A Malaysian Study Maps the Hardest Step in Rare Earth Processing—and Why China Still Holds the Leverage Midstream

Feb 9, 2026

Highlights

  • Malaysian researchers modeled a four-train solvent extraction process to separate praseodymium and neodymium to 99.99% purity from ion-adsorbed clay.
  • The process reveals that Pr/Nd separation alone requires 62 equilibrium stages and dominates plant footprint and capital costs.
  • The study explains why China controls downstream rare earth markets: the chemically adjacent Pr and Nd have a low separation factor (β ≈ 1.70), requiring massive, capital-intensive facilities that most non-Chinese producers cannot economically replicate.
  • High-purity Pr and Nd are essential for NdFeB permanent magnets in electric vehicles, wind turbines, and defense systems.
  • This simulation-based design demonstrates that any ex-China rare earth strategy must accept either large-scale infrastructure investment or continued supply dependence.

A Malaysian research team led by Norazihan Zulkifli of Universiti Malaysia Kelantan (opens in a new tab), working with collaborators from Universiti Sains Malaysia and Universiti Islam Antarabangsa Malaysia (opens in a new tab), has published a detailed engineering study that confronts one of the most difficult bottlenecks in the rare earth supply chain: separating praseodymium (Pr) from neodymium (Nd) to ultra-high purity. Published in Kompleksnoe Ispolzovanie Mineralnogo Syra = Complex Use of Mineral Resources (Vol. 342, No. 3), the paper presents a four-train, counter-current solvent extraction (SX) flowsheet designed to achieve 4N (99.99%) purity Pr and Nd from ion-adsorbed clay (IAC)–derived chloride liquor sourced from Malaysia’s Jeli deposit. The central conclusion is blunt and instructive: Pr/Nd separation dominates plant footprint, capital intensity, and technical complexity, helping explain why China—having mastered this step at scale—continues to control downstream rare earth markets.

Study Design and Methods

Rather than lab experimentation, the authors used steady-state mass-balance simulations—implemented in Microsoft Excel, a standard tool in hydrometallurgical design—to model an industrial SX circuit. The simulated feed was a pre-treated REE chloride solution, and the extractant was P507, a commercially established phosphonic acid reagent.

The proposed flowsheet is organized into four sequential SX trains:

  1. a bulk light/heavy rare earth (LREE/HREE) split, (2–3) intermediate fractionation stages, and
  2. The final Pr/Nd separation circuit.

Key design variables included A/B cut points between elements and organic-to-aqueous (O/A) ratios across each cascade.

Key Findings

The simulations identify Pr/Nd separation as the dominant bottleneck. Because the two elements are chemically adjacent, the separation factor (β ≈ 1.70) is low, requiring approximately 62 equilibrium stages to reach 4N purity. By contrast, earlier bulk separations require as few as ~16 stages. The study confirms theoretical minimum stage counts (Nmin) and provides stage-by-stage concentration profiles, offering designers a rare level of practical detail.

Bottom line: the Pr/Nd circuit dictates plant size and cost. This is the dividing line between ore production and magnet-grade materials—and the true source of China’s competitive edge.

Why this Matters Beyond Malaysia

High-purity Pr and Nd are critical inputs for NdFeB permanent magnets, which underpin electric vehicles, wind turbines, robotics, and defense systems. The study shows that non-Chinese resources can be processed to commercial purity, but only through large, highly engineered, and capital-intensive SX plants. This reality explains why many countries with upstream resources remain dependent on China for refined outputs.

Limitations & Open Questions

This is a simulation-based design study, not a pilot-plant demonstration. It assumes stable feed chemistry and idealized stage efficiencies, and it does not fully quantify operating costs, reagent losses, waste management, or environmental permitting challenges. IAC resources also raise well-known sustainability concerns. Still, the methodology reflects real industry practice, and the conclusions are technically credible.

REEx Takeaway

This paper does not promise a shortcut. It explains why no shortcut exists. China’s advantage lies not in geology but in process engineering at scale, particularly for Pr/Nd separation. Any serious ex-China strategy must plan for dozens of stages, large footprints, and significant capital—or accept continued dependence.

Citation: Zulkifli, N., Shoparwe, N., Yusoff, A.H., Abdullah, A.Z., & Ahmad, M.N. (2026). Flowsheet Design and Modelling for High Purity Praseodymium and Neodymium by Solvent Extraction. Complex Use of Mineral Resources, 342(3), 111–122. https://doi.org/10.31643/2027/6445.35 (opens in a new tab)

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By Daniel

Inspired to launch Rare Earth Exchanges in part due to his lifelong passion for geology and mineralogy, and patriotism, to ensure America and free market economies develop their own rare earth and critical mineral supply chains.

3 Comments

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yusoff123

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Malaysian study reveals praseodymium neodymium separation requires 62 stages to reach 99.99% purity, explaining China's dominance in magnet materials. (

Hi, I’m Hafidz Yusoff, a lecturer from Universiti Malaysia Kelantan and one of the authors of this paper. The main author is Norazihan Zulkifli, who is also a member of our team, not Intan Norhani. Intan Norhani is not an author of this paper. It appears that the wrong name was cited. Please refer to and reflect the full and correct name (Norazihan Zulkifli) in the paper you referenced and make the necessary amendment.

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John

Administrator

480 messages 401 likes

Hi @yusoff123

I have asked the team to amend. If it hasn't been updated in the next 24 hours. Please email me direct at john@rareearthexchanges.com

Sorry for the mix up.

John

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Les Confer

New member

7 messages 4 likes

I opened the link provided and read the technical study itself. It made me recall the attached U. of Idaho 2016 Master's thesis by Kevin Lyon. Kevin actually tested his Matlab modeling with confirming SX extraction experiments (on Idaho National Laboratory's 32-stage bench scale mixer-settler system) and you will see they were very close. If you go to his Fig. 15, you will see that he also predicts 50 to 60+ stages to achieve the Nd-4N purification. But this Fig. 15 also shows that downstream users should be very sure they are not over specifying the purity that they require for their application (in order to avoid a premium price):
with just 12 stages the Nd was 99.04% pure
with 20 stages the Nd had improved to 99.53% pure
with 30 stages the Nd had purified to 99.93%
with 40 stages the Nd had purified to 99.89%
with 50 stages the Nd had purified to 99.94%

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