A simple yet effective and robust identification method is presented using process step responses for
process identification that can provide a continuous
transfer function with time-
delay without iteration. A
cascade relay provides accurate and reliable more points on the process
frequency response. The
internal model principle is employed to design single-loop controller of PID or high-order types with best achievable control performance for controller tuning, e.g. both single and multivariable cases are covered. The
process identification and control design portions can be easily integrated into a
control system auto-tuning
package. Further, a general control scheme for disturbance rejection is given which can significantly improve disturbance rejection performance over conventional feedback systems with
time delays. Practical issues such as noises, real-time implementation and tuning guidelines are also provided. The present invention provide general, systematic, effective, and applicable methods for
process identification and control for a wide range of industries such as process and chemical plants,
food processing, waste
water treatment and
environmental systems,
oil refinery,
servo and mechatronic systems, where a
system model is needed for analysis, prediction, filtering, optimization and management, and / or where control or better control is required for their systems.