Piloting batch reverse osmosis with a flexible bladder for water recovery from scaling-prone brine

A pilot-scale batch reverse osmosis (RO) system with a flexible bladder was designed to recover additional water from RO concentrate. The sulfate-rich, ~6400-ppm concentrate was sourced from the Yuma Desalting Plant (Arizona, USA), which desalinates agricultural drainage water. The pilot produced 4.4 m3/day of permeate with 150 ppm total dissolved solids from the facility’s concentrate stream with a recovery ratio of 82.6%. Despite producing supersaturated brine, there was no performance deterioration due to scaling. Using a bladder for retentate pressurization limited average power to 633 W and the specific energy consumption to 3.3 kWh/m3. The pilot’s energy data informed a model of large-scale batch RO, which has the potential to desalinate the same water for less than 1 kWh/m3. Additionally, a model was developed to predict scaling likelihood in batch RO. This investigation demonstrates that batch RO is a viable technology for low-energy brine concentration beyond saturation limits.

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Publication Details

Journal
npj Clean Water
Published
2025-04-15
DOI
https://doi.org/10.1038/s41545-025-00462-6
Citations
11
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
8.99

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article

Piloting batch reverse osmosis with a flexible bladder for water recovery from scaling-prone brine

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11 citations
npj Clean Water
Membrane Separation Technologies
8.99
article

Piloting batch reverse osmosis with a flexible bladder for water recovery from scaling-prone brine

Quantum J. Wei, Emily W. Tow, Alyson Abraham, John H. Lienhard, Michael Plumley, Kei L. Chua
article en
11 citations

Abstract

A pilot-scale batch reverse osmosis (RO) system with a flexible bladder was designed to recover additional water from RO concentrate. The sulfate-rich, ~6400-ppm concentrate was sourced from the Yuma Desalting Plant (Arizona, USA), which desalinates agricultural drainage water. The pilot produced 4.4 m3/day of permeate with 150 ppm total dissolved solids from the facility’s concentrate stream with a recovery ratio of 82.6%. Despite producing supersaturated brine, there was no performance deterioration due to scaling. Using a bladder for retentate pressurization limited average power to 633 W and the specific energy consumption to 3.3 kWh/m3. The pilot’s energy data informed a model of large-scale batch RO, which has the potential to desalinate the same water for less than 1 kWh/m3. Additionally, a model was developed to predict scaling likelihood in batch RO. This investigation demonstrates that batch RO is a viable technology for low-energy brine concentration beyond saturation limits.

npj Clean WaterVol. 8(1)
Franklin W. Olin College of Engineering (US), United States Coast Guard Academy (US), Harmonic Drive (Germany) (DE), Massachusetts Institute of Technology (US)
Henry Luce Foundation, Bureau of Reclamation
Clean water and sanitation
Openalex Percentile: Top 2%
Membrane Separation Technologies
8.99
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