O'Reilly logo

Process Control: Modeling, Design, and Simulation by B. Wayne Bequette

Stay ahead with the world's most comprehensive technology and business learning platform.

With Safari, you learn the way you learn best. Get unlimited access to videos, live online training, learning paths, books, tutorials, and more.

Start Free Trial

No credit card required

Additional Exercises

1:Consider the case 2 operating point, Fs/V = 2.8744 min-1. Show that the steady-state concentrations are CAs = 6.0870 mol/liter and CBs = 1.117 mol/liter.
  1. Find the resulting state space model and verify that the manipulated input-output process transfer function for this operating point is

  2. Find the gain-time constant form for this transfer function.

  3. Show that a P controller (with the correct sign on the controller gain) cannot destabilize this process unless there are additional measurement and valve lags. Use the Routh stability criterion.

2:Consider the following parameters given by Klatt and Engell (1998) for a reactor operating ...

With Safari, you learn the way you learn best. Get unlimited access to videos, live online training, learning paths, books, interactive tutorials, and more.

Start Free Trial

No credit card required