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Catalytic Denitrification in a Trickle Bed Reactor: Ion Exchange Waste Brine Treatment

Catalytic reduction of nitrate in ion exchange (IX) waste brine for reuse is a promising option for reducing IX costs and environmental impacts. A recycling trickle bed reactor (TBR) was designed and optimized using 0.5 percent by weight (wt%) palladium–0.05 wt% indium catalysts supported on US mesh...

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Bibliographic Details
Published in:Journal - American Water Works Association 2017-05, Vol.109 (5), p.E129-E143
Main Authors: BERGQUIST, ALLISON M., BERTOCH, MADISON, GILDERT, GARY, STRATHMANN, TIMOTHY J., WERTH, CHARLES J.
Format: Article
Language:English
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Summary:Catalytic reduction of nitrate in ion exchange (IX) waste brine for reuse is a promising option for reducing IX costs and environmental impacts. A recycling trickle bed reactor (TBR) was designed and optimized using 0.5 percent by weight (wt%) palladium–0.05 wt% indium catalysts supported on US mesh size 12 × 14 or 12 × 30 activated carbon particles. Various liquid superficial velocities (Ur) and hydrogen gas superficial velocities (Ug-H2) were evaluated to assess performance in different flow regimes; catalyst activity increased with Ug-H2 at all Ur for both catalysts and was greatest for the 12 × 30 catalyst at the lowest Ur (8.9 m/h). The 12 × 30 catalyst demonstrated up to 100% higher catalytic activity and 280% higher mass transfer rate compared with the 12 × 14 catalyst. Optimal TBR performance was achieved with both catalysts in the trickle flow regime. The results indicate that the TBR is a promising step forward, and continued improvements are possible to overcome remaining mass transfer limitations.
ISSN:0003-150X
1551-8833
DOI:10.5942/jawwa.2017.109.0055