How to Effectively Mitigate System Shock Caused by Setpoint Changes
1. Introduction In process control, the Proportional–Integral–Derivative (PID) controller is one of the most widely used strategies.However, when the setpoint (SP) undergoes a sudden step change, the standard PID often causes controller output overshoot, valve oscillations, and mechanical stress.To address this issue, an improved structure known as Proportional–Derivative First (PD–PI) Control has been developed. This […]
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