Examines fluoride transport characteristics in membranes, showing implications for water purification efficiency.
This study primarily investigates the effect of feed concentration on the fluoride ion permeability coefficient (Ps) and reflection coefficient (σ) for two membranes: TW30 (reverse osmosis) and NF270 (nanofiltration), using three transport models: the Kedem–Katchalsky (KK), Spiegler–Kedem (SK), and the Nernst–Planck model coupled with film theory (NP-TF). Pore size estimation was performed using three distinct models: Steric hindrance pore (SHP), Ferry (neglecting solute-pore wall interactions), and Verniory (accounting for frictional forces). Experiments were conducted with sodium fluoride (NaF) solutions in distilled water across fluoride concentrations ranging from 10 to 25 mg/L. A linear relationship was observed between the initial fluoride concentration and σ for both membranes, accompanied by a progressive decrease in Ps. This concentration dependence was more pronounced for the NF270 membrane than for the TW30 membrane. The NF270 membrane's pore diameter varied significantly by model: 0.193 nm (SHP), 0.221 nm (Ferry), 0.243 nm (Verniory). This highlights complex solute transport involving diffusive-convective flow, influenced by steric exclusion and pore frictional forces. Conversely, TW30's dense polyamide structure facilitates diffusive transport via solution-diffusion. Its hydraulic pore diameter averages 0.17 nm. Thus, size exclusion and frictional effects persist but play a reduced role in fluoride rejection.
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Mohamed et al. (2026) studied this question.
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