Informing Ion-Exchange\nMembrane Design Targets for\nDonnan Dialysis-Mediated Lithium Brine Concentration

We assess the potential of a Donnan dialysis (DD) process\nfor lithium\nbrine concentration and prioritize material design opportunities from\na use-informed perspective. Bench-scale batch experiments were used\nto validate a kinetic process model, achieving lithium concentration\nfactors of 7.6–18.9× and recoveries of 22–74% for\nvarying dilute lithium feed streams and operating conditions. The\ncorresponding process model was used to assess DD performance for\ncontinuous pilot-scale concentrations of a representative lithium\nextraction eluate stream. Model outputs demonstrate that DD achieves\ncomparable lithium concentration and recovery targets with similar\nor lower membrane area requirements compared to reverse osmosis and\nelectrodialysis processes, respectively. A sensitivity analysis reveals\nthe relative importance of key parameters in ion-exchange membrane\ndesign for improving DD performance (water content > charge content\n≈ membrane thickness ≈ water permeability). The development\nof alkaline- and scaling-resistant cation exchange membranes has also\nbeen identified as a target material improvement to expand the solution\ncompatibility limits of the DD process.

Publication Details

Journal
Figshare
Published
2024-12-23
DOI
https://doi.org/10.1021/acs.iecr.4c03482.s001
Primary Topic
Membrane-based Ion Separation Techniques
Type
article
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article

Informing Ion-Exchange\nMembrane Design Targets for\nDonnan Dialysis-Mediated Lithium Brine Concentration

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Membrane-based Ion Separation Techniques
article

Informing Ion-Exchange\nMembrane Design Targets for\nDonnan Dialysis-Mediated Lithium Brine Concentration

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Abstract

We assess the potential of a Donnan dialysis (DD) process\nfor lithium\nbrine concentration and prioritize material design opportunities from\na use-informed perspective. Bench-scale batch experiments were used\nto validate a kinetic process model, achieving lithium concentration\nfactors of 7.6–18.9× and recoveries of 22–74% for\nvarying dilute lithium feed streams and operating conditions. The\ncorresponding process model was used to assess DD performance for\ncontinuous pilot-scale concentrations of a representative lithium\nextraction eluate stream. Model outputs demonstrate that DD achieves\ncomparable lithium concentration and recovery targets with similar\nor lower membrane area requirements compared to reverse osmosis and\nelectrodialysis processes, respectively. A sensitivity analysis reveals\nthe relative importance of key parameters in ion-exchange membrane\ndesign for improving DD performance (water content > charge content\n≈ membrane thickness ≈ water permeability). The development\nof alkaline- and scaling-resistant cation exchange membranes has also\nbeen identified as a target material improvement to expand the solution\ncompatibility limits of the DD process.

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Membrane-based Ion Separation Techniques
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