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Solvent Extraction for Rare-Earth Separation

1940
  • Frank Spedding
Laboratory solvent extraction setup for rare-earth element separation in chemical engineering.

(generated image for illustration only)

Separating chemically similar rare-earth elements is notoriously difficult. The primary industrial method is solvent extraction, specifically liquid-liquid counter-current extraction. This process exploits subtle differences in the partition coefficients of rare-earth ions between an aqueous phase and an immiscible organic phase containing a complexing agent. By repeating the process over hundreds of stages, high-purity individual elements can be isolated.

The process relies on the principle of differential partitioning. The rare-earth elements, typically as trivalent ions (\(RE^{3+}\)) in an acidic aqueous solution, are brought into contact with an organic solvent (like kerosene) containing an extractant. Common extractants include organophosphorus compounds like tributyl phosphate (TBP) or di-(2-ethylhexyl)phosphoric acid (D2EHPA). The extractant forms a complex with the rare-earth ions, making them soluble in the organic phase. Due to the lanthanide contraction, the stability of these complexes, and thus their tendency to move into the organic phase, varies slightly across the series. Lighter lanthanides (like lanthanum) are more basic and prefer the aqueous phase, while heavier lanthanides (like lutetium) are more acidic and have a greater affinity for the organic extractant.

In a counter-current system, the aqueous and organic phases flow in opposite directions through a series of stages (mixer-settlers). At each stage, the elements re-distribute themselves between the two phases according to their partition coefficient. This multi-stage cascade amplifies the small single-stage separation factor, allowing for the eventual separation of adjacent rare-earth elements to purities exceeding 99.99%. The choice of extractant, pH of the aqueous phase, and temperature are critical parameters that are carefully controlled to optimize the separation for specific elements. This method replaced the earlier, far more laborious fractional crystallization techniques and enabled the large-scale production of rare earths needed for modern technology.

UNESCO Nomenclature: 3305
– Chemical engineering

Type

Chemical Process

Disruption

Substancial

Usage

Widespread Use

Precursors

  • discovery of immiscible liquids
  • Nernst’s distribution law describing partitioning
  • development of fractional crystallization, an earlier, less efficient separation method
  • synthesis of organic complexing agents
  • advances in chemical engineering principles for multi-stage processes

Applications

  • industrial-scale production of high-purity rare-earth elements
  • nuclear reprocessing to separate actinides like plutonium and uranium from fission products
  • hydrometallurgy for extracting metals like cobalt and nickel
  • purification of specialty chemicals and pharmaceuticals

Patents:

NA

Potential Innovations Ideas

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Related to: solvent extraction, rare-earth separation, liquid-liquid extraction, hydrometallurgy, Ames laboratory, frank spedding, lanthanides, partition coefficient, mixer-settler, d2ehpa.

Historical Context

Solvent Extraction for Rare-Earth Separation

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1945-01-01
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1950

(if date is unknown or not relevant, e.g. "fluid mechanics", a rounded estimation of its notable emergence is provided)

Related Invention, Innovation & Technical Principles

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