This paper describes an implicit 1-D two-fluid hydrodynamic trickle-bed mod
el designed to approximate the actual two-phase flow and bed void using fou
r inclined slits consisting of a dr, a gas-(static)liquid, a (dynamic)liqui
d-(static)liquid and a gas-(dynamic)liquid slits. Based on the Holub et al.
(1) mono-slit phenomenological approach, the model can be used to predict t
he frictional two-phase pressure drop, the external, dynamic and static liq
uid hold-ups, the pellet-scale external, dynamic and static wetting efficie
ncy in trickle-bed reactors operated under trickle flow regime and partiall
y wetted pellet conditions. in this context, a collection of data relative
to the wetting efficiency, liquid hold-up and pressure drop measured under
high pressure/high temperature has been compiled from the Literature concer
ning the trickle flow regime in undiluted and diluted beds of catalysts and
fines. This useful data provided sufficient and pertinent information to p
ractically implement and successfully validate the model.