The physical absorption of CO2 and propene into toluene/water emulsion
s is studied in a stirred cell and laminar film absorber. Experimental
ly observed mass-transfer rates are compared to an absorption model, b
ased on Higbie's penetration theory describing physical gas absorption
into an emulsion. For all absorption experiments in a stirred cell ab
sorber (toluene fractions and stirring rates), experimentally observed
mass-transfer rates are considerably higher than the rates predicted
by the absorption model. Moreover, the absorption rate decreases with
increasing stirring rate, whereas no influence of the stirring rate is
predicted by the absorption model. In contradiction to the absorption
experiments in a stirred cell absorber, the observed mass-transfer ra
tes in the laminar film absorber agree with the model simulations. Pro
bable existence of a very thin toluene layer is observed on top of the
emulsion for the stirred cell experiments, likely due to minor phase
separation. Since in the laminar film absorber gas-liquid interface an
d the gravity force are parallel, this phenomenon does not probably oc
cur significantly for absorption experiments in this absorber. The obs
erved mass-transfer phenomena can be explained, at least qualitatively
, from the occurrence of a thin toluene layer.