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Special issue: ESCAPE-12 - Preface Grievink J, van Schijndel J |
3 - 15 |
A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants Alle A, Papageorgiou LG, Pinto JM |
17 - 25 |
Feasibility of equilibrium-controlled reactive distillation process: application of residue curve mapping Almeida-Rivera C, Grievink J |
27 - 35 |
Optimal sensor location and reduced order observer design for distributed process systems Alonso AA, Kevrekidis IG, Banga JR, Frouzakis CE |
37 - 44 |
Selection of internals for reactive distillation column - case-based reasoning approach Avramenko Y, Nystrom L, Kraslawski A |
45 - 61 |
Planning, scheduling and budgeting value-added chains Badell M, Romero J, Huertas R, Puigjaner L |
63 - 72 |
Design of tubular reactors in recycle systems Bildea CS, Dimian AC, Cruz SC, Iedema PD |
73 - 81 |
CAPD - computer-aided plant design Burdorf A, Kampczyk B, Lederhose M, Schmidt-Traub H |
83 - 90 |
Multiobjective process controllability analysis Cao Y, Yang ZJ |
91 - 102 |
Short-term site-wide maintenance scheduling Cheung KY, Hui CW, Sakamoto H, Hirata K, O'Young L |
103 - 109 |
Optimal design of membrane processes for wastewater treatment and metal recovery Corvalan SM, Ortiz I, Eliceche AM |
111 - 128 |
Coordinating feedback and switching for control of spalially distributed processes El-Farra NH, Christofides PD |
129 - 137 |
The effect of model simplification assumptions on the differential index of lumped process models Hangos KM, Szederkenyi G, Tuza Z |
139 - 148 |
Multi-site utility integration - an industrial case study Hirata K, Sakamoto H, O'Young L, Cheung KY, Hui CW |
149 - 160 |
Automating reactor network synthesis: finding a candidate attainable region for the water-gas shift (WGS) reaction Kauchali S, Hausberger B, Hildebrandt D, Glasser D, Biegler LT |
161 - 169 |
On the use of reduced order models in bifurcation analysis of distributed parameter systems Liu Y, Jacobsen EW |
171 - 185 |
A mixed integer programming approach for scheduling commodities in a pipeline Magatao L, Arruda LVR, Neves F |
187 - 194 |
Computation of frequency locking regions for a discontinuous periodically forced reactor Mancusi E, Russo L, Continillo G, Crescitelli S |
195 - 207 |
Robust model-based tracking control using parametric programming Sakizlis V, Dua V, Perkins JD, Pistikopoulos EN |
209 - 217 |
A new algorithm for developing dynamic radial basis function neural network models based on genetic algorithms Sarimveis H, Alexandridis A, Mazarakis S, Bafas G |
219 - 234 |
Control structure design for complete chemical plants Skogestad S |
235 - 251 |
MINLP retrofit of heat exchanger networks comprising different exchanger types Sorsak A, Kravanja Z |
253 - 265 |
Optimisation and experimental verification of startup policies for distillation columns Wozny G, Li P |
267 - 280 |
The effect of model fidelity on real-time optimization performance Yip WS, Marlin TE |