The influence of a capillary module design and its operating parameters on
the efficiency of the membrane distillation (MD) process has been studied.
It was demonstrated that a uniform arrangement of the capillary membranes o
ver the cross-section of module at 0.33 membrane packing density ensured ap
propriate conditions of membranes cooling. This allowed to obtain a high va
lue of the driving force for the mass transfer, hence the MD process procee
ded with a high efficiency. The most favourable operating conditions of MD
module were obtained with membranes arranged in a form of braided capillari
es. The performance of membranes arranged parallel with their distribution
alongside module controlled by sieve baffles was also satisfactory.