11.07.2015 Views

Technologies and Costs for Removal of Arsenic From Drinking Water

Technologies and Costs for Removal of Arsenic From Drinking Water

Technologies and Costs for Removal of Arsenic From Drinking Water

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

2.6.5 Photo-OxidationResearchers at the Australian Nuclear Science <strong>and</strong> Technology Organisation (ANSTO) havefound that in the presence <strong>of</strong> light <strong>and</strong> naturally occurring light-absorbing materials, the oxidation rate<strong>of</strong> As(III) by oxygen can be increased ten-thous<strong>and</strong>fold (Cooperative Research Centres <strong>for</strong> WasteManagement <strong>and</strong> Pollution Control Limited, 1999). The oxidized arsenic, now As(V), can then beeffectively removed by co-precipitation.ANSTO evaluated both UV lamp reactors <strong>and</strong> sunlight-assisted-photo-oxidation using acidic,metal-bearing water from an ab<strong>and</strong>oned gold, silver, <strong>and</strong> lead mine. Air sparging was required <strong>for</strong>sunlight-assisted oxidation due to the high initial As(III) concentration (12 mg/L). Tests demonstratedthat near complete oxidation <strong>of</strong> As(III) can be achieved using the photochemical process. Analysis<strong>of</strong> process waters showed 97% <strong>of</strong> the arsenic in the process stream was present as As(V).Researchers also concluded that As(III) was preferentially oxidized in the presence <strong>of</strong> excessdissolved Fe(II) (22:1 iron to arsenic mole ratio). This is a contrast to conventional plants wheredissolved Fe(II) represents an extra chemical oxidant dem<strong>and</strong> which has to be satisfied duringoxidation <strong>of</strong> As(III) (CRC-WMPC, 1999).Photo-oxidation <strong>of</strong> the mine water followed by co-precipitation was able to reduce arsenicconcentrations to as low as 17 Fg/L, which meets the current MCL <strong>for</strong> arsenic. Initial total arsenicconcentrations were unknown, though the As(III) concentration was given as approximately 12 mg/L,which is considerably higher than typical raw water arsenic concentrations. ANSTO reportedresiduals from this process are environmentally stable <strong>and</strong> passed the Toxicity Characteristic LeachingProcedure (TCLP) test necessary to declare waste non-hazardous <strong>and</strong> suitable <strong>for</strong> l<strong>and</strong>fill disposal.Based on the removals achieved <strong>and</strong> residuals characteristics, it is expected that photooxidationfollowed by co-precipitation would be an effective arsenic removal technology. However,this technology is still largely experimental <strong>and</strong> should be further evaluated be<strong>for</strong>e recommendationas an approved arsenic removal technology <strong>for</strong> drinking water.2-48

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!