부산대학교 도서관

In a chemical plant involving a series of processing units, it is beneficial to have a model that can accurately forecast the behavior of downstream variables based on upstream measurements. Such a model can be useful in feedforward and inferential control of the downstream variables to compensate for various upstream disturbances. However, creating such a dynamic model can be very difficult. The conventional multi variable identification approach based on minimizing single-step-ahead prediction error, can result in models leading to poor prediction and control in the described context. To alleviate this difficulty, we propose a modification to the conventional subspace identification method geared towards accurate k-step-ahead prediction. where k is a number chosen according to the estimated dead time. It is shown that the modified subspace identification method can be used in conjunction with the k-step prediction error minimization (PEM). Using an illustrative examples involving six mixing units with a recycle loop. we demonstrate the improvement that is possible from adopting the suggested modification.