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Ammonia oxidation by in-situ chloride electrolysis in etching wastewater of semiconductor manufacturing using RuSnO x /Ti electrode: Effect of plating mode and metal ratio.

Authors :
Rahardjo SSP
Shih YJ
Fan CS
Source :
Journal of hazardous materials [J Hazard Mater] 2024 May 05; Vol. 469, pp. 134042. Date of Electronic Publication: 2024 Mar 13.
Publication Year :
2024

Abstract

The indirect chloride-mediated ammonia oxidation encounters challenges in maintaining the effectiveness of metal oxide anodes when treating wastewaters with complex compositions. This study aims to develop a highly stable anode with RuO <subscript>2</subscript> -SnO <subscript>2</subscript> coatings for treating an etching effluent from semiconductor manufacturing, which majorly contains NH <subscript>3</subscript> and organic compounds. The RuSnO <subscript>x</subscript> /Ti electrode was synthesized using wet impregnation and calcination processes. The metal oxide configuration on Ti plate substrate was tuned by varying the step-dipping process in RuCl <subscript>3</subscript> and SnCl <subscript>4</subscript> baths. A 10-day continuous-flow electrolysis was conducted for studying the ammonia removal and chlorine yield under variable conditions, including detention, pH, current density, and initial ammonia and chloride concentrations. In the RuSnO <subscript>x</subscript> coatings, the configuration comprising RuO <subscript>2</subscript> nanorods as the surface layer and an intermediate layer of SnO <subscript>2</subscript> crystallites (by plating Ru <superscript>3+</superscript> for three times to cover one Sn <superscript>4+</superscript> layer, denoted as the Ru <subscript>3</subscript> Sn/Ti electrode) exhibited the best durability for acid washing, along with relatively high Faradaic efficiency and low energy consumption. To further improve the treatability of real wastewater (NH <subscript>3</subscript> -N = 634 mg L <superscript>-1</superscript> , chemical oxygen demand (COD) = 6700 mg L <superscript>-1</superscript> , Cl <superscript>-</superscript> = 2000 mg L <superscript>-1</superscript> , pH 11), the duel-cell electrolyzers were constructed in series under a current density of 30 mA cm <superscript>-2</superscript> and 45 min detention. Ultimately, removals of NH <subscript>3</subscript> and COD reached 95.8% and 76.3%, respectively, with successful limitation of chloramine formation.<br />Competing Interests: Declaration of Competing Interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.<br /> (Copyright © 2024 Elsevier B.V. All rights reserved.)

Details

Language :
English
ISSN :
1873-3336
Volume :
469
Database :
MEDLINE
Journal :
Journal of hazardous materials
Publication Type :
Academic Journal
Accession number :
38521031
Full Text :
https://doi.org/10.1016/j.jhazmat.2024.134042