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Optimization of magnetic powdered activated carbon for aqueous Hg(II) removal and magnetic recovery. | LitMetric

Optimization of magnetic powdered activated carbon for aqueous Hg(II) removal and magnetic recovery.

J Hazard Mater

Department of Environmental Engineering Sciences, University of Florida, 217 Black Hall, P.O. Box 116450, Gainesville, FL 32611-645, USA.

Published: January 2012

AI Article Synopsis

  • Activated carbon can effectively adsorb mercury ions (Hg(II)) from water, and a specialized version known as magnetic powdered activated carbon (MPAC) can reduce mercury levels in water to below 0.2 μg/L while allowing for easy recovery using magnets.
  • The process involves measuring mercury removal through a controlled setup that includes mixing and monitoring to capture various forms of mercury, ensuring accurate mass balance calculations for effectiveness verification.
  • Optimal conditions for MPAC include a 3:1 carbon to iron ratio without thermal oxidation, resulting in high recovery and removal rates of mercury, while maintaining the structural integrity of the sorbent material.

Article Abstract

Activated carbon is known to adsorb aqueous Hg(II). MPAC (magnetic powdered activated carbon) has the potential to remove aqueous Hg to less than 0.2 μg/L while being magnetically recoverable. Magnetic recapture allows simple sorbent separation from the waste stream while an isolated waste potentially allows for mercury recycling. MPAC Hg-removal performance is verified by mercury mass balance, calculated by quantifying adsorbed, volatilized, and residual aqueous mercury. The batch reactor contained a sealed mercury-carbon contact chamber with mixing and constant N(2) (g) headspace flow to an oxidizing trap. Mercury adsorption was performed using spiked ultrapure water (100 μg/L Hg). Mercury concentrations were obtained using EPA method 245.1 and cold vapor atomic absorption spectroscopy. MPAC synthesis was optimized for Hg removal and sorbent recovery according to the variables: C:Fe, thermal oxidation temperature and time. The 3:1 C:Fe preserved most of the original sorbent surface area. As indicated by XRD patterns, thermal oxidation reduced the amorphous characteristic of the iron oxides but did not improve sorbent recovery and damaged porosity at higher oxidation temperatures. Therefore, the optimal synthesis variables, 3:1 C:Fe mass ratio without thermal oxidation, which can achieve 92.5% (± 8.3%) sorbent recovery and 96.3% (± 9%) Hg removal. The mass balance has been closed to within approximately ± 15%.

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Source
http://dx.doi.org/10.1016/j.jhazmat.2011.10.023DOI Listing

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