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Question 1: In the context of a control system design for a chemical plant, how should you approach system modeling and simulation?

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Question 2: What is the key consideration when designing a control system for a batch process versus a continuous process in a chemical plant?

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Question 3: When using a PID controller in a distillation column, which control strategy should be used to minimize temperature oscillations?

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Question 4: How does automation reduce the occurrence of process variability in a chemical plant?

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Question 5: How can you optimize the communication infrastructure in a SCADA system used in a chemical facility?

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Question 6: In the context of a PID controller, what does the derivative (D) action primarily affect in a process like temperature control?

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