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Question 1: How do you incorporate safety instrumented systems (SIS) into control system design for a petrochemical facility?

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Question 2: What would be the effect of setting the integral (I) term too high in a PID controller in a chemical process?

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Question 3: In process automation, how can you handle emergency shutdowns in chemical plants?

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Question 4: How do you ensure real-time process automation in a chemical plant while maintaining system integrity?

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Question 5: When designing a control system for a distillation column, how do you account for the non-linearity of the process?

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Question 6: What is the primary role of a SCADA system in maintaining the operational safety of a petrochemical plant?

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