This paper studies the effect of tray geometry (especially hole diameter) and liquid tray
composition on tray efficiency in a bench-scale distillation column. The results of this study are
used for scaling up tray efficiency. Two binary systems, ethanol/water and cyclohexane/n-heptane,
were considered. The operating conditions were atmospheric pressure and total reflux. For each
one, two different hole diameters (small and large) were also tested. Kirschbaum's industrial
data (1962) for the ethanol/water system and of Yanagi and Sakata's (1982) for the cyclohexane/n-heptane system were considered as reference values. The results show the importance of
reproducing the hole diameter and liquid tray composition in small trays for using laboratory
data to predict large tray efficiency.