In this work, adsorption and membrane separation were
combined
to remove adsorbable contaminants from water at lower energy requirements.
Such an approach was investigated for arsenic (As) removal with hematite
nanoparticles (70 ± 20 nm) immobilized in a microporous (0.2
μm pore size) poly(vinylidene fluoride) (PVDF) membrane. Hematite
loading and hydraulic residence time with the role of speciation were
investigated for As(III) and As(V) removal using hematite-loaded composite
membrane (HLCM). During the flow-through filtration, it was observed
50% removal for As(III), while only 15% As(V) was removed at pH 8
with 2.6 mg/cm2 hematite loading, equivalent to uptakes
of 5.5 ± 0.8 μgAs(III)/cm2 and 3.9 ± 0.6
μgAs(V)/cm2. Varying the pH from 2 to 12 and, ultimately,
As(III, V) speciation showed a significant impact on the uptake, especially
for As(V). In this case, increasing the NaCl concentration from 0.58
to 20 g/L hindered the charge attraction. Arsenic uptake increased
with increasing the hematite loading from 0.7 to 3.9 mg/cm2, while the impact of the hydraulic residence time (flux) was observed.
Arsenic uptake by this composite membrane requires further improvement
in terms of adsorption capacity. Increasing the loading of hematite
in the membrane or chemical modifications of hematite to achieve enhanced
affinity for As(III, V) will be part of further material modification.
From the water treatment perspective, the composite membrane potentially
provides effective removal with a lower specific energy consumption
compared to nanofiltration.