A laboratory-constructed flowing liquid membrane apparatus with porous part
ition (FLM) was applied to the separation of such polyunsaturated fatty aci
d esters (PUFA-Ets) as eicosapentaenoic acid ethylester (EPA-Et) and docosa
hexaenoic acid ethylester (DHA-Et) at 293 K. The hydrophilic porous membran
e was used as a partition, and 2 M AgNO3 aqueous solution was used as a mem
brane liquid. By using dodecane as a feed diluent and m-xylene as a recover
y solution, PUFA-Ets were successfully separated from mixture of fatty acid
esters. The recovery fraction of PUFA-Ets and the separation degree betwee
n DHA-Et and EPA-Et were investigated; it increases with the velocity of me
mbrane liquid and the flow path length in the module, while it decreased wi
th the velocity of feed and recovery solution. The recovery fraction of DHA
-Et reachs 60% with only 8 s-retention time by the continuous operation. Th
e concentrations of the DHA-Et at the outlet of the module were simulated b
ased on the mass transfer model, which gave nearly 85% recovery fraction wi
th 30 s-retention time. These results show that a stable operation, a high
recovery and a high throughput are realized by the FLM.