TY - JOUR
T1 - Pore structure control of PVDF membranes using a 2-stage coagulation bath phase inversion process for application in membrane distillation (MD)
AU - Thomas, Rinku
AU - Guillen-Burrieza, Elena
AU - Arafat, Hassan A.
PY - 2014/2/15
Y1 - 2014/2/15
N2 - Polyvinylidenefluoride (PVDF) membranes were fabricated using non-solvent assisted phase inversion technique (NIPS) to ultimately create a membrane distillation (MD) membrane. No pore forming additives were employed, in order to maintain the pore size distribution (PSD) as narrow as possible. Instead, a 2-stage coagulation bath system was used. The effects of the CB temperature, immersion time, polymer solution concentration, and thickness of the casted PVDF membranes were investigated. Prospective membranes with a uniform and open structure on the surface and an asymmetric interconnected pore structure all through the thickness of the membranes were obtained. A narrow PSD (0.14-0.2 μm) along with a high liquid entry pressure (LEP) range of 420-570 kPa and porosity values ranging from 57% to 79% were observed in the fabricated membranes, with a contact angle variance from 100° to 127°. The synergy of hydrophobicity, mechanical strength, high LEP and a very narrow PSD made the fabricated membranes suitable candidates for MD applications. Direct Contact (DCMD) and Vacuum MD (VMD) testing using these membranes were then carried out to analyze and understand their operational MD performance. The membranes were found to yield acceptable water vapor flux in MD and a narrower PSD than commercial PVDF membranes with similar nominal pore size. The salt rejection achieved was lower than expected, which was explained based on pore wetting.
AB - Polyvinylidenefluoride (PVDF) membranes were fabricated using non-solvent assisted phase inversion technique (NIPS) to ultimately create a membrane distillation (MD) membrane. No pore forming additives were employed, in order to maintain the pore size distribution (PSD) as narrow as possible. Instead, a 2-stage coagulation bath system was used. The effects of the CB temperature, immersion time, polymer solution concentration, and thickness of the casted PVDF membranes were investigated. Prospective membranes with a uniform and open structure on the surface and an asymmetric interconnected pore structure all through the thickness of the membranes were obtained. A narrow PSD (0.14-0.2 μm) along with a high liquid entry pressure (LEP) range of 420-570 kPa and porosity values ranging from 57% to 79% were observed in the fabricated membranes, with a contact angle variance from 100° to 127°. The synergy of hydrophobicity, mechanical strength, high LEP and a very narrow PSD made the fabricated membranes suitable candidates for MD applications. Direct Contact (DCMD) and Vacuum MD (VMD) testing using these membranes were then carried out to analyze and understand their operational MD performance. The membranes were found to yield acceptable water vapor flux in MD and a narrower PSD than commercial PVDF membranes with similar nominal pore size. The salt rejection achieved was lower than expected, which was explained based on pore wetting.
KW - Dual coagulation bath
KW - Membrane distillation
KW - Membrane fabrication
KW - Membrane wetting
KW - Phase inversion
KW - PVDF
UR - http://www.scopus.com/inward/record.url?scp=84891482719&partnerID=8YFLogxK
U2 - 10.1016/j.memsci.2013.11.036
DO - 10.1016/j.memsci.2013.11.036
M3 - Article
AN - SCOPUS:84891482719
SN - 0376-7388
VL - 452
SP - 470
EP - 480
JO - Journal of Membrane Science
JF - Journal of Membrane Science
ER -