Mh. Aldahhan et Mp. Dudukovic, CATALYST WETTING EFFICIENCY IN TRICKLE-BED REACTORS AT HIGH-PRESSURE, Chemical Engineering Science, 50(15), 1995, pp. 2377-2389
Trickle-bed reactors are widely used in industrial high pressure opera
tions (up to 30 MPa). The knowledge of catalyst wetting efficiency as
a function of operating conditions is needed for relating laboratory a
nd pilot scale reactor data to large scale reactor operation. The avai
lable predictions of the wetting efficiency rest on data collected at
atmospheric pressure. In this study a phenomenological analysis has be
en developed to relate the wetting efficiency with operating condition
s such as reactor pressure, gas and liquid how rate. Experimental data
for the wetting efficiency at high pressure have been obtained via a
tracer technique. The data support the developed model which can be ex
pressed by the following correlation: eta(CE) = 1.104 Re-L(1/3) [1+[(D
elta P/Z)/rho(L)g]/Ga-L](1/9). This correlation is also in good agreem
ent with the data correlated previously at atmospheric pressure and pr
ovides the means for assessing liquid-catalyst contacting at all opera
ting pressures.