It is a non standard implementation of the
Fenske-Underwood-Gilliland shortcut method for multicomponent
distillation.
The following simplifications are made:
- The distribution of components between the distillate and
bottom, obtained by the Fenske equation for total reflux, is
considered valid for the actual and minimum reflux.
- It is considered just one pinch point, close to the feed
composition. As the distillate composition is taken from the
Fenske's equation, only one Underwood set of equations is needed in
order to calculate the minimum reflux. This may give poor
calculation if there is an important distribution of any component
between distillate and bottom.
The feed must be specified as flow, in kmol/h or kg/h. The top
light, and the bottom heavy, can be specified as flow or
concentration. Flow is recommended for best convergence.
The model is lacking one equation. You can configure the
needed equation by selecting the required parameter. It is done at
the graphical menu under the "Operating conditions" tab. You can
select one of the options as true: fix the reflux to a constant
value, or as a multiplier of the minimum reflux. Or fix the heat
exchange at the condenser or the reboiler. Or you can add the extra
equation (for example the value of the vpor flow at the stripping
section) by hand.
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