The Evaluation of Ammonium Sulphate as a Potential Draw Solute in a Hybrid FO-RO Process to Concentrate Nutrients (NPK) from a Simulated Liquid Digestate—Part I: Deionized Water as a Feed Solution

The ultimate objective of this research is to concentrate nutrients-nitrogen (N), phosphorus (P), and potassium (K)-and produce process water from a chemically pretreated liquid digestate using an FO-RO hybrid process. However, in this manuscript, we assessed the suitability of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> and NaCl as draw solutes in a series of FO experiments employing a commercial CTA membrane and DI water as the feed solution. We also examined the regeneration of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> in a series of RO experiments at various feed concentrations and pressures using a commercial polyamide (PA) thin-film composite (TFC) membrane, ACM4. Additionally, the RO experiments enabled the experimental determination of the osmotic pressure of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> at various feed concentrations, which is crucial for designing the FO part of the hybrid process. The CTA membrane exhibited a significantly greater selectivity for (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> than for NaCl at any osmotic pressure. The RO experiments demonstrated the possibility of reconcentrating (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> to 0.5 mol/L, with a corresponding water flux of 60 L h<sup>-1</sup> m<sup>-2</sup> at 40 bars. The experimentally determined osmotic pressures were lower than those predicted by van't Hoff's equation but were consistent with those reported in the literature using an indirect hygrometric method.

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Journal
Membranes
Published
2025-12-01
DOI
https://doi.org/10.3390/membranes15120366
Primary Topic
Membrane Separation Technologies
Type
article
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article

The Evaluation of Ammonium Sulphate as a Potential Draw Solute in a Hybrid FO-RO Process to Concentrate Nutrients (NPK) from a Simulated Liquid Digestate—Part I: Deionized Water as a Feed Solution

Reeni A. Abraham, Boguslaw Kruczek, Majid Sartaj, Niloofar Abdehagh et al.
Membranes
Membrane Separation Technologies
article

The Evaluation of Ammonium Sulphate as a Potential Draw Solute in a Hybrid FO-RO Process to Concentrate Nutrients (NPK) from a Simulated Liquid Digestate—Part I: Deionized Water as a Feed Solution

Reeni A. Abraham, Boguslaw Kruczek, Majid Sartaj, Niloofar Abdehagh, Marsa Tolouei
article en

Abstract

The ultimate objective of this research is to concentrate nutrients-nitrogen (N), phosphorus (P), and potassium (K)-and produce process water from a chemically pretreated liquid digestate using an FO-RO hybrid process. However, in this manuscript, we assessed the suitability of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> and NaCl as draw solutes in a series of FO experiments employing a commercial CTA membrane and DI water as the feed solution. We also examined the regeneration of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> in a series of RO experiments at various feed concentrations and pressures using a commercial polyamide (PA) thin-film composite (TFC) membrane, ACM4. Additionally, the RO experiments enabled the experimental determination of the osmotic pressure of (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> at various feed concentrations, which is crucial for designing the FO part of the hybrid process. The CTA membrane exhibited a significantly greater selectivity for (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> than for NaCl at any osmotic pressure. The RO experiments demonstrated the possibility of reconcentrating (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub> to 0.5 mol/L, with a corresponding water flux of 60 L h<sup>-1</sup> m<sup>-2</sup> at 40 bars. The experimentally determined osmotic pressures were lower than those predicted by van't Hoff's equation but were consistent with those reported in the literature using an indirect hygrometric method.

MembranesVol. 15(12)
Natural Resources Canada (CA), University of Ottawa (CA)
Natural Sciences and Engineering Research Council of Canada, Agriculture and Agri-Food Canada
Openalex Percentile: Top 65%
Membrane Separation Technologies
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