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March 23, 2026Desalination and Water Treatment2 citationsOpen Access

Selective separation and recovery of strontium from seawater reverse osmosis brine using sequential oxalate precipitation and ion exchange

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JMJeong-Ki MoonSCSangki ChoiTATaebum Ahn

Key Points

  • The aim is to develop an effective recovery process for strontium from seawater reverse osmosis brine using novel techniques.
  • Sequential oxalate precipitation to remove calcium and magnesium
  • Use of an ion-exchange column for strontium enrichment
  • Pre-treatment with NaOH and oxalate to optimize ion ratios
  • Achieved a [Sr 2+ ]/[Ca 2+ ] ratio increase from 0.016 to 2.5
  • Produced a strontium-enriched solution exceeding 4 g/L
  • Maximized [Sr 2+ ]/[Ca 2+ ] ratio of 28.6 with approximately 2 g/L strontium

Abstract

Seawater desalination effectively produces fresh water, yet brine byproducts raise significant environmental concerns. Strontium, a valuable resource in brine, is increasingly sought after due to diminishing terrestrial mineral sources. However, its recovery is challenging because strontium ion (Sr 2+ ) and calcium ion (Ca 2+ ) exhibit similar physicochemical behaviors in the aqueous phase, necessitating advanced recovery technologies. This study proposes an integrated recovery process for seawater reverse osmosis (SWRO) brine combining oxalate-based precipitation and ion exchange. In the pretreatment stage, NaOH and oxalate were employed to sequentially remove magnesium and calcium interferences. Specifically, oxalate addition at a 1.6 molar ratio relative to Ca 2+ preferentially precipitated calcium, drastically increasing the Sr 2+ /Ca 2+ ratio from 0.016 to 2.5, indicating a notable enhancement in Sr 2+ relative to Ca 2+ . For the enrichment of Sr 2+ from the pretreated solution, an ion-exchange column was employed. Two consecutive concentration cycles yielded a Sr-enriched solution exceeding 4 g/L. A post-IEX Ca 2+ removal step further reduced residual calcium, achieving a maximum Sr 2+ /Ca 2+ ratio of 28.6, with a Sr 2+ concentration of approximately 2 g/L. These results demonstrate that an integrated process using sequential oxalate-based precipitation and ion exchange achieves high efficiency in Ca 2+ removal, enhancing the overall feasibility of the Sr 2+ recovery process.

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Cite This Study

Moon et al. (2026) studied this question.

synapsesocial.com/papers/69c08bcaa48f6b84677f97a8https://doi.org/10.1016/j.dwt.2026.101734
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