| نویسندگان | غلامحسین صدیفیان,فاطمه مسعودیه ارانی |
| همایش | The 15 th Iranian National Congress of Chemical Engineering (IChEC 2015) |
| تاریخ برگزاری همایش | 2015-2-17 |
| محل برگزاری همایش | تهران |
| نوع ارائه | سخنرانی |
| سطح همایش | ملی |
چکیده مقاله
Membrane distillation (MD), a thermally driven process involving hydrophobic micro-porous
membranes has acquired extensive attention of academic research and is arranged to become an
alternative solution to other membrane separation processes such as reverse osmosis (RO). Choice
of membrane for MD applications is a compromise between low thermal conductivity attained by
thicker membranes and high flux achieved by thin membrane, large pore size, and porosity and yet
very few research groups have examined the effects of these membrane parameters on direct
contact membrane distillation (DCMD) performance. In this work, six commercial membranes are
used to study simultaneously heat and mass transfer in DCMD by predicting permeate flux at
different feed temperature, feed concentration and feed/permeate flow rates. The results show a
membrane with pore size of 0.22µm, thickness of 125µm, porosity of 75% and conductivity of
0.041W/m.K presents the most amount of permeate flux compared to the other membranes,
indicating likely optimum membrane properties for DCMD process.