| 2109 - 2129 |
Continuous-time versus discrete-time approaches for scheduling of chemical processes: a review
Floudas CA, Lin XX |
| 2131 - 2140 |
A two-step supervisory fault diagnosis framework
Power Y, Bahri PA |
| 2141 - 2155 |
"Store and retrieve" representations of dynamic systems motivated by studies in gas phase chemical kinetics
Androulakis IP |
| 2157 - 2164 |
Biological reaction modeling using radial basis function networks
Vande Wouwer A, Renotte C, Bogaerts P |
| 2165 - 2188 |
A decomposition method for synthesizing complex column configurations using tray-by-tray GDP models
Barttfield M, Aguirre PA, Grossmann IE |
| 2189 - 2192 |
An improved MT-NT method for gross error detection and data reconciliation
Wang F, Jia XP, Zheng SQ, Yue JC |
| 2193 - 2200 |
Flowsheet decomposition heuristic for scheduling: a relax-and-fix method
Kelly JD, Mann JL |
| 2201 - 2218 |
A simple method of tuning PID controllers for stable and unstable FOPTD systems
Sree RP, Srinivas MN, Chidambaram M |
| 2219 - 2231 |
Scalable multi-objective optimization of industrial purified terephthalic acid (PTA) oxidation process
Mu SJ, Su HY, Jia T, Gu Y, Chu J |
| 2233 - 2244 |
CFD modeling of conjugate heat transfer and homogeneously mixing two different fluids in a stirred and heated hemispherical vessel
Yapici H, Basturk G |
| 2245 - 2258 |
Thermodynamic uncertainties in batch processing and optimal control
Ulas S, Diwekar UM |
| 2259 - 2270 |
Multivariable model predictive control of a catalytic reverse flow reactor
Dufour P, Toure Y |
| 2271 - 2286 |
Cyclic short-term scheduling of multiproduct batch plants using continuous-time representation
Wu D, Ierapetritou M |
| 2287 - 2306 |
Tabu search algorithm for chemical process optimization
Lin B, Miller DC |
| 2307 - 2329 |
Design of distillation sequences: from conventional to fully thermally coupled distillation systems
Caballero JA, Grossmann IE |
| 2331 - 2335 |
A new method for sizing mass exchange units without the singularity of the Kremser equation
Fraser DM, Shenoy UV |
| 2337 - 2349 |
A numerical method for the solution of the wave model and convection dominated diffusion type models for catalytic packed bed reactors
Iordanidis AA, Annaland MV, Kronberg AE, Kuipers JAM |
| 2351 - 2361 |
Post-processing of detailed chemical kinetic mechanisms onto CFD simulations
Skjoth-Rasmussen MS, Holm-Christensen O, Ostberg M, Christensen TS, Johannessen T, Jensen AD, Glarborg P, Livbjerg H |
| 2363 - 2375 |
An adaptive remeshing strategy for shear-thinning fluid flow simulations
Fortin A, Bertrand F, Fortin M, Chamberland E, Boulanger-Nadeau PE, El Maliki A, Najeh N |
| 2377 - 2390 |
Optimisation of design and operation policies of binary batch distillation with fixed product demand
Miladi MM, Mujtaba IM |
| 2391 - 2406 |
On the synthesis and optimization of liquid-liquid extraction processes using stochastic search methods
Papadopoulos AI, Linke P |
| 2407 - 2419 |
Neural network-based prediction and optimization of estradiol release from ethylene-vinyl acetate membranes
Simon L, Fernandes M |
| 2421 - 2431 |
Dynamic modelling of an adsorption storage tank using a hybrid approach combining computational fluid dynamics and process simulation
Mota JPB, Esteves IAAC, Rostam-Abadi M |
| 2433 - 2437 |
Simple method of calculatingset point weighting parameter for unstable systems with a zero
Sree RP, Chidambaram M |
