| 389 - 398 |
Robust estimation of free-radical homopolymer reactors
Alvarez J, Lopez T, Hernandez E |
| 399 - 410 |
A feedback-based implementation scheme for batch process optimization
Visser E, Srinivasan B, Palanki S, Bonvin D |
| 411 - 418 |
Post analysis on different operating time processes using orthonormal function approximation and multiway principal component analysis
Chen JH, Liu JL |
| 419 - 432 |
Control of particle size distribution described by a population balance model of semibatch emulsion polymerization
Crowley TJ, Meadows ES, Kostoulas E, Doyle FJ |
| 433 - 440 |
Application of an iterative identification for control scheme to a neutralization process
Ochs S, Engell S |
| 441 - 448 |
Optimal operation of a continuous DTB crystallizer
Hasebe S, Hamamura T, Naito K, Sotowa KI, Kano M, Hashimoto I, Betsuyaku H, Takeda H |
| 449 - 458 |
A hybrid model predictive control strategy for nonlinear plant-wide control
Zhu GY, Henson MA, Ogunnaike BA |
| 459 - 469 |
Sensor and actuator fault isolation by structured partial PCA with nonlinear extensions
Huang Y, Gertler J, McAvoy TJ |
| 471 - 486 |
Recursive PCA for adaptive process monitoring
Li WH, Yue HH, Valle-Cervantes S, Qin SJ |
| 487 - 507 |
Plantwide control: the search for the self-optimizing control structure
Skogestad S |
