also, one other question is, if i mask a subsystem that includes a PID
controller? how do i get the masked block parameters to be connected
to the parameters of the PID? (ie in the masked block have
P,I,D,Tsp,etc...show up and linked properly?)
thanx!:)
A good starting point might be the Matlab/Simulink files created by Sigurd
Skogestad and posted on his site. He also has there several papers on
dynamics and control of distillation columns that use those files -- very
useful info. They're simple binary columns with ideal VLE, but they
demonstrate the concepts. Sigurd's one of the best this profession has, in
my opinion (which ain't worth much, I admit).
Here's a link: http://www.chembio.ntu.no/~skoge/distillation/
Good luck,
Rob
In this type of modelling you have two choices about the thermodynamic
and transport properties:
o Write your own calculations, based on equation-of-state & other
models.
o Link to a thermodynamics and physical properties package (as does
Hysys, Aspenplus, gPROMS, etc.)
If you decide to go down the second route, you may want to check out our
own Multiflash for MATLAB product, which provides MATLAB/Simulink access
to Infochem's popular independent Multiflash product. This essentially
provides MATLAB/Simulink with similar thermophysprops capabilities as
the mainstream ChemEng simulation packages.
See <http://www.khace.com/products/multiflash>.
Kelvin B. Hales
Kelvin Hales Associates Limited
Consulting Process Control Engineers
E-mail: kha...@khace.com
Web: www.khace.com