4.6 Article

Separation of Rare-Earth Elements Using Supported Liquid Membrane Extraction in Pilot Scale

Journal

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Volume 61, Issue 50, Pages 18475-18491

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.2c03268

Keywords

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Funding

  1. Swedish Foundation for Strategic Research SSF
  2. [IRT 11-0026]

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This study investigates the use of supported liquid membrane extraction for the recovery and separation of rare-earth elements (REEs). The experiments compare different configurations and conditions to examine the performance of the liquid membrane. The results show that the membrane has higher selectivity towards heavy REEs and different configurations exhibit different transport rates and selectivity. The HFRLM and EPT configurations demonstrate more stable performance and provide feasible options for processing REE liquors.
The use of supported liquid membrane extraction for recovery and separation of rare-earth elements (REEs) has been investigated. Experiments have been carried out using the different configurations: (1) standard hollow fiber supported liquid membrane operation (HFSLM), (2) renewal liquid membrane operation (HFRLM), and (3) emulsion pertraction technology (EPT). The experiments were performed in pilot scale using a hollow fiber module with a mass transfer surface area of 8 m2. Synthetic feed solution was used with compositions based on a process for recovery of REE from an apatite concentrate. The total concentration of REE in the feed was varied from 1 to 22 mM REE and the pH was varied in the range 1.5-3.2. Di(2-ethylhexyl) phosphoric acid (D2HEPA) diluted in kerosene, 10% (v/v), was used as the organic membrane solution, and 3 M HCl was used as stripping solution. In supported liquid membrane extraction, the extraction performance is governed by both the kinetics of REE transport through the membrane and by thermodynamics. The effect of feed composition on the selectivity and transport of REE through the liquid membrane have been investigated. The results show that the liquid membrane is more selective toward the heavy REE at lower pH values and higher REE concentration. HFRLM shows a higher transport rate than HFSLM, while the HFSLM configuration gives a higher selectivity toward individual REE. The membrane performance in HFSLM configuration rapidly decays with time, while in the HFRLM and EPT configurations, the performance is much more stable. Possible mechanisms for decaying membrane performance are discussed, and gel formation is identified as being of significant importance. Gel formation is observed at an organic loading above similar to 46% for Nd, 38% for Y, 46% for Dy, and 65% for Er. The work performed in this study serves as an initial step to demonstrate that HFRLM and EPT can provide stable operation and be feasible options for processing of REE liquors. A process flow diagram for the recovery of the REE, present in the apatite concentrate, in three fractions is proposed based on the results from this study.

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