Simulation, optimization and control of the process of synthesis of ethyl propionate by reactive distillation

2022 ◽  
pp. 108779
Author(s):  
Peng Du ◽  
Xiaohong Wang ◽  
Zenghu Tian ◽  
Jingxuan Chen ◽  
Xin Ding
Keyword(s):  
Reactive Distillation ◽  
Simulation Optimization ◽  
Ethyl Propionate ◽  
Optimization And Control ◽  
And Control

Modelling, simulation, optimization and control of multistage flashing (MSF) desalination plants Part II: Optimization and control

Desalination ◽  
1993 ◽  
Vol 92 (1-3) ◽  
pp. 43-55 ◽  
Author(s):  
Asghar Husain ◽  
Darwish M.K. Al-Gobaisi ◽  
Ali Hasan ◽  
A. Kesou ◽  
A. Kurdali ◽  
...  
Keyword(s):  
Simulation Optimization ◽  
Optimization And Control ◽  
Desalination Plants ◽  
And Control ◽  
Modelling Simulation

Simulation, optimization and control of a thermal cracking furnace

Energy ◽  
2006 ◽  
Vol 31 (4) ◽  
pp. 516-527 ◽  
Author(s):  
M MASOUMI ◽  
S SADRAMELI ◽  
J TOWFIGHI ◽  
A NIAEI
Keyword(s):  
Simulation Optimization ◽  
Thermal Cracking ◽  
Optimization And Control ◽  
And Control

scholarly journals Dynamic Simulation, Parameter Optimization, and Control of a Reactive Distillation Column for Production of Isopropanol via Propylene Hydration

2021 ◽  
Vol 34 (4) ◽  
pp. 233-242
Author(s):  
Bahareh Feizi-Afshar ◽  
Ali Farzi
Keyword(s):  
Distillation Column ◽  
Reactive Distillation ◽  
Freezing Point ◽  
Base Case ◽  
Operating Variables ◽  
Point Tracking ◽  
Condenser Temperature ◽  
Optimization And Control ◽  
Simulation Parameter ◽  
And Control

In this study, a reactive distillation column for production of isopropanol was investigated. Firstly, a dynamic model was developed for the process. The model of the process was then programmed, and the process simulated using a base case obtained from the literature. Results showed that distillate contained more than 58 mol% propylene-free<br /> isopropanol. In the next step, optimization of some operating variables was performed to<br /> maximize concentration of isopropanol in distillate with condenser temperature as constraint, which was considered to be above the freezing point of water. Several simulations were performed by changing operating parameters, and finally optimum isopropanol content in distillate was obtained above 58 mol%. Results of using classic controllers showed that PID controller had the best performance for both condenser temperature set-point tracking and disturbance rejection.

Optimization and control of a reactive distillation process for the synthesis of dimethyl carbonate

2017 ◽  
Vol 25 (8) ◽  
pp. 1079-1090 ◽  
Author(s):  
Zhixian Huang ◽  
Yixiong Lin ◽  
Xiaoda Wang ◽  
Changshen Ye ◽  
Ling Li
Keyword(s):  
Dimethyl Carbonate ◽  
Reactive Distillation ◽  
Distillation Process ◽  
Optimization And Control ◽  
And Control
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