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Catalytic selective recovery of silver from dilute aqueous solutions and e-waste leachates

[Display omitted] •The new process for selective silver ions recovery from water is reported.•Ag+ ions are catalytically reduced to Ag0 by H2 on the Pt in the separation step.•The Ag0 is oxidized by air on the Pt catalyst within the regeneration step.•Both steps are performed at ambient temperature...

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Published in:Separation and purification technology 2022-03, Vol.285, p.120303, Article 120303
Main Authors: Ruck, Erez B., Amikam, Gidon, Darom, Yonatan, Manor-Korin, Naama, Gendel, Youri
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cited_by cdi_FETCH-LOGICAL-c306t-8df6fe8c22e2c6579d15624525ca146426bc6b252fb1c53309bef6e47ffed1963
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container_title Separation and purification technology
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creator Ruck, Erez B.
Amikam, Gidon
Darom, Yonatan
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Gendel, Youri
description [Display omitted] •The new process for selective silver ions recovery from water is reported.•Ag+ ions are catalytically reduced to Ag0 by H2 on the Pt in the separation step.•The Ag0 is oxidized by air on the Pt catalyst within the regeneration step.•Both steps are performed at ambient temperature and gas pressure of 1 bar.•Ag+ ions are separated from Cu2+ ions due to higher reduction potential of Ag+. The two-step catalytic process is proposed for the recovery of silver ions from aqueous solutions. First, the Ag+-containing solution is enriched with hydrogen gas and recirculated through the Pt-loaded activated carbon (Pt/AC). The Ag+ ions are reduced into the metal particles at ambient temperature and H2 gauge pressure of 1 atmosphere. Next, the Ag particles precipitated on the Pt/AC are oxidized by air to form the pure Ag+ concentrate and to regenerate the catalyst. The process was studied using pure AgNO3 solutions at varied pH values (0.0, 1.5 and 3.9) in a batch mode system that was operated with Pt/AC particles loaded with 0.1–1.0% of Pt metal. The complete removal of Ag+ ions was achieved within
doi_str_mv 10.1016/j.seppur.2021.120303
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The two-step catalytic process is proposed for the recovery of silver ions from aqueous solutions. First, the Ag+-containing solution is enriched with hydrogen gas and recirculated through the Pt-loaded activated carbon (Pt/AC). The Ag+ ions are reduced into the metal particles at ambient temperature and H2 gauge pressure of 1 atmosphere. Next, the Ag particles precipitated on the Pt/AC are oxidized by air to form the pure Ag+ concentrate and to regenerate the catalyst. The process was studied using pure AgNO3 solutions at varied pH values (0.0, 1.5 and 3.9) in a batch mode system that was operated with Pt/AC particles loaded with 0.1–1.0% of Pt metal. The complete removal of Ag+ ions was achieved within&lt;2 h of hydrogenation of 1-liter AgNO3 solutions with an initial concentrations of 100–1000 mgAg/L. The hydrogenation rate was not influenced by the pH value. Increasing the Pt load in the Pt/AC media above 0.25% did not result in an increase in the Ag+ hydrogenation rate. Next, the process was applied for the separation of Ag+ ions from H2SO4 leachates of Ag2O-Zn batteries. 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The two-step catalytic process is proposed for the recovery of silver ions from aqueous solutions. First, the Ag+-containing solution is enriched with hydrogen gas and recirculated through the Pt-loaded activated carbon (Pt/AC). The Ag+ ions are reduced into the metal particles at ambient temperature and H2 gauge pressure of 1 atmosphere. Next, the Ag particles precipitated on the Pt/AC are oxidized by air to form the pure Ag+ concentrate and to regenerate the catalyst. The process was studied using pure AgNO3 solutions at varied pH values (0.0, 1.5 and 3.9) in a batch mode system that was operated with Pt/AC particles loaded with 0.1–1.0% of Pt metal. The complete removal of Ag+ ions was achieved within&lt;2 h of hydrogenation of 1-liter AgNO3 solutions with an initial concentrations of 100–1000 mgAg/L. The hydrogenation rate was not influenced by the pH value. Increasing the Pt load in the Pt/AC media above 0.25% did not result in an increase in the Ag+ hydrogenation rate. Next, the process was applied for the separation of Ag+ ions from H2SO4 leachates of Ag2O-Zn batteries. 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The two-step catalytic process is proposed for the recovery of silver ions from aqueous solutions. First, the Ag+-containing solution is enriched with hydrogen gas and recirculated through the Pt-loaded activated carbon (Pt/AC). The Ag+ ions are reduced into the metal particles at ambient temperature and H2 gauge pressure of 1 atmosphere. Next, the Ag particles precipitated on the Pt/AC are oxidized by air to form the pure Ag+ concentrate and to regenerate the catalyst. The process was studied using pure AgNO3 solutions at varied pH values (0.0, 1.5 and 3.9) in a batch mode system that was operated with Pt/AC particles loaded with 0.1–1.0% of Pt metal. The complete removal of Ag+ ions was achieved within&lt;2 h of hydrogenation of 1-liter AgNO3 solutions with an initial concentrations of 100–1000 mgAg/L. The hydrogenation rate was not influenced by the pH value. Increasing the Pt load in the Pt/AC media above 0.25% did not result in an increase in the Ag+ hydrogenation rate. Next, the process was applied for the separation of Ag+ ions from H2SO4 leachates of Ag2O-Zn batteries. Finally, it was shown that due to a large difference in standard reduction potentials the silver and the copper ions can be “kinetically” separated within the hydrogenation and the oxygenation steps of the process.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.seppur.2021.120303</doi></addata></record>
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subjects Adsorption
Capacitive-Faradaic fuel cells
Electroless deposition
Hydrogenation
Hydrometallurgy
Metals separation
title Catalytic selective recovery of silver from dilute aqueous solutions and e-waste leachates
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