Membrane fouling is a critical problem for efficient commercialization of nanofiltration plants. A nano-MgO/
GAC (Granular Activated Carbon) process was investigated the feasibility of using as pre-treatment for
nanofiltration. Based on the results obtained, nano-MgO could decrease 51% of Permanganate Index (CODMn),
60% of the ultraviolet absorbance at 254 nm (UVA254), and more than 99% of colony counts within 6 h. The pH
increased to about 10.30 within only 0.5 h and then kept stable in the system containing nano-MgO. In
addition, adding GAC led to less organic matters (remaining 4.74 mg·L−1 versus 6.80 mg·L−1) and bacteria
(13 CFU·mL−1 versus 15 CFU·mL−1) relative to using nano-MgO only. Furthermore, almost all nano-MgO
could be adsorbed by the GAC column. The pH value of the effluents from the nano-MgO and GAC was 10.18
and 10.20, respectively, while that of the effluent after KH2PO4 adjustment could keep about 7.10.
Membrane fouling is a critical problem for efficient commercialization of nanofiltration plants. A nano-MgO/
GAC (Granular Activated Carbon) process was investigated the feasibility of using as pre-treatment for
nanofiltration. Based on the results obtained, nano-MgO could decrease 51% of Permanganate Index (CODMn),
60% of the ultraviolet absorbance at 254 nm (UVA254), and more than 99% of colony counts within 6 h. The pH
increased to about 10.30 within only 0.5 h and then kept stable in the system containing nano-MgO. In
addition, adding GAC led to less organic matters (remaining 4.74 mg·L−1 versus 6.80 mg·L−1) and bacteria
(13 CFU·mL−1 versus 15 CFU·mL−1) relative to using nano-MgO only. Furthermore, almost all nano-MgO
could be adsorbed by the GAC column. The pH value of the effluents from the nano-MgO and GAC was 10.18
and 10.20, respectively, while that of the effluent after KH2PO4 adjustment could keep about 7.10.
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