967 - 968 |
ADCHEM 2009 Special Issue Engell S, Arkun Y |
969 - 982 |
The state of the art in chemical process control in Japan: Good practice and questionnaire survey Kano M, Ogawa M |
983 - 998 |
Plantwide Optimizing Control of a continuous bioethanol production process Ochoa S, Wozny G, Repke JU |
999 - 1008 |
Modeling and control system design of an industrial crystallizer train for para-xylene recovery Seki H, Amano S, Emoto G |
1009 - 1018 |
Applied advanced process analytics in biopharmaceutical manufacturing: Challenges and prospects in real-time monitoring and control Undey C, Ertunc S, Mistretta T, Looze B |
1019 - 1026 |
Parallel Dantzig-Wolfe decomposition for real-time optimization-Applied to a complex oil field Gunnerud V, Foss B, Torgnes E |
1027 - 1037 |
A dual modifier-adaptation approach for real-time optimization Marchetti A, Chachuat B, Bonvin D |
1038 - 1048 |
Approximate dynamic programming approach for process control Lee JH, Wong W |
1049 - 1058 |
Dealing with structural constraints in self-optimizing control engineering Heldt S |
1059 - 1075 |
Detection, isolation and handling of actuator faults in distributed model predictive control systems Chilin D, Liu JF, de la Pena DM, Christofides PD, Davis JF |
1076 - 1083 |
Guaranteed steady state bounds for uncertain (bio-)chemical processes using infeasibility certificates Hasenauer J, Rumschinski P, Waldherr S, Borchers S, Allgower F, Findeisen R |
1084 - 1091 |
Optimal decision-oriented Bayesian design of experiments Anand FS, Lee JH, Realff MJ |
1092 - 1102 |
A combined approach to nonlinear model predictive control of fast systems Tamimi J, Li P |