Efficient salt recovery from aqueous streams using multistage liquid-liquid extraction with thermo-responsive polymers

Liquid-liquid extraction (LLX) using thermo-responsive polymers is a promising low-energy alternative for concentrating hypersaline brines from reverse osmosis (RO). This study presents a comprehensive evaluation of a multistage crosscurrent LLX process, comparing poly(propylene glycol) 400 (PPG 400) and the nonionic surfactant Dehypon® LS54. The methodology includes determining liquid-liquid equilibrium (LLE) data, a theoretical graphical multistage countercurrent LLX analysis, four-stage crosscurrent batch experiments, solvent regeneration, and product purification via thermally induced phase separation (TIPS). LLE results revealed that PPG 400 possesses higher water over salt selectivity. Using ternary diagrams from LLE results, it was found that PPG 400 and Dehypon® LS54 require four and five theoretical stages, respectively, to increase the NaCl concentration from 7 to 20 wt%. In comparative four-stage crosscurrent experiments, PPG 400 achieved a higher final raffinate NaCl concentration (17.8 wt%) than Dehypon® LS54 (13.8 wt%). Using TIPS, for both polymers high recovery (>99.5%) was achieved at 80 wt% to 97 wt% polymer purity. TIPS was also proven to be an effective separation for the raffinate streams, reducing polymer contamination to as low as 0.3 wt% for PPG 400 and 0.04 wt% for Dehypon® LS54. The co-extracted salt in the extract yielded a secondary brine stream (1.3 wt% to 10.4 wt% NaCl) rather than clean water, showing that more sophisticated processing and/or downstream purification is necessary to obtain high quality potable water. This work elucidates the fundamental trade-offs between thermodynamic selectivity, solvent loss, and product purity that govern the design of LLX systems for brine concentration and valorization. • Multistage crosscurrent liquid-liquid extraction concentrates NaCl brines • Poly(propylene glycol) 400 (PPG 400) and Dehypon® LS54 were successfully applied • PPG 400 exhibits over 3 times higher water over NaCl selectivity than Dehypon® LS54 • Four-stage PPG 400 crosscurrent extraction concentrates from 7.0 to 17.8 wt% NaCl • Solvent regeneration via temperature induced phase separation is partly effective

Authors

Institutions

Publication Details

Journal
Desalination
Published
2026-01-19
DOI
https://doi.org/10.1016/j.desal.2026.119886
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.00

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Efficient salt recovery from aqueous streams using multistage liquid-liquid extraction with thermo-responsive polymers

Gerrald Bargeman, Boelo Schuur, Gabriela Pulido, Daniël Feddes
Desalination
Membrane Separation Technologies
article

Efficient salt recovery from aqueous streams using multistage liquid-liquid extraction with thermo-responsive polymers

Gerrald Bargeman, Boelo Schuur, Gabriela Pulido, Daniël Feddes
article en

Abstract

Liquid-liquid extraction (LLX) using thermo-responsive polymers is a promising low-energy alternative for concentrating hypersaline brines from reverse osmosis (RO). This study presents a comprehensive evaluation of a multistage crosscurrent LLX process, comparing poly(propylene glycol) 400 (PPG 400) and the nonionic surfactant Dehypon® LS54. The methodology includes determining liquid-liquid equilibrium (LLE) data, a theoretical graphical multistage countercurrent LLX analysis, four-stage crosscurrent batch experiments, solvent regeneration, and product purification via thermally induced phase separation (TIPS). LLE results revealed that PPG 400 possesses higher water over salt selectivity. Using ternary diagrams from LLE results, it was found that PPG 400 and Dehypon® LS54 require four and five theoretical stages, respectively, to increase the NaCl concentration from 7 to 20 wt%. In comparative four-stage crosscurrent experiments, PPG 400 achieved a higher final raffinate NaCl concentration (17.8 wt%) than Dehypon® LS54 (13.8 wt%). Using TIPS, for both polymers high recovery (>99.5%) was achieved at 80 wt% to 97 wt% polymer purity. TIPS was also proven to be an effective separation for the raffinate streams, reducing polymer contamination to as low as 0.3 wt% for PPG 400 and 0.04 wt% for Dehypon® LS54. The co-extracted salt in the extract yielded a secondary brine stream (1.3 wt% to 10.4 wt% NaCl) rather than clean water, showing that more sophisticated processing and/or downstream purification is necessary to obtain high quality potable water. This work elucidates the fundamental trade-offs between thermodynamic selectivity, solvent loss, and product purity that govern the design of LLX systems for brine concentration and valorization. • Multistage crosscurrent liquid-liquid extraction concentrates NaCl brines • Poly(propylene glycol) 400 (PPG 400) and Dehypon® LS54 were successfully applied • PPG 400 exhibits over 3 times higher water over NaCl selectivity than Dehypon® LS54 • Four-stage PPG 400 crosscurrent extraction concentrates from 7.0 to 17.8 wt% NaCl • Solvent regeneration via temperature induced phase separation is partly effective

DesalinationVol. 624
Thales (Netherlands) (NL), University of Twente (NL)
Topconsortium voor Kennis en Innovatie
Openalex Percentile: Top 85%
Membrane Separation Technologies
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.