Index of /skoge/publications/thesis/2004_skouras/matlab-distillation/3-component

[ICO]NameLast modifiedSizeDescription

[PARENTDIR]Parent Directory  -  
[   ]NRTL.m2010-07-15 10:08 6.8K 
[TXT]README.html2010-07-15 10:08 922  
[TXT]README.txt2010-07-15 10:08 913  
[   ]Rectifier.m2010-07-15 10:08 5.6K 
[   ]UNIQUAC.m2010-07-15 10:08 6.2K 
[   ]Wilson.m2010-07-15 10:08 4.8K 
[   ]input_rectifier.m2010-07-15 10:08 1.3K 
[   ]run_rectifier.m2010-07-15 10:08 1.5K 


Delivered-To: skoge@smtp.nt.ntnu.no 
Delivered-To: kikp-alias/to-skoge@chemeng.ntnu.no 
X-Sender: skouras@imap.nt.ntnu.no 
X-Mailer: QUALCOMM Windows Eudora Version 5.2.1 
Date: Mon, 10 Jan 2005 13:34:52 +0100 
To: skoge@chemeng.ntnu.no 
From: Stathis Skouras  
Subject: Matlab files 


Sigurd,


Here are the Matlab files you asked for. I put them in order and I wrote some more detailed comments so it would be easier to use them.


The column simulated is a batch rectifier and the system is a 3-component one (methanol/ethanol/1-propanol) but it can easily be changed to a continuous column.


Three VLE models can be used (Wilson, UNIQUAC or NRTL). Wilson and NRTL work fine for 2-components (the third is set to zero). However, UNIQUAC does not accept a zero (0) value but a very small value (e.g 0.000001)  for the third component works fine.


Stathis