Process Dynamics and Tuning — MCQs – EE 35 Score: 0 Attempted: 0/35 1. The term process dynamics refers to: (A) Static behavior of a system (B) Time-dependent behavior of a process (C) Steady-state operation only (D) Electrical characteristics of the process 2. The time constant of a process is a measure of: (A) Process gain (B) Speed of response (C) Steady-state error (D) Overshoot 3. A first-order process has: (A) One energy storage element (B) Two poles (C) A nonlinear response (D) A dead-time behavior 4. The dead time or time delay in a process represents: (A) Instantaneous response (B) Time taken before the output starts to respond (C) The time constant (D) System gain 5. The process gain represents: (A) The change in output per unit change in input (B) The delay in response (C) The system damping ratio (D) The feedback sensitivity 6. The steady-state gain of a process is: (A) The ratio of steady-state output change to steady-state input change (B) The instantaneous rate of change (C) Always zero (D) Dependent only on time delay 7. A first-order plus dead-time (FOPDT) model is commonly used to: (A) Represent dynamic behavior of industrial processes (B) Eliminate process lag (C) Calculate steady-state gain only (D) Model noise 8. Process lag is caused by: (A) Energy storage in the system (B) High-frequency noise (C) Poor control tuning (D) Signal distortion 9. Process tuning is the adjustment of: (A) Controller parameters to achieve desired performance (B) Mechanical alignment of instruments (C) Valve body size (D) Signal scaling 10. The Ziegler–Nichols method is widely used for: (A) Controller tuning (B) Measuring process variables (C) Linearization (D) Frequency analysis 11. In open-loop tuning, the process is: (A) Tested without feedback control (B) Controlled by feedback (C) Operating under closed-loop feedback (D) Disconnected from sensors 12. In closed-loop tuning, the process is: (A) Tested under feedback control (B) Disconnected from controller (C) Isolated from disturbances (D) Linearized manually 13. The ultimate gain (Ku) is defined as: (A) The gain at which the system output oscillates continuously (B) The gain that minimizes error (C) The smallest possible gain (D) The steady-state gain 14. The ultimate period (Pu) is: (A) The period of sustained oscillations at ultimate gain (B) The time constant of the process (C) The dead time of the process (D) The response delay 15. The Ziegler–Nichols tuning provides: (A) Empirical settings for P, I, and D controllers (B) Exact theoretical values for control parameters (C) Instantaneous tuning (D) Dead-time compensation 16. Increasing the proportional gain (Kp) generally: (A) Reduces steady-state error but increases oscillations (B) Increases steady-state error (C) Decreases overshoot (D) Reduces system speed 17. Increasing the integral gain (Ki) tends to: (A) Eliminate steady-state error (B) Increase steady-state error (C) Slow the system response (D) Reduce oscillations 18. Increasing the derivative gain (Kd): (A) Improves damping and reduces overshoot (B) Slows response (C) Increases steady-state error (D) Causes instability 19. Fine-tuning of a controller involves: (A) Adjusting small changes to improve system response (B) Redesigning the process (C) Changing sensor location (D) Modifying actuator type 20. Quarter-amplitude damping refers to: (A) Successive oscillations reducing to one-fourth amplitude (B) Sustained oscillations (C) Critically damped response (D) Instability 21. Overdamped response means: (A) Slow return to steady state without oscillations (B) Fast response with overshoot (C) Continuous oscillations (D) No response 22. Underdamped response means: (A) Response oscillates before settling (B) Very slow response (C) No overshoot (D) Constant error 23. A critically damped response achieves: (A) Fastest response without overshoot (B) Maximum overshoot (C) Continuous oscillation (D) No damping 24. The setpoint in a control system is: (A) The desired value of the process variable (B) The measured output (C) The disturbance input (D) The feedback signal 25. The process variable (PV) represents: (A) The measured output of the process (B) The desired setpoint (C) The manipulated variable (D) The disturbance 26. The manipulated variable (MV) is: (A) The input adjusted by the controller (B) The process disturbance (C) The sensor signal (D) The error signal 27. The error signal in a control system is the: (A) Difference between setpoint and process variable (B) Output of the actuator (C) Process gain (D) Feedback signal 28. The time constant of a slow process is generally: (A) Large (B) Small (C) Zero (D) Negative 29. Dead-time compensation is achieved using: (A) Smith Predictor (B) Ziegler–Nichols tuning (C) PI controller (D) Feedforward control only 30. A self-regulating process is one that: (A) Returns to steady-state without external control (B) Needs manual reset (C) Always oscillates (D) Is unstable 31. A non-self-regulating process is one that: (A) Does not reach steady-state without control (B) Automatically stabilizes (C) Has zero gain (D) Is purely static 32. The process reaction curve method is used to determine: (A) Process gain, time constant, and dead time (B) Controller output (C) Setpoint value (D) Steady-state error 33. Tuning constants are adjusted to achieve: (A) Desired transient and steady-state performance (B) Minimum process gain (C) Constant frequency (D) Linear signal behavior 34. Aggressive tuning generally results in: (A) Faster response but higher overshoot (B) Slower response and more stability (C) Reduced gain (D) No oscillations 35. Conservative tuning results in: (A) Slower but more stable response (B) Faster and less stable response (C) No steady-state (D) High-frequency oscillations Related Posts:Performance Tuning and Monitoring MCQsTeam Dynamics and Team Building MCQsEcological succession and community dynamics MCQsKinematics and Dynamics of Robots — MCQs – EEResearch Topics Non linear vibration dynamics and machine designResearch Topics of flutter and computational fluid dynamics