| Mathematical Modeling and Model Based Control of a Pulp Mill Powerhouse |
Model Predictive Control of Weight-on-Bit near Its Optimum in Hydrocarbon Well Drilling: the Value of Constraints
Ankur Awasthi, Chemical Engineering, University of Houston, S222 Engineering Bldg. 1, Houston, TX 77204 and M. Nikolaou, Chemical Engineering, University of Houston, Houston, TX 77204-4004 |
Evaluation of Criteria for Selecting Temperature Control Trays in Distillation Columns
William L. Luyben, Lehigh University, Department of Chemical Engineering, Bethlehem, PA 18015 |
Application of a Lyapunov-Based Nonlinear Controller to a Reactor with Highly Exothermic Reactions
Dário A. F. Luís1, A. Astolfi2 and L. Kershenbaum1, (1)CPSE, Imperial College, Prince Consort Road, London, SW7 2AZ, United Kingdom, (2)Department of Electrical and Electronic Engineering, Imperial College, London, Exhibition Road, SW7 2BT, London, United Kingdom |
Control Loop Pairing Using Dynamic Performance
Tom E. Marlin, McMaster University, 1280 Main Street West, Hamilton, ON L8N4L7, Canada and Yongsong Cai, Chemical Engineering, McMaster University, 1280 Main Street West, Hamilton, ON L8N4L7, Canada |
An Advanced Model for Optimal Operation of Emulsion Terpolymerization Processes: Application to Styrene/Mma/Ma
M. H. Srour1, V. G. Gomes1 and J.A. Romagnoli2, (1)Chemical Engineering, Sydney University, CNR shepherd and Lander St., Sydney, Australia, (2)Chemical Engineering, Sydney University, CNR shepherd and Lander St., Australia |
Evaluation of a Two-Temperature Control Structure for a Two-Reactant/Two-Product Type of Reactive Distillation Column
Devrim B. Kaymak, Department of Chemical Engineering, Istanbul Technical University, Istanbul, Turkey and William L. Luyben, Lehigh University, Department of Chemical Engineering, Bethlehem, PA 18015 |