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Hello, <br>
<br>
First, you will need physical property models that will provide you
with fugacity (or fugacity coefficient, or log fugacity
coefficient). See here:<br>
<br>
<a class="moz-txt-link-freetext" href="http://www.amsterchem.com/scilabthermo.html">http://www.amsterchem.com/scilabthermo.html</a><br>
<a class="moz-txt-link-freetext" href="http://www.amsterchem.com/scilabunitop.html">http://www.amsterchem.com/scilabunitop.html</a><br>
<br>
(Both only for Window). <br>
<br>
If you are planning on writing phase-equilibrium based distillation
models, that should suffice. For rate-limited based models, you will
need to come up with mass transfer coefficient models, diffusion
coefficient models, etc. But as Christophe says, you will have to
decide on what exactly you want to model. <br>
<br>
Hope that helps, best wishes, <br>
<br>
Jasper, AmsterCHEM<br>
<br>
<div class="moz-cite-prefix">On 7/31/2013 18:06, Dang, Christophe
wrote:<br>
</div>
<blockquote
cite="mid:3B5FFC67498DFF49AE7271A584867D16F31E9C1A2A@301EX00100.sidel.com"
type="cite">
<pre wrap="">Hello,
</pre>
<blockquote type="cite">
<pre wrap="">De la part de Eze-Okoli Ifeoma Sandra
Envoyé : mardi 30 juillet 2013 17:36
Good day, i would like to know how to design a multi-component flash
distillation system using scilab
</pre>
</blockquote>
<pre wrap="">
This seems to be a physical/chemical engineering problem.
Scilab performs calculations, but you decide which calculations.
So, first decide what you have to calculate and how,
and then we might be able to help you.
Best regards
</pre>
</blockquote>
<br>
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