## Abstract This paper presents a nonlinear modelβbased controller based on the ideas of parametric predictive control applied to a continuous stirred tank reactor (CSTR) process unit. Controller design aims at avoiding the complexity of implementation and long computational times associated with c
Design of observer based nonlinear model predictive controller for a continuous stirred tank reactor
β Scribed by J. Prakash; R. Senthil
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 218 KB
- Volume
- 18
- Category
- Article
- ISSN
- 0959-1524
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Globally linearixi ng control, a differential geometry-based technique (continuous), and nonlinear predictive conuol, an optimization-based approach (discrete), are compared for temperature control of a classical exothermic CSTR The two strategies can be tuned to have identical performance for setpo
A mathematical model is developed for solution copolymerization in a continuous stirred tank reactor. For the thermal copolymerization of styrene and acrylonitrile (SAN), the kinetic rate expression for thermal initiation is derived by applying the pseudo-steady-state hypothesis to the intermediates