Separation (Membrane)

AEco grade
Midstream2 facilities tracked

Next-generation enclosed-system separation using hydrophobic membrane contactors (e.g. Carester MSX) or ion-exchange chromatography (e.g. Energy Fuels). Organic solvent is confined within the membrane pore structure with near-zero open-tank exposure, eliminating raffinate discharge ponds and cutting solvent inventory to ~10 t per 100 t feed. Best-in-class ESG profile among all separation routes.

Where does the mass go?

Material flow balance — per 100 t mixed REE chloride feed — Membrane SX (MSX)

FeedstockChemical InputProcessValuable OutputBy-productWaste / Emissions

Critical Ratio

Membrane SX keeps extractant locked inside hydrophobic membrane pores — eliminating open-tank solvent exposure and cutting raffinate to ~13% of the conventional volume

Ratings

Capital Outlay Very High
Technical DifficultyVery High
Geopolitical SensitivityMedium
Energy Intensity⚡⚡ Medium
Environmental Footprint🍃🍃🍃 A - Lowest environmental impact
Value Add3x-5x
Technical MoatVery High

Material Flow

INMREC / Mixed Chlorides / Sulphate Leachate
OUTHigh-Purity REE Oxides (>99.9%)

Key Reagents / Inputs

  • Selective membrane extractants
  • Hydrochloric acid (strip)
  • Ion-exchange resin (IEX route)

Waste Outputs

  • Minimal treated raffinate
  • Spent IEX resin (IEX route)
  • Membrane cleaning effluent
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Technical Moat

Very High

The moat is Membrane Materials Science and System Integration. Fabricating membranes that maintain selectivity and flux under continuous industrial REE chemistry without fouling or degradation is a deep materials engineering challenge. European IP (Carester) and US DoE-funded IEX programmes hold the leading positions outside China.