Abstract
This study investigates the performance of solvent extraction desalination (SED) using three amine solvents DPA, DIPA, and DBA under various temperature and ion valency conditions. The results revealed that reaction and separation temperatures significantly influenced water recovery and salt removal efficiencies. DIPA demonstrated the highest water recovery, while DPA exhibited superior salt removal efficiency. Mg²⁺ was effectively removed through a precipitation mechanism, distinct from the polarity-driven removal of sodium chloride. Additionally, reuse experiments over nine cycles showed stable performance in water recovery and salt removal, emphasizing the economic and operational feasibility of SED. These findings highlight the adaptability and potential of SED as a membrane-free desalination technology for high-brine scenarios, offering a sustainable alternative for seawater and brine treatment.
| Original language | English |
|---|---|
| Pages (from-to) | 95-100 |
| Number of pages | 6 |
| Journal | Membrane and Water Treatment |
| Volume | 16 |
| Issue number | 2 |
| DOIs | |
| Publication status | Published - 2025 Mar |
Bibliographical note
Publisher Copyright:© 2025 Techno-Press, Ltd.
Keywords
- amine solvents (DPA, DIPA, DBA)
- magnesium ion (Mg²⁺) removal
- salt removal efficiency
- solvent extraction desalination
- solvent reuse
- water recovery efficiency
ASJC Scopus subject areas
- General Chemical Engineering
- Water Science and Technology
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