# Available for Licensing - Electrochemical Rare Earth Recovery from Coal Fly Ash: Turn Waste Stockpiles into Critical Materials Revenue

Notice 2f34fb3328f84cc6b3a63b834eddfe69 (solicitation BA-1747) from ENERGY, DEPARTMENT OF, BATTELLE ENERGY ALLIANCE–DOE CNTR, posted 2026-08-24, responses due 2026-11-01T06:00:00.000Z. Status: open.

| Field | Value |
| --- | --- |
| Notice ID | 2f34fb3328f84cc6b3a63b834eddfe69 |
| Solicitation number | BA-1747 |
| Type | Special Notice |
| Agency | ENERGY, DEPARTMENT OF |
| Sub-tier | ENERGY, DEPARTMENT OF |
| Office | BATTELLE ENERGY ALLIANCE–DOE CNTR |
| Posted | 2026-08-24T17:48:12.000Z |
| Response deadline (UTC) | 2026-11-01T06:00:00.000Z |
| Set-aside | - |
| NAICS | 21229 |
| PSC | AJ11 |
| Place of performance | Idaho Falls, ID, USA |
| Award | - |

## Description

Electrochemical Rare Earth Recovery from Coal Fly Ash: Turn Waste Stockpiles into Critical Materials Revenue Technology Overview Researchers at Idaho National Laboratory have developed an electrochemical process that selectively extracts rare earth elements (REEs) from coal fly ash leachate using electricity instead of chemical reagents. The technology employs tuned anodic electrosorption with functionalized mesoporous carbon electrodes to achieve superior separation of REEs from competing metal ions. Opportunity Coal fly ash represents a massive, untapped resource: 158 million tons produced annually in the U.S. 1.5 billion tons currently stockpiled Contains 74,000-106,000 metric tons of rare earth elements Current extraction methods don't work at scale. Traditional solvent extraction relies on large volumes of chemical reagents, generating significant hazardous waste and requiring costly disposal. Poor selectivity (separation factor around 1) means you need 50-200 extraction cycles to achieve high purity. This translates to slow processing times (days to weeks), high operating costs, and growing regulatory pressure. Bottom line: there's no efficient, cost-effective, and environmentally sustainable technology for REE recovery from coal fly ash at commercial scale. Competitive Advantages Conventional solvent extraction approaches: Separation factors typically below 10, requiring 50 to 200 extraction cycles Processing times measured in days to weeks Heavy reliance on chemical reagents Significant hazardous waste generation and disposal costs Large footprint, batch-based systems Increasing regulatory and ESG pressure INL electrochemical process: Separation Factor ~7 Processing completed in hours Electricity-driven, reagent-free operation Minimal waste generation Compact, modular system design Lower disposal burden and ESG-aligned operation Additional Benefits: 60% recovery efficiency, reusable electrodes, lower operating costs, faster time to revenue. Market Applications Coal Power Plants (200+ in U.S.) - Convert fly ash from liability to revenue stream REE Recovery Companies - Replace chemical extraction with cleaner, faster processing Environmental Remediation - Process mining tailings, contaminated soils Critical Materials Supply Chain - Domestic REE sourcing for defense and electronics Beyond Coal Fly Ash - Applicable to any complex mixed-ion separation challenge Development and Licensing Current Stage: Laboratory-scale validation Underway Next Step: Pilot-scale demonstration with commercial partner Idaho National Laboratory is seeking industrial partners to license and commercialize this patent-pending technology. INL does not procure services as part of its collaboration agreements.

## Sources

- View on SAM.gov: https://sam.gov/opp/2f34fb3328f84cc6b3a63b834eddfe69/view
- Data as of 2026-11-14. Source: https://sam.gov/data-services/Contract%20Opportunities/datagov

## Cite this

"Available for Licensing - Electrochemical Rare Earth Recovery from Coal Fly Ash: Turn Waste Stockpiles into Critical Materials Revenue, SAM.gov contract opportunity 2f34fb3328f84cc6b3a63b834eddfe69." samgovapi.io, https://samgovapi.io/opportunity/2f34fb3328f84cc6b3a63b834eddfe69, data as of 2026-11-14. Primary record: https://sam.gov/opp/2f34fb3328f84cc6b3a63b834eddfe69/view

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