On the Steady-State Multiplicities for an Ethylene Glycol Reactive Distillation Column

1999 ◽  
Vol 38 (2) ◽  
pp. 451-455 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Jose Alvarez-Ramirez
Keyword(s):  
Steady State ◽  
Ethylene Glycol ◽  
Distillation Column ◽  
Reactive Distillation

Nonlinear PI control of an ethylene glycol reactive distillation column

1999 ◽  
Vol 23 ◽  
pp. S835-S838 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Eduardo Pérez-Cisneros ◽  
José Alvarez-Ramírez
Keyword(s):  
Ethylene Glycol ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Pi Control

A robust PI control configuration for a high-purity ethylene glycol reactive distillation column

2000 ◽  
Vol 55 (21) ◽  
pp. 4925-4937 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Eduardo Perez-Cisneros ◽  
Jose Alvarez-Ramirez
Keyword(s):  
Ethylene Glycol ◽  
High Purity ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Pi Control ◽  
Control Configuration

Theoretical study on transesterification in a combined process consisting of a reactive distillation column and a pervaporation unit

2011 ◽  
Vol 65 (2) ◽  
Author(s):  
Zuzana Švandová ◽  
Jozef Markoš
Keyword(s):  
Steady State ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Steady States ◽  
Multiple Steady States ◽  
Process Unit ◽  
Steady State Analysis ◽  
Operation Temperature ◽  
State Behaviour ◽  
State Analysis

AbstractSteady state analysis of a combined hybrid process consisting of a reactive distillation column, pervaporation unit, and a distillation column is presented. This process configuration was first presented by Steinigeweg and Gmehling (2004) for the transesterification of methyl acetate and butanol to butyl acetate and methanol. This system is characteristic for its low reaction rate and complex phase equilibrium. Steinigeweg and Gmehling (2004) have shown that the combination of reactive distillation and pervaporation is favourable since conversions close to 100 % can be reached with a reasonable size of the reactive section in the reactive distillation column. The aim of this paper is to show that although high conversion can be achieved, very complicated steady state behaviour must be expected. The presented analysis is based on mathematical modelling of a process unit, where the steady-state analysis, including continuation and bifurcation analyses, was used. Multiple steady states were predicted for the studied system; three steady states with conversions higher than 98 %. However, not all predicted steady states met the maximal allowed temperature condition in the reactive section (catalyst maximal operation temperature of 393 K). The presence of multiple steady states reduces the operability and controllability of the reactive distillation column during its start-up and during the occurrence of any variation of operating parameters because the system can be shifted from one steady state to another one (concurrent exceeding the maximal allowed temperature) with unwanted consequences, e.g. production loss. Therefore, design and subsequent operation of such a complicated system is an ambitious task requiring knowledge of any possible system behaviour.

Control of ethylene glycol reactive distillation column

AIChE Journal ◽  
2002 ◽  
Vol 48 (4) ◽  
pp. 905-908 ◽  
Author(s):  
Muhammad A. Al-Arfaj ◽  
William L. Luyben
Keyword(s):  
Ethylene Glycol ◽  
Distillation Column ◽  
Reactive Distillation

Steady-state analysis of an industrial reactive distillation column

1999 ◽  
Vol 16 (3) ◽  
pp. 251-260 ◽  
Author(s):  
Fabrizio Bezzo ◽  
Alberto Bertucco ◽  
Anna Forlin ◽  
Massimiliano Barolo
Keyword(s):  
Steady State ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Steady State Analysis ◽  
State Analysis
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