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| Content Provider | IEEE Xplore Digital Library |
|---|---|
| Author | Phuc Xuan Dang Banjerdpongchai, D. |
| Copyright Year | 2011 |
| Description | Author affiliation: Department of Electrical Engineering, Faculty of Engineering, Chulalongkorn University 254 Phayathai Road, Pathumwan, Bangkok 10330 Thailand (Phuc Xuan Dang; Banjerdpongchai, D.) |
| Abstract | This paper presents two integration approaches of real time optimization (RTO) and model predictive control (MPC) with the application to a distillation column. In particular, we present the modified RTO/MPC integration in the 2-layer structure and 3-layer structure. The 2-layer structure is constructed based on the conventional hierarchical control layer. In the 3-layer structure, the quadratic programming (QP) layer is inserted to compute the feasible set points for the MPC layer. Then, we apply the design methods to the distillation column. The simulation results illustrate the differences in the transient responses of two integration structures. The stability test shows that the 3-layer structure gives better results than that of the 2-layer structure in enforcing the stability of the system. |
| Starting Page | 988 |
| Ending Page | 993 |
| File Size | 367052 |
| Page Count | 6 |
| File Format | |
| ISBN | 9781612844879 |
| Language | English |
| Publisher | Institute of Electrical and Electronics Engineers, Inc. (IEEE) |
| Publisher Date | 2011-05-15 |
| Publisher Place | Taiwan |
| Access Restriction | Subscribed |
| Rights Holder | Asian Control Association |
| Subject Keyword | Distillation Column (DC) Distillation equipment Heating Quadratic Programming (QP) Model Predictive Control (MPC) Stability analysis Steady-state Real Time Optimization (RTO) Mathematical model Transient analysis Optimization |
| Content Type | Text |
| Resource Type | Article |
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