| 1171 - 1179 |
Review: Important contributions in development and improvement of the heat integration techniques
Morar M, Agachi PS |
| 1180 - 1191 |
A fast and accurate solver for the general rate model of column liquid chromatography
von Lieres E, Andersson J |
| 1192 - 1198 |
Systematic development of predictive mathematical models for animal cell cultures
Kontoravdi C, Pistikopoulos EN, Mantalaris A |
| 1199 - 1219 |
A generalized TSK model with a novel rule antecedent structure: Structure identification and parameter estimation
Su M, Rhinehart RR |
| 1220 - 1225 |
Estimation of the temporal coefficients for an empirical approximator. New approach based on the Proper Orthogonal Decomposition modes
Enrique AJ |
| 1226 - 1236 |
Optimizing the design of complex energy conversion systems by Branch and Cut
Ahadi-Oskui T, Vigerske S, Nowak I, Tsatsaronis G |
| 1237 - 1245 |
Improving benders decomposition using maximum feasible subsystem (MFS) cut generation strategy
Saharidis GKD, Ierapetritou MG |
| 1246 - 1255 |
A simple heuristic for reducing the number of scenarios in two-stage stochastic programming
Karuppiah R, Martin M, Grossmann IE |
| 1256 - 1267 |
A chance constrained approach for a gas processing plant with uncertain feed conditions
Mesfin G, Shuhaimi M |
| 1268 - 1281 |
Nonlinear model-based control of highly nonlinear processes
Gregorcic G, Lightbody G |
| 1282 - 1295 |
Plantwide control system design of the benchmark vinyl acetate monomer production plant
Seki H, Ogawa M, Itoh T, Ootakara S, Murata H, Hashimoto Y, Kano M |
| 1296 - 1305 |
Analysis and control of a partially heat integrated refinery debutanizer
Jana AK, Mali SV |
| 1306 - 1311 |
A novel multi-dimensional visualization technique for understanding the design parameters of drug formulations
Yamashita F, Itoh T, Yoshida S, Haidar MK, Hashida M |
| 1312 - 1319 |
Aggregate models based on improved group methods for simulation and optimization of distillation systems
Kamath RS, Grossmann IE, Biegler LT |
