Diffusion dialysis (DD) is effective to separate and recover acid component from acid feed, but the performance is restricted by the narrow and short flowing channels due to the conventional flat membranes and plate-and-frame dialyzer. Hence, tubular membranes, as prepared from polyvinyl alcohol (PVA), are serially connected to form a long tubular channel for running acid feed including H2SO4/FeSO4 and HCl/FeCl2. The tubular membranes are installed in 3D-printing dialyzers, which provide a long furrow channel for running water. Hence, furrow and tubular channels are formed for continuous DD process. As the number of tubular membranes in furrow channel increases from 1, 6 to 12, the channel length increases from 80, 300 to 600 cm.The tubular membrane shows tensile strength of 3.0 – 5.2 MPa and elongation at break of 251 – 316% after swelling in water or acid feeds. The membrane packing density in dialyzer reaches up to 425 cm2‧L-1, with the weight percent of 5.2%. Continuous DD process shows water reverse osmosis (from -1.7 to -15.4 mol‧m-2‧h-1) due to the higher pressure in the tubular channel. As the channel length increases from 80 to 600 cm, the ion transport rates increase as reflected by the recovered acid concentration (Cd-H), recovery ratio (RH) and Fe2+ rejection ratio (ηFe). The Cd-H increases from 0.83 to 2.08 mol‧L-1 (M), the RH increases from 29.6% to 70.0%, and the ηFe decreases from 97.9% to 86.5% at the flow rate of 1.49 L m-2 h-1 for the H2SO4/FeSO4 after 8 h. As for the HCl/FeCl2, the RH and ηFe can be balanced at 83.1% and 80.1% correspondingly when the channel length is 600 cm, and the residual acid concentration is only 0.17 – 0.22 M. The DD performances are generally stable after an acid immersion of seven days. Hence, a simple and effective separation can be realized by the long channels.
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