卤水
反渗透
缩放比例
环境科学
渗透
石油工程
工艺工程
计算机科学
化学
工程类
膜
数学
有机化学
生物化学
几何学
作者
Emily W. Tow,Quantum J. Wei,Alyson Abraham,Kei L. Chua,Michael Plumley,John H. Lienhard
标识
DOI:10.1038/s41545-025-00462-6
摘要
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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