Practical energy-efficient reverse osmosis: experimental and modeling investigation for high-temperature water treatment
Reducing the energy demands of conventional water treatment systems is crucial. High-temperature treatment can be efficient when waste heat is freely available, such as from geothermal or steam-assisted gravity drainage (SAGD) produced water. These industrial streams present both an opportunity and a challenge: elevated temperatures enable integration with heat-recovery systems, yet most commercial membranes lose performance or stability under such conditions. In this study, we developed and evaluated lab-synthesized thin-film composite (TFC) high-temperature reverse osmosis (HTRO) membranes capable of stable operation from room temperature to 120 °C. The best-performing membrane (TFC3, made with 2 wt% TAP) achieved 255 LMH flux at 120 °C, over 190 % higher than the control membrane, and maintained >96 % salt rejection with only 12.9 % flux decline over seven hours of continuous operation. These results show higher permeability and thermal stability than the commercial AG membrane, due to greater polyamide crosslinking and better substrate thermal resistance. A temperature-dependent modeling framework was developed and validated against experimental data. Both convective and diffusive transport models were evaluated, with the diffusive model showing better agreement with the experiments. Energy analysis showed that optimized HTRO membranes can significantly reduce specific energy consumption (SEC) at high temperatures relative to ambient-temperature RO, reaching values as low as ~0.5 kWh/m 3 under geothermal-like conditions. These findings highlight the potential of high-performance HTRO membranes to address the energy intensity of conventional water treatment in thermally intensive industries. • Lab-made HTRO TFC membranes show stable operation from 25 to 120 °C in extended testing. • Trifunctional monomer boosts crosslinking, permeability, and stability in high-T TFCs • Diffusive-flow model best matches temperature-dependent flux and salt transport data. • Operating on hot feeds reduces SEC vs ambient RO; SAGD and geothermal cases assessed. • HTRO–ORC integration recovers energy while producing freshwater efficiently at scale.
Authors
- Mohtada Sadrzadeh (ORCID: https://orcid.org/0000-0002-0403-8351)
- Pooria Karami (ORCID: https://orcid.org/0000-0001-5532-6882)
- Nazanin Chitgar (ORCID: https://orcid.org/0000-0002-7813-192X)
Institutions
- University of Alberta (CA)
Publication Details
- Journal
- Desalination
- Published
- 2025-10-18
- DOI
- https://doi.org/10.1016/j.desal.2025.119541
- Primary Topic
- Membrane Separation Technologies
- Type
- article
- Field-Weighted Citation Impact
- 0.00