Figure 7.
(a) The oil–water separation devices, (b,c) the separation efficiency and the water flux of n-hexane/water mixtures for CC@TiO2, CC@Cu:TiO2 and CC@Cu:TiO2@ AgY (Y = 0.1, 0.2, 0.3, 0.4, 0.5 and 0.6) membranes.
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