Mechanisms for the flow of liquid over outlet weirs of distillation and abs
orption trays are described in this paper. Weir flow contributes to the liq
uid height on a tray, and this height is important for the design and opera
tion of trayed columns. Comparisons of available experimental data with Fra
ncis' weir equation and with new stochastic liquid flow models showed that
the traditionally used Francis' equation needs modification. The stochastic
flow models Link the weir flow to the flow mechanisms upstream of the tray
outlet. These upstream mechanisms provide the input needed for a new weir
crest equation. The existence of a so-called 'edge-vortex' (a horizontal ro
ll cell at the boundary of the gassed and the ungassed region) is shown to
play an important role, when a calming zone is present upstream of the outl
et weir. (C) 1999 Elsevier Science S.A. All rights reserved.