A multi-tube air-lift loop reactor (MT-ALR) is presented in this paper. Bas
ed on the energy conservation, a mathematical model describing the liquid c
irculation flow rate was developed, which was determined by gas velocity, t
he cross areas of riser and downcomer, gas hold-up and the local frictional
loss coefficient. The experimental data indicate that either increase of g
as flow rate or reduction of the downcomer diameter contributes to higher l
iquid circulation rate. The correlation between total and the local frictio
nal loss coefficients was also established. Effects of gas flowrate in two
risers and diameter of downcomer on the liquid circulation rate were examin
ed. The value of total frictional loss coefficient was measured as a functi
on of the cross area of downcomer and independent of the gas flow rate. The
calculated results of liquid circulation rates agreed well with the experi
mental data with an average relative error of 9.6%.