化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2001年
5期
468-470
,共3页
内模控制器鲁棒控制器 H2最优控制 H∞最优控制鲁棒稳定性鲁棒性能
內模控製器魯棒控製器 H2最優控製 H∞最優控製魯棒穩定性魯棒性能
내모공제기로봉공제기 H2최우공제 H∞최우공제로봉은정성로봉성능
In the design of IMC controller or other robust controller for robust performance in process control application, one of the necessary conditions is model (or process) uncertainty bound. The method of calculating model (or process) uncertainty bound for the first order lag process with dead time (FOPDT) in the robust controller design is reported in literatures. Up to the now, however, no any analytical method of calculating model (or process) uncertainty bound can be used in the second order lag process with dead time (SOPDT). Therefore, the design of the IMC controller for robust performance used to SOPDT also can not be simply achieved.By using first order Pade approximation for the dead time,an analytical method of calculating model (or process) uncertainty bound for SOPDT in the robust controller design is given for the first time.By using this bound, IMC controller design for robust performance can be made satisfactorily.