Nano-Composite Arsenic Sorbent (N-CAS)
- 技術優勢
- Costs$0.10-0.15 per thousand gallons of water treated (less than ¼ the cost ofcompeting technologies)Canremove 7-100 times more arsenic than existing adsorbents, meaning a longer runcycleSpentmedia passes TCLP leach test (non-leachable), reducing cost of disposalMultipleregenerations without losing efficacyShortcontact times for removal
- 技術應用
- Municipalwater treatmentIndividualhome or well-head systemsPortablewater treatment devicesPhilanthropicpurposes
- 詳細技術說明
- Researchers at INL havedeveloped methods and systems for the removal of arsenic from water at a cost projectedto be below $0.15 per thousand gallons. Utilizing Nano-sized particles,extremely high reaction rates facilitate rapid, selective arsenic removal evenat low (10 ppb) concentrations. The Nano sorbent has an arsenic “loading”factor seven to 100 times greater than existing adsorbents, and can beregenerated without appreciable loss of capacity multiple times, reducing wasteand operating costs.
- *Abstract
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TECHNOLOGYMARKETING SUMMARY:
Globally, tens of millions of people are exposed to dangerous concentrations ofthe toxin arsenic as it naturally leaches from rocks and soil into drinkingwater supplies. Even in the United States, thousands of municipalities andmillions of people have drinking water that exceeds the EPA recommendation of10 parts per billion (ppb) of arsenic. Current arsenic removal methods cost$0.50-$1.50 per thousand gallons of water treated, require frequentreplacement, are prone to decomposition, have low removal efficiencies, andoften require long contact times to facilitate the capture. These limitationsmake them difficult to implement in large-scale water treatment or local wellwater treatment.
- 其他
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LICENSINGOPPORTUNITY:
IdahoNational Laboratory (INL) and its M&O Contractor Battelle Energy Alliance,LLC (BEA) are currently looking for commercialization partner(s) interested inentering into a license agreement for the purpose of commercializing thetechnology described below.INTELLECTUALPROPERTY STATUS:
This invention has associated intellectual property:- US Patent No. 7,368,412,BEA Docket No. B-379: “High Capacity Adsorption Media And Methods OfProducing,” issued 6 May 2008
- US Patent No. 8,043,586,BEA Docket No. B-379D1: “High Capacity Adsorption Media for Separating orRemoving constituents and Methods of Producing and Using the Adsorption Media,”issued 25 October 2011
- US Patent No. 7,807,606,BEA Docket No. BA-032: “High Capacity Adsorption Media for Separating orRemoving Constituents, Associated Apparatus, and Methods of Producing and Usingthe Adsorption Media,” issued 5 October 2010
- US Patent No. 7,947,861,BEA Docket No. BA-032D1: “Removing a Constituent from a Feed Stream UsingAdsorption Media,” issued 24 May 2011
- US Patent No. 8,664,150,BEA Docket No. BA-378: “Methods of Producing Metal Oxides, a Method ofProducing Adsorption Media Including the Same, and a Precursor of an ActiveComponent Including the Metal Oxide,” issued 22 September 2011
This technology has been tested and validated at thebench scale. Additional development will be required to establish a commercialscale manufacturing process.
ADDITIONAL INFORMATION: Fact Sheet
- 國家/地區
- 美國
