahmad Majdi Abdul Rani
Keyword(s):  
Linear Model ◽  
Distillation Column ◽  
Reference Model ◽  
Adaptive Controller ◽  
Modeling And Control ◽  
Reduced Order ◽  
Order Linear ◽  
Balance Structure ◽  
And Control ◽  
Model Reference Adaptive

This paper introduces a calculation procedure for modeling and control simulation of a condensate distillation column based on the energy balance structure. In this control, the reflux rate and the boilup rate are used as the inputs to control the outputs of the purity of the distillate overhead and the impurity of the bottom products. The modeling simulation is important for process dynamic analysis and the plant initial design. In this paper, the modeling and simulation are accomplished over three phases: the basic nonlinear model of the plant, the full-order linearised model, and the reduced-order linear model. The reduced-order linear model is then used as the reference model for a model-reference adaptive control (MRAC) system to verify the applicable ability of a conventional adaptive controller for a distillation column dealing with the disturbance and the model-plant mismatch as the influence of the plant feed disturbances.

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