| 773 - 784 |
Effective transfer function method for decentralized control system design of multi-input multi-output processes
Xiong Q, Cai WH |
| 785 - 794 |
Performance assessment of single-loop industrial controllers
Hugo AJ |
| 795 - 808 |
Nonlinear model predictive control for the ALSTOM gasifier
Al Seyab RK, Cao Y |
| 809 - 818 |
Analytical method of PID controller design for parallel cascade control
Lee Y, Skliar M, Lee M |
| 819 - 829 |
Online monitoring of steel casting processes using multivariate statistical technologies: From continuous to transitional operations
Zhang Y, Dudzic MS |
| 831 - 843 |
A noncausal approach for PID control
Piazzi A, Visioli A |
| 845 - 854 |
Linear controller design and performance limits of binary distillation column subject to disturbances with bounds on magnitudes and rates of change
Khaisongkram W, Banjerdpongchai D |
| 855 - 864 |
A practical robust control scheme for yeast fed-batch cultures - An experimental validation
Renard F, Vande Wouwer A, Valentinotti S, Dumur D |
| 865 - 875 |
Globally stabilizing control of fed-batch processes with Haldane kinetics using growth rate estimation feedback
De Battista H, Pico J, Pico-Marco E |
| 877 - 886 |
State-dependent parameter modelling and identification of stochastic non-linear sampled-data systems
Akesson BM, Toivonen HT |
