TY - JOUR
T1 - Chemistry in a spinneret - On the interplay of crosslinking and phase inversion during spinning of novel hollow fiber membranes
AU - Kopec, K.K.
AU - Dutczak, S.M.
AU - Wessling, Matthias
AU - Stamatialis, Dimitrios
PY - 2011
Y1 - 2011
N2 - This work explores a new method of simultaneous membrane formation and chemical modification in a spinning process for fabricating asymmetric composite hollow fiber membranes. This method is based on controlled crosslinking reaction between the membrane forming polyimide P84 and the chemically modifying poly(ethylene imine) (PEI) dissolved in the bore liquid. We study the interplay between phase inversion and crosslinking, which determines the final morphology and chemistry of the hollow fiber membrane.
Depending on the composition of chemically active bore liquid, two different types of membranes can be fabricated. The first type is a membrane with a dense, crosslinked, gas selective inner layer (thickness in the range 1.4–6.1 μm) having a mixed gas CO2/N2 selectivity 12 in the presence of water vapor. The second type is an entirely crosslinked membrane which is not soluble in NMP; it is porous (pure water flux 44.4 ± 1.2 l/(m2 bar h)) and selective for the separation of similar size proteins, bovine serum albumin (BSA) and hemoglobin (Hb), due to the charge of the membrane. The isoelectric point of the new membrane is basic (pH 9.3), much higher than that of the P84 membrane (pH 3.75).
The ease of process operation (only the bore composition needs to be modified) opens new perspectives towards applications in the area of gas separation and/or liquid filtration, the latter especially in harsh solvent environments.
AB - This work explores a new method of simultaneous membrane formation and chemical modification in a spinning process for fabricating asymmetric composite hollow fiber membranes. This method is based on controlled crosslinking reaction between the membrane forming polyimide P84 and the chemically modifying poly(ethylene imine) (PEI) dissolved in the bore liquid. We study the interplay between phase inversion and crosslinking, which determines the final morphology and chemistry of the hollow fiber membrane.
Depending on the composition of chemically active bore liquid, two different types of membranes can be fabricated. The first type is a membrane with a dense, crosslinked, gas selective inner layer (thickness in the range 1.4–6.1 μm) having a mixed gas CO2/N2 selectivity 12 in the presence of water vapor. The second type is an entirely crosslinked membrane which is not soluble in NMP; it is porous (pure water flux 44.4 ± 1.2 l/(m2 bar h)) and selective for the separation of similar size proteins, bovine serum albumin (BSA) and hemoglobin (Hb), due to the charge of the membrane. The isoelectric point of the new membrane is basic (pH 9.3), much higher than that of the P84 membrane (pH 3.75).
The ease of process operation (only the bore composition needs to be modified) opens new perspectives towards applications in the area of gas separation and/or liquid filtration, the latter especially in harsh solvent environments.
KW - IR-77514
KW - METIS-282875
U2 - 10.1016/j.memsci.2010.12.010
DO - 10.1016/j.memsci.2010.12.010
M3 - Article
SN - 0376-7388
VL - 369
SP - 308
EP - 318
JO - Journal of membrane science
JF - Journal of membrane science
IS - 1-2
ER -