Real Time Optimization (RTO) with Model Predictive Control (MPC)

被引:0
作者
De Souza, Glauce [1 ]
Odloak, Darci [1 ]
Zanin, Antonio C. [2 ]
机构
[1] Univ Auckland, Dept Chem & Mat Engn, 20 Symonds St,8th Floor,City Campus 1042, BR-05508900 Auckland, New Zealand
[2] Petrobras SA, BR-20035900 Rio De Janeiro, Brazil
来源
10TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING | 2009年 / 27卷
关键词
Real Time Optimization; Model Predictive Control; Fluid Catalytic Converter; Non-linear programming; PLANT;
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper studies a simplified methodology to integrate the real time optimization of a continuous system into the model predictive controller in the one layer strategy. The gradient of the economic objective function is included in the cost function of the controller. One of the control objectives is to zero the reduced gradient of the economic objective while maintaining the system outputs inside their zones. Optimal conditions of the process at steady state are searched through the use of a rigorous nonlinear process model, while the trajectory to be followed is predicted with the use of a linear dynamic model that can be obtained through a plant step test. Moreover, the reduced gradient of the economic objective is computed taking advantage of the predicted input and output trajectories. The main advantage of the proposed strategy is that the resulting control/optimization problem can be solved with a quadratic programming routine at each sampling step. Simulation results show that the approach proposed here is comparable to the strategy that solves the full economic optimization problem inside the MPC controller where the resulting control problem becomes a nonlinear programming with a high computer load.
引用
收藏
页码:1365 / 1370
页数:6
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