Page 310 - Separation process engineering
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Figure 8-8. Distillation curves at total reflux for acetone, chloroform, benzene mixtures at 1.0 atm
(Biegler et al., 1997), reprinted with permission of Prentice-Hall PTR, copyright 1997, Prentice-
Hall.
Calculation of the bubble-point at every stage can be laborious; fortunately, the calculation is easily done
with a process simulator. Next, at total reflux the operating equation is,
