TY - JOUR
T1 - Nanofiltration of dye solution using chitosan/poly(vinyl alcohol)/ZIF-8 thin film composite adsorptive membranes with PVDF membrane beneath as support
AU - Khajavian, Mohammad
AU - Salehi, Ehsan
AU - Vatanpour, Vahid
N1 - Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2020/11/1
Y1 - 2020/11/1
N2 - Nanobiocomposite adsorptive membranes were engineered by integrating metal-organic frameworks (ZIF-8), into the chitosan/poly(vinyl alcohol) blend and coating the blend on PVDF membrane support for an enhanced separation performance. The membranes were characterized by SEM, AFM, BET, XRD, ATR-FTIR and tensile stress analyses. The central composite design was utilized to optimize the water flux and dye rejection. Using CCD, the effect of the membrane thickness, PEG (pore-former), and chitosan content on the flux and rejection were studied. The optimal conditions were obtained as; 10 wt% PEG, 3 wt% chitosan, and 200 μm membrane thickness. The optimized flux and rejection were obtained 78.94 L m−2 h-1 and 90.3 %, respectively. The antifouling of the membranes was also examined by the filtration of BSA protein solution. The membranes showed comparable performance; however, extremely higher permeability (78.94 L m−2 h-1 bar -1) compared to similar TFC membranes that guarantee the economic favorability of the filtration process.
AB - Nanobiocomposite adsorptive membranes were engineered by integrating metal-organic frameworks (ZIF-8), into the chitosan/poly(vinyl alcohol) blend and coating the blend on PVDF membrane support for an enhanced separation performance. The membranes were characterized by SEM, AFM, BET, XRD, ATR-FTIR and tensile stress analyses. The central composite design was utilized to optimize the water flux and dye rejection. Using CCD, the effect of the membrane thickness, PEG (pore-former), and chitosan content on the flux and rejection were studied. The optimal conditions were obtained as; 10 wt% PEG, 3 wt% chitosan, and 200 μm membrane thickness. The optimized flux and rejection were obtained 78.94 L m−2 h-1 and 90.3 %, respectively. The antifouling of the membranes was also examined by the filtration of BSA protein solution. The membranes showed comparable performance; however, extremely higher permeability (78.94 L m−2 h-1 bar -1) compared to similar TFC membranes that guarantee the economic favorability of the filtration process.
KW - Chitosan
KW - Membrane adsorbent
KW - Metal-organic frameworks
KW - Optimization
UR - http://www.scopus.com/inward/record.url?scp=85086993161&partnerID=8YFLogxK
U2 - 10.1016/j.carbpol.2020.116693
DO - 10.1016/j.carbpol.2020.116693
M3 - Article
C2 - 32829821
AN - SCOPUS:85086993161
SN - 0144-8617
VL - 247
JO - Carbohydrate Polymers
JF - Carbohydrate Polymers
M1 - 116693
ER -