Separation

DEco grade
Midstream18 facilities tracked

Solvent extraction (SX) and ion-exchange processes that isolate individual rare earth elements from mixed feedstocks into high-purity oxides. The most technically demanding and geopolitically sensitive step in the value chain.

Covers traditional solvent extraction (SX), Advanced Column extraction (RapidSX™ by Ucore Rare Metals), membrane solvent extraction (MSX), and ion-exchange chromatography - the four principal technologies used to separate mixed rare earth chlorides into individual oxides for use in magnets, catalysts, and batteries.

Where does the mass go?

Material flow balance — per 100 t mixed REE chloride feed

FeedstockChemical InputProcessValuable OutputBy-productWaste / Emissions

Critical Ratio

Only ~20% of feed mass becomes NdPr oxide - but the organic phase (kerosene + P507) must be continuously recycled or the plant becomes uneconomic

Ratings

Capital Outlay$$$$ Critical
Technical DifficultyVery High
Geopolitical SensitivityExtreme
Energy Intensity⚡⚡⚡ High
Environmental Footprint🍂 D - High impact
Value Add3x-5x
Technical MoatExtreme

Material Flow

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

Key Reagents / Inputs

  • D2EHPA
  • PC88A
  • Organic extractants
  • Hydrochloric acid
  • Ammonia
  • Magnesia
  • Ammonium Hydroxide

Waste Outputs

  • Spent organic solvent
  • Ammonium chloride wastewater
  • Acid/alkali strip solutions
  • Low-level radioactive residues

The Duel: Traditional vs Next-Gen

Same NdPr oxide output, dramatically different resource footprint. Values are per 100 t of mixed REE chloride feed.

Traditional SX

~80% of global capacity

D
Organic Solvent
80 t / 100 t feedbaseline
Raffinate Discharge
150 t / 100 t feedbaseline
Physical Footprint
10,000 baseline
Cycle Time
12 days (approx.)baseline

Advanced Column (RapidSX™)

Commercial demo · 2026

B+
Organic Solvent
20 t / 100 t feed−75%
Raffinate Discharge
40 t / 100 t feed−73%
Physical Footprint
2,500 −75%
Cycle Time
1 days (approx.)−92%

Membrane SX

Pilot · early commercial

A-
Organic Solvent
10 t / 100 t feed−87%
Raffinate Discharge
20 t / 100 t feed−87%
Physical Footprint
3,000 −70%
Cycle Time
3 days (approx.)−75%

Explore Each Technology

Switch between technologies to see how the mass-flow Sankey changes.

Where does the mass go?

Material flow balance — per 100 t mixed REE chloride feed

FeedstockChemical InputProcessValuable OutputBy-productWaste / Emissions

Critical Ratio

Only ~20% of feed mass becomes NdPr oxide - but the organic phase (kerosene + P507) must be continuously recycled or the plant becomes uneconomic

Technology Metrics at a Glance

MetricTraditional SXAdvanced Column (RapidSX™)Membrane SX
Separation Time10-14 days~24 hours2-5 days
Physical Footprint~10,000 m²~2,500 m²~3,000 m²
Organic Solvent Vol.Very High (80 t / 100 t)Low (20 t / 100 t)Minimal (10 t / 100 t)
Raffinate DischargeVery High (~150 t)Moderate (~40 t)Low (~20 t, treated)
ESG RatingDB+A-
Capital IntensityMediumHighVery High
Separation Stages200-500 stages20-50 stagesContinuous pore contact
Market MaturityMature (70+ yrs)Commercial demo (2026)Pilot / Early commercial
Western IP DependencyHigh (Chinese chemistry)Low (Ucore / USA IP)Low (European IP)

Facilities by Processing Technology

Tracked facilities grouped by their confirmed processing method.