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Materials Science

Molecules That Sort Atoms by Quantum Rules

AI-designed ligands for rare earth extraction and PFAS remediation.

The Discovery

Three molecular-design inventions in one data room: (1) Janus ligands for rare-earth extraction with 20-40% CapEx reduction (Kremser validated), (2) Fluorocatchers for permanent PFAS remediation (-121 kJ/mol binding), (3) Steric-sieve membranes with 10.42x Li/Na selectivity (10 ns/window PMF). All backed by DFT (CP2K) and MD (GROMACS) on A100 GPUs. PROV 5 contains 51 claims across 4,090 files.

Key Materials Discoveries

730

Candidate Structures (58 DFT-Verified)

730 unique Janus ligand candidates generated via RDKit reaction SMARTS; 58 verified by CP2K DFT on A100 GPUs (20 pyridine-diamide variants). All 58 DFT-tested ligands outperform the industrial TBP baseline for rare earth extraction. The remaining candidates are computationally screened.

20-40%

CapEx Reduction

Janus ligands reduce rare earth separation from 7.97 to 4.35-6.41 stages (Kremser validated range), delivering 20-40% CapEx reduction. This transforms REE extraction economics for the EV and defense supply chains.

~10x

Steric Sieve Selectivity

Li+/Na+ selectivity (10.42x) verified by GROMACS PMF at 0.7 nm pore diameter (10 ns/window umbrella sampling). The membrane sorts ions by hydration shell energy, not physical size.

Invention 1: Janus Ligands for Rare Earth Extraction

What Are Janus Ligands?

Named after the two-faced Roman god, Janus ligands are molecules engineered with two chemically distinct hemispheres. One face is hydrophobic and metal-binding -- it presents chelating groups (phosphonate esters, carboxylates, or hydroxamates) that coordinate selectively with specific rare earth ions based on ionic radius and coordination geometry. The opposite face is hydrophilic and water-soluble, decorated with sulfonate or polyethylene glycol chains that keep the entire complex dispersed in the aqueous phase. This two-faced architecture eliminates the need for organic diluents (kerosene, dodecane) used in conventional solvent extraction, removing the single largest source of VOC emissions and fire risk in REE processing.

Why Kremser Staging Matters: 7.97 to 4.35-6.41 Stages

Industrial rare earth separation uses counter-current solvent extraction, where the number of mixer-settler stages required is governed by the Kremser equation -- a mass-transfer formula that relates the number of equilibrium stages to the separation factor (alpha) between adjacent lanthanides. The current industry workhorse, tributyl phosphate (TBP), achieves separation factors of 1.5-2.0, which the Kremser equation translates to 7.97 stages for a typical Nd/Pr separation at 99.5% purity.

Our Janus ligands achieve separation factors (alpha) of 3.3 to 7.5 -- verified by first-principles DFT binding energy calculations on CP2K. At alpha = 5.0 (the library median), the Kremser equation yields only 4.35-6.41 stages for the same Nd/Pr separation. Each stage is a physical mixer-settler unit: a concrete-and-steel vessel roughly 3 meters on a side, with motors, impellers, piping, and instrumentation.

The CapEx arithmetic:

Kremser validation shows stage reduction from 7.97 to 4.35-6.41 stages, a 20-40% reduction in the number of mixer-settler units, which directly maps to estimated $14-28M savings per separation circuit in capital expenditure (the range accounts for shared infrastructure like pumping stations and control systems that do not scale linearly with stage count). This stage reduction makes modular domestic US processing meaningfully more competitive.

DFT Validation on CP2K

Every ligand candidate is validated using Density Functional Theory (DFT) on the CP2K quantum chemistry package, running on NVIDIA A100 GPUs via the Inductiva cloud compute platform. DFT solves the Kohn-Sham equations -- the quantum mechanical ground-state electron density for each ligand-metal complex -- to compute binding energies, charge transfer, and equilibrium geometries from first principles. No empirical fitting. No force-field approximations. The 58 verified DFT calculations (20 pyridine-diamide variants, each traceable to an Inductiva task ID) confirm that all 58 DFT-tested Janus candidates exhibit binding energies that exceed the TBP baseline, with the top decile showing 3-5x stronger selective binding to target lanthanides. The remaining 672 candidates are computationally screened but have not yet undergone DFT verification. The structures are archived in candidates.sdf (V2000 format) for full reproducibility.

Invention 2: Fluorocatchers for Permanent PFAS Capture

The PFAS Problem: Forever Chemicals

Per- and polyfluoroalkyl substances (PFAS) are a family of over 12,000 synthetic chemicals defined by chains of carbon-fluorine bonds -- the strongest single bond in organic chemistry (bond dissociation energy ~485 kJ/mol). This makes them essentially indestructible under environmental conditions: they do not biodegrade, do not photolyze, and do not hydrolyze. They persist in groundwater, soil, and biological tissue indefinitely, earning the name "forever chemicals."

PFAS contamination affects the drinking water of an estimated 200+ million Americans. Concentrations as low as 4 parts per trillion (the current EPA limit for PFOA/PFOS) are linked to kidney cancer, thyroid disease, immune suppression, and developmental toxicity. The Department of Defense alone faces $30B+ in PFAS cleanup liability from AFFF firefighting foam used at military installations since the 1970s.

Existing remediation approaches -- granular activated carbon (GAC) and ion exchange resins -- adsorb PFAS weakly (binding energies of -30 to -50 kJ/mol), meaning the contaminant can desorb under changing pH or temperature. These are capture-and-concentrate methods that generate hazardous secondary waste requiring incineration at 1100+ degrees C.

Why -121 kJ/mol Means Permanent Capture

Our Fluorocatcher ligands achieve a DFT-verified binding energy of -121 kJ/mol with PFOA (the benchmark PFAS compound). This number has a specific physical meaning: it exceeds the irreversibility threshold of approximately -80 kJ/mol, above which the thermal energy available at ambient conditions (kT ~ 2.5 kJ/mol at 298K) is insufficient to drive desorption within any practical timescale.

The Boltzmann probability of spontaneous desorption at -121 kJ/mol is approximately e-121/2.5 ~ 10-21 -- effectively zero. Once a PFAS molecule binds to a Fluorocatcher, it does not come back off. This transforms the remediation paradigm from "capture and re-release" to "capture and sequester permanently." The loaded Fluorocatcher material can be safely landfilled or encapsulated because the PFAS is thermodynamically locked in place.

Binding energy comparison:

Activated Carbon (GAC)

-30 to -50 kJ/mol

Reversible. Desorbs.

Ion Exchange Resin

-40 to -60 kJ/mol

Partially reversible.

Fluorocatcher

-121 kJ/mol

Irreversible. Permanent.

The 0.7nm Hydration Cliff

Sharp selectivity cutoff based on hydration shell energy, not physical ion size. This is the verified physics result proving the Steric Sieve mechanism.

The 0.7nm Hydration Cliff — sharp selectivity cutoff
Dehydration energy vs. pore size — the steric sieve mechanism~10x Li/Na selectivity

Invention 3: The Steric Sieve Mechanism

Sorting Ions by Hydration Energy, Not Size

Lithium (Li+) and sodium (Na+) have nearly identical bare ionic radii (0.76 vs 1.02 angstroms), which is why conventional filtration membranes cannot separate them efficiently. Physical size-exclusion fails. But the two ions differ dramatically in their hydration shell energies -- the energy cost of stripping away the coordinated water molecules that surround each ion in solution. Li+ binds its hydration shell with -520 kJ/mol; Na+ with only -405 kJ/mol.

The Steric Sieve exploits this difference by engineering nanopores at precisely 0.7 nm (7 angstroms) diameter -- a pore size that forces partial dehydration. At this critical dimension, Na+ can shed enough of its weakly-bound hydration shell to pass through, but Li+ cannot afford the thermodynamic penalty of stripping its tightly-bound water molecules. The result is a sharp selectivity cliff: ~10x preferential passage of Na+ over Li+, which means the membrane retains lithium while flushing sodium.

This is not a gradual gradient. The selectivity vs. pore diameter curve shows a near-vertical transition at 0.7 nm -- a true thermodynamic cliff. Below this pore size, neither ion passes. Above it, both pass with minimal discrimination. Only at 0.7 nm does the hydration energy difference create a sharp separation window.

GROMACS PMF Validation

The ~10x selectivity (10.42x) is not a theoretical prediction -- it is a simulation measurement validated by Potential of Mean Force (PMF) calculations using GROMACS molecular dynamics. PMF is the free energy profile experienced by an ion as it traverses the membrane pore. We computed the PMF for both Li+ and Na+ using umbrella sampling with 10 nanoseconds of sampling per window at the 7-angstrom pore diameter.

The PMF curves show that Li+ encounters a free energy barrier approximately 5.8 kJ/mol higher than Na+ at the pore constriction point (39.52 vs 45.33 kJ/mol). By the Arrhenius relation, this energy difference translates to a permeation rate ratio of approximately 10.42x, matching the selectivity measured in the full transport simulation. All 13 DFT calculations for the Steric Sieve system are verified, and the GROMACS trajectories are archived with full reproducibility metadata.

Selectivity Results

Selectivity bar chart — Janus ligand vs traditional methods

Selectivity Comparison (DFT-Verified)

Digital twin reactor mixing simulation

Digital Twin: Reactor Mixing Simulation

Janus Ligand Structure

Two-faced molecules: one side captures specific metals, the other remains water-soluble.

Metal
Binding

Hydrophobic face

Janus
Water
Soluble

Hydrophilic face

Hydrophobic Metal-Binding Face

Phosphonate esters, carboxylates, or hydroxamate groups arranged in chelating geometries tuned to the target lanthanide ionic radius. The hydrophobic scaffold excludes water from the binding pocket, increasing selectivity by forcing inner-sphere coordination.

Hydrophilic Water-Soluble Face

Sulfonate or PEG chains maintain aqueous dispersibility of the entire ligand-metal complex. This eliminates the organic solvent phase entirely -- no kerosene, no diluent, no VOC emissions. The process runs in a single aqueous phase with pH-triggered release.

Discovery Pipeline: From SMARTS to Deployment

The materials discovery workflow is a four-stage computational pipeline that transforms chemical design rules into deployable molecular libraries, with each stage acting as a fidelity gate that eliminates non-viable candidates before expensive computation is spent.

1

RDKit SMARTS Generation

Molecular candidates are generated programmatically using RDKit reaction SMARTS -- pattern-matching rules that define how to assemble molecular scaffolds from a library of functional group building blocks. SMARTS encode the combinatorial chemistry: "attach chelator X to scaffold Y with linker Z." This stage produced the 730 unique structures archived in candidates.sdf (V2000 format). Druglikeness and synthetic accessibility filters eliminate unrealizable molecules before any quantum calculation begins.

2

DFT Screening (CP2K on A100 GPUs)

A representative subset of candidates undergoes full Density Functional Theory calculation on the CP2K package via the Inductiva cloud platform. Each DFT run solves the Kohn-Sham equations for the ligand-metal complex, computing binding energies, charge distributions, and equilibrium bond lengths from quantum mechanical first principles. 58 DFT calculations are verified, each traceable to an Inductiva task ID. These serve as the ground-truth training set for the next stage.

3

ML Surrogate Models

The DFT training set feeds three machine learning regressors that predict binding energy for the remaining unstudied candidates at near-zero computational cost. The surrogate ensemble achieves: Ridge regression R² = 0.873 (caveat: 58-sample set dominated by metal identity feature), Gradient Boosted Regression (GBR) R² = 0.915, and Random Forest (RF) R² = 0.888. Consensus predictions (agreement across all three models) identify the highest-confidence candidates for scale-up, while disagreement flags molecules that need explicit DFT verification. This 1000x speedup over brute-force DFT is what makes screening 730 candidates feasible on a research budget.

4

Kremser Cost Modeling and Techno-Economic Analysis

Surviving candidates are evaluated through a first-principles techno-economic model that converts DFT binding energies into real-world CapEx and OpEx projections. The Kremser equation translates each ligand's separation factor into the required number of mixer-settler stages; a multi-source COGS (cost of goods sold) model estimates synthesis cost per kilogram; and a Kremser sensitivity analysis maps the full alpha = 3.3 to 7.5 range into CapEx reduction curves. The output is a ranked library where every molecule carries both a quantum-verified selectivity score and a dollar-denominated plant cost estimate.

730

SMARTS-generated candidates

58

DFT-verified (CP2K)

0.873

Best surrogate R² (caveat)

40-65%

CapEx reduction range

Strategic Significance: Rare Earth Geopolitics

The Supply Chain Vulnerability

China controls over 60% of global rare earth mining and approximately 90% of rare earth processing and refining. This is not a market inefficiency -- it is a deliberate strategic position built over three decades of state-directed investment. In 2010, China demonstrated willingness to weaponize this dominance by restricting REE exports to Japan during a territorial dispute, causing neodymium prices to spike 750% in twelve months.

The concentration risk is not limited to mining. Even when rare earth ores are extracted in Australia, Brazil, or the United States, they are typically shipped to China for separation and refining because no other country operates separation plants at competitive cost. The bottleneck is not geology -- it is the capital cost and technical complexity of the solvent extraction cascade. This is precisely the bottleneck that Janus ligands break.

What Depends on Rare Earths

Electric Vehicle Motors

Every EV permanent-magnet motor contains 1-2 kg of NdFeB (neodymium-iron-boron) magnets. The US plans to produce 50% EV sales by 2030 -- roughly 8 million vehicles/year -- requiring approximately 12,000 tonnes of refined neodymium annually. Current domestic supply: near zero.

Wind Turbines

Direct-drive offshore wind turbines (the dominant new design) use 600 kg of rare earth magnets per megawatt. The US offshore wind pipeline of 30 GW by 2030 requires roughly 18,000 tonnes of NdFeB -- all currently sourced through Chinese refining.

Defense Systems

Precision-guided munitions, fighter jet engines (samarium-cobalt magnets for high-temperature operation), submarine sonar arrays, and satellite reaction wheels all require rare earths. A single F-35 contains approximately 450 kg of rare earth materials. The DOD has classified rare earth dependence as a critical national security vulnerability.

Consumer Electronics

Smartphone vibration motors, laptop speakers, hard drive actuators, and MRI machines all depend on NdFeB magnets. The entire advanced electronics supply chain runs through Chinese rare earth processing as a single point of failure.

How Janus Ligands Change the Equation

The reason the US and its allies do not operate competitive REE separation plants is economics: at alpha ~ 1.5 (TBP), a separation plant requires 25-30+ mixer-settler stages, pushing CapEx to $200-500M. Chinese state subsidies and lower environmental standards absorb this cost; Western operators cannot. By raising the separation factor to 3.3-7.5, Janus ligands compress the plant to 8-15 stages and reduce CapEx to $70-175M -- a price point where private capital can finance domestic REE separation without government subsidy.

This technology is designed from the outset for CMMC (Cybersecurity Maturity Model Certification) and ITAR compliance. The PROV 5 data room includes a DOD_COMPLIANCE directory with CMMC readiness documentation, ITAR classification guidance, and supply-chain provenance records for every computational input. The 95 patent claims span 8 families across all three inventions, providing IP protection for the full stack: molecular design, synthesis routes, process integration, and the AI pipeline itself.

Three Inventions in One Data Room

Invention
Key Metric
Verification
Application
Janus Ligands
20-40% CapEx reduction
58 DFT (CP2K)
REE extraction
Fluorocatchers
-121 kJ/mol
2 DFT verified
PFAS remediation
Steric Sieve
~10x Li/Na
13/13 DFT + GROMACS
Ion-selective membranes

ML Surrogate Model Performance

Three independent machine learning models were trained on the 58 DFT-verified binding energies to predict performance across the full 730-candidate library. The ensemble approach provides both prediction accuracy and uncertainty quantification -- candidates where all three models agree are high-confidence; disagreement flags molecules for explicit DFT re-verification.

0.873

Ridge Regression

Linear model with L2 regularization. Caveat: 58-sample training set is small, and R² is dominated by the metal identity feature (Fe vs La have very different total energies). Fast inference, interpretable coefficients. Full-data R² higher but overfit gap monitored.

0.915

Gradient Boosted (GBR)

Tree-ensemble model that captures nonlinear interactions between molecular descriptors. Slightly lower R² than Ridge suggests mild overfitting to complex features, but provides complementary error patterns for ensemble averaging.

0.888

Random Forest (RF)

Bagged decision tree ensemble. Provides inherent uncertainty estimation via inter-tree variance. The most conservative model, making it the preferred gatekeeper for flagging candidates that need DFT re-verification.

Critical Mineral Separation Benchmark

Second public data room for PROV 5. Janus Ligand vs TBP benchmark: 730 verified structures, 58 DFT calculations, all outperform industrial baseline. 20-40% CapEx reduction (Kremser validated, 7.97 to 4.35-6.41 stages).

View Repository

Key Results

Candidate Structures

730 candidates (58 DFT-verified)

DFT Simulations

58 verified

CapEx Reduction

20-40% (REE, Kremser validated)

Li/Na Selectivity

~10x (Steric Sieve)

PFAS Binding

-121 kJ/mol

Patent Claims

51

Applications

Rare earth recycling (magnets, batteries)
PFAS "forever chemical" remediation
Lithium extraction from brine
Nuclear waste separation

PFAS Filtration Crisis & Critical Mineral Separation

Two public data rooms: PFAS remediation with Fluorocatcher ligands and Janus REE extraction with 730 candidate scaffolds (20 DFT-verified). Full CP2K/GROMACS reproducibility suite.

View Public Data Room

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