Abstract
Liquid-vapour equilibrium compositions and
pressures and relevant thermodynamic functions are given for the systems
benzene-n-heptane at 80 �C., n-hexane-chlorobenzene at (65 �C., and
cyclohexane-nitrobenzene at 80 �C. A comparison with values obtained previously
for the first of these systems is used to demonstrate the improved performance
of a new equilibrium still which is described. It is shown that consistent
results can be obtained with the new still for miscible systems having a
relative volatility in the range 1.0 to 14. Equilibrium data are also given for
the system n-hexane-chlorobenzene at 760 mm. Hg to permit comparison with the
performance of other equilibrium stills.
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