Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6477260 | Journal of Environmental Chemical Engineering | 2017 | 9 Pages |
â¢To study on the feasibility of NF300 and PN40 nanofiltration membranes for rejection of Cr(VI) and F from binary solution.â¢Characterization of NF300 and PN40 membrane with FTIR, SEM, and AFM.â¢Rejection of Cr(VI) and F was enhanced with increasing pressure and significant influence by pH of feed solution.â¢Membrane transport parameter and mass transfer coefficient was estimated by using CFSK model.â¢Experimental observed rejection and true rejection by Cr(VI) and F show good arrangement.
The current work examines the performance of NF300 and PN40 nanofiltration (NF) membranes for simultaneous rejection of Cr(VI) and F.Experimental: results indicate that, Cr(VI) and F percentage of removal was improved with increasing operating pressure and declined with increasing feed concentration. Highest percent rejection of Cr(VI) and F were found 97% and 92% with NF300 and 88% and 82% with PN40 membranes for 5Â ppm feed respectively. Maximum removal was found at pH 8 and above with NF300 membrane compared to PN40 membrane. Mass transfer coefficient (MTC) was found 6.88Â ÃÂ 104Â cm/s and 5.74Â ÃÂ 104Â cm/s and membrane transport parameters (MTPs) such as solute permeability was 4.03Â ÃÂ 105Â cm/s and 6.23Â ÃÂ 105Â cm/s and reflection coefficient was 0.9688 and 0.9223 using CFSK model for 5Â ppm feed of Cr(VI) and F respectively for NF300 membrane. A Good correlation was found in experimental results (observed rejection for Cr(VI) and F was 0.97 and 0.92) and the model predicts results (true rejection for Cr(VI) and F was 0.9731 and 0.9222) for 5Â ppm feed of Cr(VI) and F respectively for NF300 membrane.