TY - JOUR
T1 - Tuning the Performance of Composite Membranes by Optimizing PDMS Content and Cross-Linking Time for Solvent Resistant Nanofiltration
AU - Zhang, Yujing
AU - Zhang, Haoqin
AU - Li, Yifan
AU - Mao, Heng
AU - Yang, Guanghui
AU - Wang, Jingtao
N1 - Publisher Copyright:
© 2015 American Chemical Society.
PY - 2015/6/17
Y1 - 2015/6/17
N2 - Herein, a series of composite membranes with optimized solvent permeance and rejection are prepared by combining the advantages of hybridization and cross-linking techniques. Polyethylenimine (PEI) and hydroxyl terminated trifluoride polydimethylsiloxane (PDMS) are cross-linked with trimesoyl chloride as the skin layer, which is isotropic rather than hierarchical. The chain mobility of PEI is inhibited upon hybridization and cross-linking, affording enhanced solvent resistance and thermal/mechanical stabilities. The composite membrane achieves high rejection ability with the rejection of PEG 1000 of about 100%. Additionally, the synergy of hydrophilic PEI and hydrophobic PDMS segments gives acceptable solvent permeances for acetone (up to 2.7 L m-2 h-1 bar-1) and ethyl acetate (up to 1.4 L m-2 h-1 bar-1). The membrane microstructures are facilely tuned by regulating PDMS content and cross-linking time, allowing the efficient optimization of solvent resistant nanofiltration performances. Moreover, the operational stability and the separation of lotus seedpod proanthocyanidins-ethanol/water mixtures are investigated to evaluate the practical application of the composite membrane.
AB - Herein, a series of composite membranes with optimized solvent permeance and rejection are prepared by combining the advantages of hybridization and cross-linking techniques. Polyethylenimine (PEI) and hydroxyl terminated trifluoride polydimethylsiloxane (PDMS) are cross-linked with trimesoyl chloride as the skin layer, which is isotropic rather than hierarchical. The chain mobility of PEI is inhibited upon hybridization and cross-linking, affording enhanced solvent resistance and thermal/mechanical stabilities. The composite membrane achieves high rejection ability with the rejection of PEG 1000 of about 100%. Additionally, the synergy of hydrophilic PEI and hydrophobic PDMS segments gives acceptable solvent permeances for acetone (up to 2.7 L m-2 h-1 bar-1) and ethyl acetate (up to 1.4 L m-2 h-1 bar-1). The membrane microstructures are facilely tuned by regulating PDMS content and cross-linking time, allowing the efficient optimization of solvent resistant nanofiltration performances. Moreover, the operational stability and the separation of lotus seedpod proanthocyanidins-ethanol/water mixtures are investigated to evaluate the practical application of the composite membrane.
UR - http://www.scopus.com/inward/record.url?scp=84934995132&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.5b01236
DO - 10.1021/acs.iecr.5b01236
M3 - Article
AN - SCOPUS:84934995132
SN - 0888-5885
VL - 54
SP - 6175
EP - 6186
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 23
ER -