Industrial Preparation Methods of Rhenium Metal

Abstract

Rhenium (Re), a high-melting-point rare metal, is primarily recovered from byproducts of copper-molybdenum smelting, flue dust, and spent catalysts. Industrial production relies on hydrometallurgical processes, including:

  • Chemical precipitation (selective sulfide separation for initial enrichment),
  • Solvent extraction (e.g., N235/TBP systems for efficient ReO₄⁻ separation),
  • Ion exchange (suitable for deep purification of low-concentration Re solutions).

Additional pyrometallurgical roasting activation is often employed for pre-treatment. High-purity rhenium (≥99.99%) is obtained via hydrogen reduction or electrolytic refining.


1. Rhenium Resources and Pre-Treatment

(1) Resource Types

  • Copper-molybdenum smelting byproducts: Rhenium accumulates as Re₂O₇ in flue dust or waste acid (0.001%–0.1% Re content).
  • Flue dust: Contains 0.05%–0.3% Re, often co-existing with molybdenum. Requires roasting (400–600°C) to convert to soluble Re₂O₇.
  • Spent catalysts: Platinum-rhenium catalysts contain 1%–5% Re, requiring acid/alkali leaching for extraction.

(2) Pre-Treatment Processes

  • Roasting activation: Converts refractory Re compounds (e.g., ReS₂ → Re₂O₇), increasing leaching efficiency to >95%.
  • Acid/alkali leaching:
    • Sulfuric acid (10%–20%) or NaOH (3–5 mol/L) selectively dissolves Re.
    • pH control minimizes co-dissolution of impurities.

2. Main Extraction Technologies

(1) Chemical Precipitation

  1. Sulfide Precipitation
    • Na₂S₂O₃ or Na₂S is added to form ReS₂ precipitate (Ksp = 2.4×10⁻¹⁰), achieving >99% Re recovery.
    • Limitations: Co-precipitation of As/Pb (As removal rate: ~47%), resulting in low-grade Re concentrate (0.8%–1.4%).
  2. Stepwise Precipitation Optimization
    • Pre-removal of Cu (99.7% CuS precipitation) before Re recovery, improving Re concentrate grade to 0.836%.

(2) Solvent Extraction

  1. Amine-Based Extraction (N235)
    • At pH 2–3, N235 selectively binds ReO₄⁻, achieving >99.4% recovery via three-stage countercurrent extraction.
    • Advantages: Direct processing of highly acidic waste (pH = -0.5); <20% Mo co-extraction.
  2. Phosphorus-Based Extraction (TBP)
    • High-acidity conditions (8 mol/L HCl) extract Re, with >99.9% purity after stripping.

(3) Ion Exchange

  1. Resin Adsorption
    • Strong-base anion resins (e.g., Dowex 1-X8) adsorb ReO₄⁻; elution with NaCl yields NaReO₄ (Re recovery >98%).
    • Best for: Low-concentration Re solutions (<100 ppm).

3. High-Purity Refining

(1) Hydrogen Reduction

  • Ammonium perrhenate (NH₄ReO₄) is reduced at 800°C under H₂, yielding ≥99.99% pure Re powder.

(2) Electrolytic Refining

  • Perrhenic acid solution is electrolyzed to deposit high-purity Re (oxygen content ≤50 ppm).

4. Industrial Challenges & Optimization

(1) Impurity Control

  • Key issue: Separation from As/Mo.
  • Solution: Selective chelating agents (e.g., thiourea derivatives) reduce co-extraction.

(2) Green Process Development

  • Ionic liquid extraction (e.g., [N₈₈₈₁][ReO₄]) replaces toxic organic solvents.

Conclusion

Rhenium production requires tailored “leaching-enrichment-purification” processes based on feedstock characteristics. Future trends focus on:

  • High-selectivity separation (e.g., molecular recognition extraction),
  • Low-carbon metallurgy,
    to meet aerospace superalloy demands for ultra-high-purity Re (≥99.995%).

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