Abstract
Numerical and experimental analyses were performed for a modified air gap distillation membrane that combines the low conductive heat loss of an air gap membrane for distillation with the reduced mass transfer resistance of a direct contact membrane. Instead of a stagnant film of air separating the membrane and the condensing surface, the air is moved by temperature differences between the top and the bottom of the cavity. The air movement within the enclosure modifies the hydrodynamic conditions and the temperature and the mass transfer mechanisms in the air gap. The result shows a slight enhancement of permeate flux. An experimental laboratory apparatus was built, and different operating parameters were investigated such as feed flow rate, temperature difference and air gap width. The results are in good agreement with those found in the numerical study.