1 - 1 |
Preface to Escape SI Fonyo Z, Rev E |
3 - 14 |
Properties and CAPE: from present uses to future challenges Gani R, O'Connell JP |
15 - 26 |
On-line optimal trajectory control for a fermentation process using multi-linear models Azimzadeh F, Galan O, Romagnoli JA |
27 - 40 |
Quality costs and robustness criteria in chemical process design optimization Bernardo FP, Pistikopoulos EN, Saraiva PM |
41 - 48 |
Multiplicity and stability approach to the design of heat-integrated multibed plug flow reactor Bildea CS, Dimian AC, Iedema PD |
49 - 60 |
Systematic structure generation for reactive distillation processes Giessler S, Danilov RY, Pisarenko RY, Serafimov LA, Hasebe S, Hashimoto I |
61 - 72 |
An integrated approach to early process hazard identification of continuous and batch plants with statechart modelling and simulation Graf H, Schmidt-Traub H |
73 - 83 |
Integration of thermodynamic insights and MINLP optimization for the synthesis, design and analysis of process flowsheets Hostrup M, Gani R, Kravanja Z, Sorsak A, Grossmann I |
85 - 95 |
A study on the evaluation of structural controllability in chemical processes Lee B, Kim Y, Shin D, Yoon ES |
97 - 107 |
Tracking the predefined optimal policies for multiple-fraction batch distillation by using adaptive control Li P, Wozny G |
109 - 117 |
Optimal structure and on-line optimal operation of batch distillation column Noda M, Kato A, Chida T, Hasebe S, Hashimoto I |
119 - 140 |
Energy savings of integrated and coupled distillation systems Rev E, Emtir M, Szitkai Z, Mizsey P, Fonyo Z |
141 - 150 |
Optimal design and control of a high-purity industrial distillation system Ross R, Perkins JD, Pistikopoulos EN, Koot GLM, van Schijndel JMG |
151 - 160 |
Fault diagnosis support system for complex chemical plants Ruiz D, Nougues JM, Puigjaner L |
161 - 167 |
Receding horizon iterative dynamic programming with discrete time models Rusnak A, Fikar M, Latifi MA, Meszaros A |
169 - 176 |
Dynamic modeling and simulation of reactive batch distillation Schneider R, Noeres C, Kreul LU, Gorak A |
177 - 188 |
Process design and control structure screening based on economic and static controllability criteria Seferlis P, Grievink J |