Kaya, I2024-08-042024-08-0420030019-05781879-2022https://doi.org/10.1016/S0019-0578(07)60117-7https://hdl.handle.net/11616/93482Good control of processes. With long dead time is often achieved using a Smith predictor configuration. Typically a PI or PID controller is used; however, it is shown in this paper that for some situations improved set point and disturbance responses can be obtained if a PI-PD controller is Used. Several methods are possible for selecting the parameters of the PI-PD controller but when the plant transfer function has no zeros, the use of the standard forms provides a simple algebraic approach, and also reveals why difficulties may be encountered if a PID controller is used. Some examples are given to show the value of the approach presented. (C) 2003 ISA-The Instrumentation, Systems, and Automation. Society.eninfo:eu-repo/semantics/closedAccesspredictive controlintegral performance indicesdelay compensationPID controllersdisturbance rejectionArticle4211011101254647210.1016/S0019-0578(07)60117-72-s2.0-0037267259Q1WOS:000180391200010Q3