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Question 1: How can you use a cascade control algorithm in a chemical process with multiple interacting loops?

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Question 2: What is the most effective method for ensuring fail-safe operation in a process automation system for critical petrochemical processes?

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Question 3: What is the impact of increasing the integral time in a PID controller for a chemical distillation column?

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Question 4: How does a PID controller handle changes in setpoint in a temperature control system for a reactor?

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Question 5: What is the most important consideration when tuning a PID controller for an exothermic reactor system?

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Question 6: What is the primary advantage of using a Model Predictive Control (MPC) algorithm in a chemical process?

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