Abstract
For thin film composite (TFC) reverse osmosis (RO) membranes, a trade-off is evident between water permeance and salt rejection; and yet to improve their RO performance it is desirable to increase flux without sacrificing selectivity. This paper describes the fabrication of polyamide TCF membranes on highly solvent stable cross-linked polyimide UF supports and the use of an activating solvent as a strategy to increase water flux; and in certain cases, water permeance and salt rejection are increased simultaneously. Performance was evaluated in terms of NaCl rejection and water permeance before and after post-treatment with dimethylformamide (DMF) as the activating solvent. Additionally, the morphology of the TFC membranes was characterized by SEM, their hydrophilicity was determined by contact angle measurements, and zeta (ζ)-potential was obtained by a streaming potential based method. NaCl rejection was found to be improved for TFC membranes with initial NaCl rejections below 90%, reaching a maximum value of 94%. Water permeance was also increased and to greater extent for membranes with low initial permeance values. The biggest improvement was obtained for a TFC membrane with initial permeance value of 0.2L·m-2·h-1·bar-1, rising to 1.6L·m-2·h-1·bar-1 with a rejection of 93.8%. © 2014 Elsevier B.V.
| Original language | English |
|---|---|
| Pages (from-to) | 181-188 |
| Number of pages | 7 |
| Journal | Desalination |
| Volume | 344 |
| DOIs | |
| Publication status | Published - 1 Jul 2014 |
Keywords
- Activating solvent
- Cross-linked polyimide support membrane
- Interfacial polymerization (IP)
- Polyamide (PA)
- Reverse osmosis (RO)
- Thin film composite (TFC) membranes
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