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Phone: 337-475-5874
Fax: 337-475-5286
Box 91735
Lake Charles, LA 70609
engineering@mcneese.edu
http://mcneese.edu/ceet/eng
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Chemical Engineering - CHEG 670
Process Control Systems
- Perform material and energy balances on unsteady state systems to form dynamic models.
- Model fluid flow systems.
- Model heat transfer systems.
- Linearize process models to form linear systems of differential equations.
- Apply Laplace transforms to solve linear differential equations.
- Apply Laplace transforms to linear process models and reduce to block diagrams including transfer functions in the Laplace (s) domain.
- Apply the final value theorem to determine the steady state outcome of inputs to process models.
- Use block diagram algebra to extract various transfer functions from process models.
- Simulate process models using SIMULINK.
- Develop blocks for process sensors and transmitters.
- Develop blocks for final control elements.
- Develop blocks for PID controllers.
- Develop block diagrams for single feedback control loops.
- Develop open and closed loop transfer functions for feedback loops.
- Find the ultimate gain and period for a control loop.
- Use the ultimate gain and period to find tuning parameters for PID controllers.
- Characterize a process as a first order plus dead time (FOPDT) process using step test data.
- Tune a control loop using FOPDT parameters.
- Configure and tune cascade loops, and draw their P&I diagrams and block diagrams.
- Design feed forward loops, and draw their P&I diagrams and block diagrams.
- Determine appropriate controlled/manipulated variable pairings using Bristol’s relative gain array.
- Design static and dynamic de-couplers for multivariate loops.
- Using the simulations created above (9), extend the simulation to include controls.
- Test the simulated control systems developed above and report on the effectiveness of the various control schemes.
Prepared by Dr. D. John Griffith
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