| 741 - 747 |
A practical loop pairing criterion for multivariable processes
Xiong Q, Cai WH, He MJ |
| 749 - 761 |
A noniterative neuro-fuzzy based identification method for Hammerstein processes
Jia L, Chiu MS, Ge SZS |
| 763 - 770 |
Multiscale fuzzy system identification
Nounou MN, Nounou HN |
| 771 - 784 |
Boundary control for an industrial under-actuated tubular chemical reactor
Del Vecchio D, Petit N |
| 785 - 797 |
Classifying organic crystals via in-process image analysis and the use of monitoring charts to follow polymorphic and morphological changes
De Anda JC, Wang XZ, Lai X, Roberts KJ |
| 799 - 805 |
Fault detection properties of global, local and time evolving models for batch process monitoring
Ramaker HJ, van Sprang ENM, Westerhuis JA, Smilde AK |
| 807 - 817 |
Design of robust gain-scheduled PI controllers for nonlinear processes
Gao JY, Budman HM |
| 819 - 835 |
From data to diagnosis and control using generalized orthonormal basis filters. Part I: Development of state observers
Patwardhan SC, Shah SL |
| 837 - 846 |
Robust MPC for systems with output feedback and input saturation
Rodrigues MA, Odloak D |
| 847 - 847 |
Comments on "On line estimation of product properties for crude distillation unit" by Tirtha Chatterjee and Deoki N. Saraf [Journal of Process Control 14 (2004) 61-77]
Friedman YZ |
| 849 - 849 |
Reply to "Comments on'On line estimation of product properties for crude distillation unit' by Tirtha Chatterjee and Deoki N. Saraf", by Y. Zak Friedman [Journal of Process Control 14 (2004) 61-77]
Saraf DN |
