A comprehensive mathematical model is developed to simulate gas-liquid reac
tor in which both, reactants as well as products enter or leave the reactor
in gas phase while the reactions take place in liquid phase. A case of fir
st-order reaction (isothermal) was investigated in detail using the dynamic
model and numerical bifurcation tools. Strong coupling between reaction ki
netics and product removal rate was found to lead to complex dynamic (inclu
ding over-flow/dry-up or oscillatory) behaviour. Key parameters controlling
operability and dynamic characteristics were identified. Operability maps
of the reactor/separator are presented. The model and results discussed wil
l be useful for design and operation of industrial reactor/separators. (C)
1999 Elsevier Science Ltd. All rights reserved.