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BSTILL - Binary Batch Distillation Column

This distillation equipment is as described in Sec. 3.3.3.2. For convenience a column containing seven theoretical plates and reboiler is assumed, together with constant volume conditions in the reflux drum. The example is based on that of Luyben (1973, 1990). [Pg.584]

The component balance for the more volatile component on any plate n yields dX, [Pg.585]

It may be noted that the liquid holdup on the plates is set rather large. This is necessary to avoid very slow rates of computation. [Pg.585]

CONSTANT HOLDUP BINARY BATCH DISTILLATION COLUMN EQUILIBRIUM PLATE BEHAVIOUR [Pg.586]

CONSTANT MOLAR OVERFLOW AND CONSTANT PLATE HOLDUP CONSTANT HOLDUP IN REBOILER AND SURGE DRUM [Pg.586]

The component balance for plate n, based on the more volatile component, is [Pg.545]

5 Simulation Tools and Examples of Chemical Engineering Processes [Pg.546]

For the reflux drum and condenser, assuming constant holdup [Pg.546]

Startup is at initially total reflux, with the reflux value set at an arbitrarily high value, R = Rinit. Once the distillate composition, XO, exceeds the set point composition, XOset, control of reflux ratio is effected by varying the reflux ratio according to the proportional control relationship RC=KC (X0set-X0). The change from initial startup to controlled withdrawal of distillate is effected by means of the logical control variable Flag . [Pg.546]


See other pages where BSTILL - Binary Batch Distillation Column is mentioned: [Pg.584]    [Pg.490]    [Pg.632]    [Pg.545]    [Pg.584]    [Pg.490]    [Pg.632]    [Pg.545]   


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