Thorium Valorization at the Interface of Technology, Risk, and Sustainability
Abstract
1. Introduction
2. Sources and Occurrence of Thorium in Natural and Technological Systems
3. Thorium Extraction and Separation Technologies: A Critical Assessment
3.1. Conventional Hydrometallurgical Approaches
3.2. Advanced and Emerging Technologies
3.3. Scalability and Waste Challenges in Thorium Extraction
4. Environmental Behavior and Speciation of Thorium
5. Toxicological Effects and Human Health Implications
5.1. Thorium Exposure, Bioavailability, and Occupational Risk
5.2. Molecular Mechanisms of Thorium Toxicity
6. Integrating Valorization and Risk: Technological Trade-Offs and Knowledge Gaps
| Process/Material | Type of Process | Key Performance | Scalability & Limitations | References |
|---|---|---|---|---|
| Activated carbon (avocado seeds) | Adsorbent | 97.3% Th(IV) removal; 73 mg·g−1 capacity; 94% uptake in 5 min | Partial regeneration (70.5%), lab-scale; industrial scaling requires optimization | [125] |
| MOFs (SZ-7 zirconium phosphonate) | Adsorbent | Near-quantitative Th(IV) capture from acidic wastewater (pH < 2) | Exceptional acid stability; regeneration and long-term scaling unknown | [77] |
| Polyethylenimine-functionalized graphene oxide | Adsorbent | 38.17 mg·g−1 capacity; SF > 100 | High selectivity and recyclability; industrial deployment limited by synthesis and scale | [215] |
| Polycinnamic acid resin | Adsorbent | Selective Th(IV) removal from REE solutions | Requires precise polymer synthesis; large-scale production uncertain | [87] |
| TOPO/XAD-7 resin | Resin/Solid-phase extractor | 59.79 mg·g−1 capacity; >99.5% recovery in dynamic columns | High acid and radiation tolerance; scale-up requires consideration of competing ions | [216] |
| N,O-donor hybrid heterocyclic extractants | Solvent/Extractant | >90% Th(IV) recovery; SF 50–110 | Effective under controlled HNO3; multi-step stripping needed; scale-up challenges | [217] |
| Deep eutectic solvents (2-hexyldecanoic acid-based) | Solvent/Green extractant | >98% Th extraction; SF > 1000 vs. REEs | Lab-scale; long-term stability, radiolytic resistance, and industrial scalability unresolved | [200] |
| HCl multi-step leaching (Longnan, China) | Acid leaching | ~99% Th leaching; >98% REE recovery | Reduces acid consumption; secondary waste management and extractant sustainability need evaluation | [43] |
| Alkaline fusion (ThO2 from monazite) | Alkaline/Conventional process | ROI 21.92% at 1 t batch; payback 4.56 years | High capital for large batch; sensitive to raw material cost and reaction time | [74] |
| Monazite processing (Korea, eco-friendly) | Conventional/Integrated REE-Th-U | Th and U recovery with REEs; payback ~4.5 y | Operational cost dominated by materials/reagents; market-dependent | [61] |
7. Future Research Directions and a Framework for Sustainable Thorium Management
- Supportive Policy and Governance: Regulatory frameworks, extended producer responsibilities, material tracking, and green incentives that guide and facilitate the circular management of thorium [222].
8. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Abbreviations
| ACE | Activated carbon electrodes |
| COFs | Covalent organic frameworks |
| DMHMP | Di(1-methyl-heptyl) methyl phosphonate |
| GBE | Graphene-based electrodes |
| g-C3N4 | Graphitic carbon nitride |
| GF-AO | Amidoxime-modified graphite felt |
| H2SO4 | Sulfuric acid |
| HCl | Hydrochloric acid |
| HNO3 | Nitric acid |
| LCA | Life cycle assessment |
| MOFs | Metal–organic frameworks |
| NORM | Naturally occurring radioactive materials |
| REE | Rare earth element |
| TBP | Tributyl phosphate |
| TEA | Techno-economic analysis |
| Th | Thorium |
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| Separation Method for Thorium | Key Technical Advantages | Major Limitations/Challenges | Technology Maturity and Key Evidence | References |
|---|---|---|---|---|
| Acid leaching (H2SO4, HCl, HNO3) | High thorium dissolution efficiency from monazite; well-integrated into conventional rare earth processing flowsheets. | Generation of large volumes of acidic, radioactive waste; high reagent consumption and corrosion issues. | Commercial process. Subject of recent techno-economic evaluations for integrated industrial flowsheets | [61,72,79] |
| Alkaline leaching/fusion (NaOH, KOH) | Provides improved control over thorium separation; can reduce co-dissolution of rare earths compared to some acid routes. | High energy input required; generates alkaline waste that needs neutralization. | Commercial process (conditional). Economically evaluated for ThO2 production. | [74,75] |
| Solvent extraction (TBP, D2EHPA, etc.) | High selectivity and efficiency for Th/RE separation; proven in scalable, multi-stage contactor systems (e.g., mixer-settlers). | Generates organic secondary waste; risks of solvent degradation and crud formation; requires rigorous safety protocols. | Commercial unit operation. Solvent extraction circuits are designed and optimized for “nuclear industry applications”. | [71,103,122] |
| Ion-exchange resins | Highly effective for polishing and recovering thorium from dilute or low-concentration streams (e.g., wastewater). | Limited kinetic rates and adsorption capacity; generates secondary waste from resin regeneration. | Pilot-scale/auxiliary. Primarily demonstrated at laboratory scale for separation from complex sulfate media. | [103] |
| Advanced solid adsorbents—MOFs, COFs, functional polymers | Exceptional selectivity and high adsorption capacity under controlled laboratory conditions. | Complex and costly synthesis; performance often degrades in complex, real matrices; challenges with material stability and recycling. | Fundamental research. Novel materials described for “selective extraction” in batch lab studies. | [93,95,106,107] |
| Membrane-based processes | Potential for continuous, low-chemical-input operation with a small footprint. | Susceptibility to fouling and scaling; low throughput; limited long-term stability data for radioactive feeds. | Emerging technology (pilot-concept). Systems like “continuous-flow electrosorption” are “advancing towards technology readiness”. | [85,123] |
| Bio-hydrometallurgy (bioleaching, biosorption) | Low energy and chemical consumption in principle; potential for processing low-grade or secondary resources. | Very slow kinetics; sensitive to environmental conditions; poor reproducibility and control at larger scales. | Early-stage research. Reviewed as a “sustainable approach” with focus on “future prospects” rather than current application. | [99,101,121] |
| Electrosorption/electrochemical recovery | Electric-field-assisted adsorption enhances thorium uptake, selectivity, and reusability; reduces chemical use; compatible with renewable energy. | Limited electrode stability and availability; low throughput; sensitive to competing ions; lab-scale demonstration | Emerging technology. High lab-scale recovery (>3000 mg·g−1 GF-AO; ~124 mg·g−1 g-C3N4); industrial scale-up not yet validated | [31,90,110] |
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Man, G.T.; Iordache, A.M.; Popescu, D.I.; Zgavarogea, I.R.; Șuțan, N.A. Thorium Valorization at the Interface of Technology, Risk, and Sustainability. Toxics 2026, 14, 193. https://doi.org/10.3390/toxics14030193
Man GT, Iordache AM, Popescu DI, Zgavarogea IR, Șuțan NA. Thorium Valorization at the Interface of Technology, Risk, and Sustainability. Toxics. 2026; 14(3):193. https://doi.org/10.3390/toxics14030193
Chicago/Turabian StyleMan, Geani Teodor, Andreea Maria Iordache, Diana Ionela Popescu (Stegarus), Ionela Ramona Zgavarogea, and Nicoleta Anca Șuțan. 2026. "Thorium Valorization at the Interface of Technology, Risk, and Sustainability" Toxics 14, no. 3: 193. https://doi.org/10.3390/toxics14030193
APA StyleMan, G. T., Iordache, A. M., Popescu, D. I., Zgavarogea, I. R., & Șuțan, N. A. (2026). Thorium Valorization at the Interface of Technology, Risk, and Sustainability. Toxics, 14(3), 193. https://doi.org/10.3390/toxics14030193

