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Question 1: What impact does increasing the integral time (I) have on the control performance of a PID controller?

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Question 2: What is the most effective method for compensating for process dead time in a PID-controlled system?

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Question 3: When developing a control algorithm for a distillation column, how do you minimize disturbances from feed composition variations?

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Question 4: How do you address noise amplification when using derivative action in a PID controller for a chemical pump system?

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Question 5: How does an Automatic Control System (ACS) help optimize energy consumption in a petrochemical plant?

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Question 6: What is the advantage of using a distributed control system (DCS) alongside SCADA in a chemical plant?

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