132
S. Pakdel et al.
Fig. 14 Contact angle and pure water flux (after 60 min) of the prepared membranes. The figure
is adapted with permission from Elsevier [39]
Fig. 15 Dye retention performance of the PES/GO nanofiltration membranes (0.4 MPa, pH = 6.0
± 0.1, after 60 min filtration).The figure is adapted with permission from Elsevier [39]
the membranes was determined, which is presented in Fig. 16. The impregnation of
GO into the PES membrane can considerably enhance the antifouling property of
the modified PES membranes compared with the unfilled one.
Bano et al. [108] demonstrated that impregnation of GO into a TFC-PA can effectively increase its hydrophilicity, which resulted in its flux and antifouling property
improvement [118, 120]. GO was incorporated into PA polymer using interfacial
polymerization to develop TFN-PA/GO matrix membrane. The GO was loaded into
S. Pakdel et al.
Fig. 14 Contact angle and pure water flux (after 60 min) of the prepared membranes. The figure
is adapted with permission from Elsevier [39]
Fig. 15 Dye retention performance of the PES/GO nanofiltration membranes (0.4 MPa, pH = 6.0
± 0.1, after 60 min filtration).The figure is adapted with permission from Elsevier [39]
the membranes was determined, which is presented in Fig. 16. The impregnation of
GO into the PES membrane can considerably enhance the antifouling property of
the modified PES membranes compared with the unfilled one.
Bano et al. [108] demonstrated that impregnation of GO into a TFC-PA can effectively increase its hydrophilicity, which resulted in its flux and antifouling property
improvement [118, 120]. GO was incorporated into PA polymer using interfacial
polymerization to develop TFN-PA/GO matrix membrane. The GO was loaded into