Dewatering Hypersaline Na2SO4 and NaCl via Commercial Forward Osmosis Module

Efficient water recycling in the hydrometallurgical industry requires the dewatering of hypersaline Na<sub>2</sub>SO<sub>4</sub> or similar brines via non-evaporative methods. Unfortunately, many non-evaporative methods require the use of specific solutes and are not compatible with complex hydrometallurgical effluents. Forward Osmosis (FO) uses a draw solution to link known non-evaporative water recycling methods with feed solutions that are otherwise incompatible. There is minimal experimental data on the dewatering performance of today's available commercial FO membranes, especially with hypersaline concentrations (>70,000 mg/L total dissolved solids). This study tests the commercially available Aquaporin HFFO2 hollow fibre FO membrane module with hypersaline Na<sub>2</sub>SO<sub>4</sub> or NaCl feed solutions versus a MgCl<sub>2</sub> draw solution. It identifies a key requirement to maintain water flux above a certain threshold to prevent a decrease in Na Rejection or an increase in Mg reverse flux. It also defines a minimum osmotic differential that can be used to parameterize water flux, similar to the temperature of approach in heat exchangers, but to determine the extent of water removal in FO. We demonstrate that even under mildly acidic conditions, existing FO membranes can concentrate Na<sub>2</sub>SO<sub>4</sub> to saturation, paving the way for their use in the hydrometallurgical industry.

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Publication Details

Journal
Membranes
Published
2025-12-31
DOI
https://doi.org/10.3390/membranes16010014
Primary Topic
Membrane Separation Technologies
Type
article
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article

Dewatering Hypersaline Na2SO4 and NaCl via Commercial Forward Osmosis Module

Noel Devaere, Vladimiros G. Papangelakis
Membranes
Membrane Separation Technologies
article

Dewatering Hypersaline Na2SO4 and NaCl via Commercial Forward Osmosis Module

Noel Devaere, Vladimiros G. Papangelakis
article en

Abstract

Efficient water recycling in the hydrometallurgical industry requires the dewatering of hypersaline Na<sub>2</sub>SO<sub>4</sub> or similar brines via non-evaporative methods. Unfortunately, many non-evaporative methods require the use of specific solutes and are not compatible with complex hydrometallurgical effluents. Forward Osmosis (FO) uses a draw solution to link known non-evaporative water recycling methods with feed solutions that are otherwise incompatible. There is minimal experimental data on the dewatering performance of today's available commercial FO membranes, especially with hypersaline concentrations (>70,000 mg/L total dissolved solids). This study tests the commercially available Aquaporin HFFO2 hollow fibre FO membrane module with hypersaline Na<sub>2</sub>SO<sub>4</sub> or NaCl feed solutions versus a MgCl<sub>2</sub> draw solution. It identifies a key requirement to maintain water flux above a certain threshold to prevent a decrease in Na Rejection or an increase in Mg reverse flux. It also defines a minimum osmotic differential that can be used to parameterize water flux, similar to the temperature of approach in heat exchangers, but to determine the extent of water removal in FO. We demonstrate that even under mildly acidic conditions, existing FO membranes can concentrate Na<sub>2</sub>SO<sub>4</sub> to saturation, paving the way for their use in the hydrometallurgical industry.

MembranesVol. 16(1)
University of Toronto (CA)
Openalex Percentile: Top 35%
Membrane Separation Technologies
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