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公开(公告)号:US20220275527A1
公开(公告)日:2022-09-01
申请号:US17631844
申请日:2020-07-28
Applicant: Aqua Metals Inc.
Inventor: Samaresh Mohanta , Joshua Reill , Benjamin Sol Taecker , Jeffery Hoke , Brian James Dougherty , Jiaqi Liao
Abstract: Valuable metals, and especially copper and silver, are recovered from a lead containing electrolyte in a process in which the electrolyte is fed into an electrochemical polishing reactor that has a high-surface area cathode at which the electrode potential is controlled to so preferentially reduce copper and silver and to form a pre-treated lead-enriched electrolyte that can then be subjected electrochemical lead recovery.
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公开(公告)号:US10665907B2
公开(公告)日:2020-05-26
申请号:US15810808
申请日:2017-11-13
Applicant: Aqua Metals Inc.
Inventor: Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
Abstract: Lead from lead acid battery scrap is recovered in two separate production streams as clean grid lead and as high-purity lead without smelting. In preferred aspects, lead recovery is performed in a continuous process that uses an aqueous electroprocessing solvent and electro-refining, and spent electroprocessing solvent can be recycled to the recovery process.
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公开(公告)号:US20180355494A1
公开(公告)日:2018-12-13
申请号:US15573393
申请日:2016-05-13
Applicant: Aqua Metals Inc.
Inventor: Stephen R. Clarke , Robert Lewis Clarke , Brian Dougherty
Abstract: A closed loop electrochemical process of recovery of high-purity lead uses continuous formation of adherent lead on a cathode from an electrolyte that is used to dissolve desulfated lead paste. Preferred cathodes include aluminum containing cathodes that are operated in methane sulfonic acid to produce a micro- or nanoporous mixed matrix metallic composition and lead dioxide formation at the anode is avoided using appropriate anode configurations or operating conditions
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公开(公告)号:US09837689B2
公开(公告)日:2017-12-05
申请号:US15037318
申请日:2014-11-18
Applicant: Aqua Metals Inc.
Inventor: Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
CPC classification number: H01M10/54 , C25C1/18 , C25C5/02 , C25C7/00 , C25C7/005 , C25C7/007 , C25C7/08 , H01M4/14 , H01M10/06 , Y02P10/212 , Y02W30/84
Abstract: Lead from lead acid battery scrap is recovered in two separate production streams as clean grid lead and as high-purity lead without smelting. In preferred aspects, lead recovery is performed in a continuous process that uses an aqueous electroprocessing solvent and electro-refining and spent electroprocessing solvent can be recycled to the recovery process.
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