693 - 701 |
Robust disturbance modeling for model predictive control with application to multivariable ill-conditioned processes Pannocchia G |
703 - 715 |
Scenario-integrated on-line optimisation of batch reactors Abel O, Marquardt W |
717 - 727 |
The integration of the output controllability index within the dynamic operability framework in process system design Ekawati E, Bahri PA |
729 - 737 |
On SISO and MIMO variable structure control of non linear distributed parameter systems: application to fixed bed reactors Boubaker O, Babary JP |
739 - 757 |
Projection based MIMO control performance monitoring: I-covariance monitoring in state space McNabb CA, Qin SJ |
759 - 768 |
Control of the ALSTOM gasifier benchmark problem using H-2 methodology Chin CS, Munro N |
769 - 786 |
A direct method for multi-loop PI/PID controller design Huang HP, Jeng JC, Chiang CH, Pan W |
787 - 800 |
A unified step response procedure for autotuning of PI controller and Smith predictor for stable processes Matausek MR, Kvascev GS |
801 - 818 |
State and parameter estimation in chemical and biochemical processes: a tutorial Dochain D |
819 - 830 |
Feedback linearization of discrete-time nonlinear uncertain plants via first-principles-based serial neuro-gray-box models Bazaei A, Majd VJ |
831 - 838 |
Control of the temperature distribution in two dimensional space of an annular type non-isothermal adsorber Yoshida M, Takeda T, Maruko M, Matsumoto S |