Gas-lift reactors offer important advantages for a number of gas/liquid and
gas/liquid/solid reactions. However, the design and operation of these rea
ctors can be complex when there is a substantial change in the molar gas fl
ow rate along the length of the reactor, e.g., when a gaseous reactant is c
onverted into a liquid product. In this situation, there is a strong coupli
ng between reactor hydrodynamics and reaction kinetics, which arises from t
he fact char the rate of liquid circulation through the reactor and the lon
gitudinal profile of gas holdup in the riser are mutually dependent. Severa
l one-dimensional models have been developed to describe Kinetic/hydrodynam
ic coupling in gas-lift reactors. These models offer useful insights into t
he parameters that: affect reactor performance. The models can also be used
to explore different approaches to scale-up.