[1]Huang H P, Chen C C. Controlsystem synthesis for openloop unstable process with time delay[J]. Control Theory and Applications, IEE Proceedings, 1997, 144(4): 334346. [2]Huv Ngoc Vu, Hai Trung Do, Minh Xuan Tran, et al. Robust tracking for the openloop unstable process with time delay by combining PID typep and inner compensators[C]∥Control Engineering and Communication Technology. Liaoning, China, 2012:1316. [3]尹成强,岳继光. 化工不稳定时滞对象的改进内模控制[J].测控技术,2009,28(6):4750. YIN Chengqiang, YUE Jiguang. Modified internal model control for chemical unstable processes with time delay[J].Mesurement & Control Technology,2009,28(6):4759. [4]Xiang C, Nguyen L A. Controller of unstable processes with dead time by PID controllers [J]. Control and Automation, 2005,27(2):703708. [5]欧林林,张卫东,顾诞英.一类时滞对象的PID控制器参数稳定域计算[J]. 控制与决策,2009,21(9):10201023. OU Linlin, ZHANG Weidong, GU Danying. Calculation of stability region of PID controllers for a class of processes with time delay[J].Control and Decision,2009,21(9):10201023. [6]Guillermo J Silva. New results on the synthesis of PID controllers[J]. IEEE Transactions on Automatic Control, 2002, 47(2): 241252. [7]Guillermo J Silva. PID controllers for timedelay systems[M]. USA:Springer, 2005: 179263. [8]Tan Wen, Liu Jizhen, Chen Tongwen, et al. Comparison of some wellknown PID tuning formulas[J]. Computers and Chemical Engineering, 2006, 30(9):14161423. [9]Simon Haykin. Neural networks and learning machines[M].McMaster University, Canada:Prentice Hall, 2009. [10]边丽华. PID控制器参数自整定方法的研究与实现[D]. 大连:大连理工大学,2009. |