TY - JOUR
T1 - Scalable Chitosan-Graphene Oxide Membranes
T2 - The Effect of GO Size on Properties and Cross-Flow Filtration Performance
AU - Abolhassani, Mojtaba
AU - Griggs, Chris S.
AU - Gurtowski, Luke A.
AU - Mattei-Sosa, Jose A.
AU - Nevins, Michelle
AU - Medina, Victor F.
AU - Morgan, Timothy A.
AU - Greenlee, Lauren F.
N1 - Funding Information:
We acknowledge the Institute for Nanoscience and Engineering at the University of Arkansas for facilitating and supporting membrane characterization and data analysis. We acknowledge Prof. Kartik Balachandran and his research group at the University of Arkansas for help with tensile testing of the membranes. Funding for membrane fabrication and cross-flow filtration testing was provided by the U.S. Army Environmental Quality and Installations Research Program (Dr. E. Ferguson, Technical Director).
Publisher Copyright:
© 2017 American Chemical Society.
PY - 2017/12/31
Y1 - 2017/12/31
N2 - Chitosan (CS)-graphene oxide (GO) composite films were fabricated, characterized, and evaluated as pressure-driven water filtration membranes. GO particles were incorporated into a chitosan polymer solution to form a suspension that was cast as a membrane via evaporative phase inversion allowing for scale-up for cross-flow testing conditions. Morphology and composition results for nano and granular GO in the CS matrix indicate that the particle size of GO impacts the internal membrane morphology as well as the structural order and the chemical composition. Performance of the membranes was evaluated with cationic and anionic organic probe molecules and revealed charge-dependent mechanisms of dye removal. The CSGO membranes had rejections of at least 95% for cationic methylene blue with mass balances obtained from measurements of the feed, concentrate, and permeate. This result suggests the dominant mechanism of removal is physical rejection for both GO particle sizes. For anionic methyl orange, the results indicate sorption as the dominant mechanism of removal, and performance is dependent on both GO particle size and time, with micrometer-scale GO removing 68-99% and nanometer-scale GO showing modest removal of 29-64%. The pure water flux for CSGO composite membranes ranged from 2-4.5 L/m2 h at a transmembrane pressure of 344 kPa (3.44 bar), with pure water permeance ranging from 5.8 × 10-3 to 0.01 L/m2 h kPa (0.58-1.3 L/m2 h bar). Based on the 41 μm membrane thickness obtained from microscopy, the hydraulic permeability ranged from 0.24-0.54 L μm/m2 h kPa (24.4-54.1 L μm/m2 h bar).
AB - Chitosan (CS)-graphene oxide (GO) composite films were fabricated, characterized, and evaluated as pressure-driven water filtration membranes. GO particles were incorporated into a chitosan polymer solution to form a suspension that was cast as a membrane via evaporative phase inversion allowing for scale-up for cross-flow testing conditions. Morphology and composition results for nano and granular GO in the CS matrix indicate that the particle size of GO impacts the internal membrane morphology as well as the structural order and the chemical composition. Performance of the membranes was evaluated with cationic and anionic organic probe molecules and revealed charge-dependent mechanisms of dye removal. The CSGO membranes had rejections of at least 95% for cationic methylene blue with mass balances obtained from measurements of the feed, concentrate, and permeate. This result suggests the dominant mechanism of removal is physical rejection for both GO particle sizes. For anionic methyl orange, the results indicate sorption as the dominant mechanism of removal, and performance is dependent on both GO particle size and time, with micrometer-scale GO removing 68-99% and nanometer-scale GO showing modest removal of 29-64%. The pure water flux for CSGO composite membranes ranged from 2-4.5 L/m2 h at a transmembrane pressure of 344 kPa (3.44 bar), with pure water permeance ranging from 5.8 × 10-3 to 0.01 L/m2 h kPa (0.58-1.3 L/m2 h bar). Based on the 41 μm membrane thickness obtained from microscopy, the hydraulic permeability ranged from 0.24-0.54 L μm/m2 h kPa (24.4-54.1 L μm/m2 h bar).
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U2 - 10.1021/acsomega.7b01266
DO - 10.1021/acsomega.7b01266
M3 - Article
AN - SCOPUS:85053461347
SN - 2470-1343
VL - 2
SP - 8751
EP - 8759
JO - ACS Omega
JF - ACS Omega
IS - 12
ER -