Question 1: What is the primary disadvantage of a poorly tuned PID controller in a dynamic chemical process?
Which action should you take?
Question 2: In a chemical plant, how do you ensure that control loops for highly dynamic systems, like pumps and compressors, are optimized for stability and response time?
Which action should you take?
Question 3: How would you tune a PID controller for a chemical reactor system with significant time delays?
Which action should you take?
Question 4: How does a SCADA system handle real-time process control in a chemical plant?
Which action should you take?
Question 5: How do you ensure effective communication between process automation systems and operators in a chemical plant?
Which action should you take?
Question 6: What would be the effect of setting the integral (I) term too high in a PID controller in a chemical process?
Which action should you take?