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公开(公告)号：US11239507B2
公开(公告)日：2022-02-01
申请号：US16407914
申请日：2019-05-09
申请人： Aqua Metals Inc.
发明人： Brian Dougherty , Michael John King , Robert Lewis Clarke , Stephen R. Clarke , Michael David Hurwitz
摘要： 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. Spent electroprocessing solvent and/or base utilized to treat lead paste from the lead acid battery scrap can be recycled to the recovery process.
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公开(公告)号：US20180127888A1
公开(公告)日：2018-05-10
申请号：US15573410
申请日：2016-05-13
申请人： Aqua Metals Inc.
IPC分类号： C25C1/18 , C25C5/02 , H01M4/16 , H01M4/68 , H01M4/73 , H01M4/84 , H01M10/06 , B82Y40/00 , B21J1/06 , B21K23/00
CPC分类号： C25C1/18 , B21J1/06 , B21K23/00 , B82Y40/00 , C25C5/02 , H01M4/14 , H01M4/16 , H01M4/68 , H01M4/73 , H01M4/84 , H01M10/06 , Y02W30/84
摘要： The inventive subject matter is directed to continuous electrochemical production of highly pure micro- or nanostructured lead that at least partially encloses the electroprocessing solvent and molecular hydrogen and optional guest compounds to form a mixed matrix. Such compositions are particularly suitable for cold forming of various structures and/or for alloy and composite material production.
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公开(公告)号：US10689769B2
公开(公告)日：2020-06-23
申请号：US15573410
申请日：2016-05-13
申请人： Aqua Metals Inc.
IPC分类号： H01M4/16 , H01M4/68 , C25C1/18 , H01M10/06 , C25C5/02 , H01M4/14 , B21J1/06 , B82Y40/00 , H01M4/73 , H01M4/84 , B21K23/00
摘要： The inventive subject matter is directed to continuous electrochemical production of highly pure micro- or nanostructured lead that at least partially encloses the electroprocessing solvent and molecular hydrogen and optional guest compounds to form a mixed matrix. Such compositions are particularly suitable for cold forming of various structures and/or for alloy and composite material production.
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公开(公告)号：US10566665B2
公开(公告)日：2020-02-18
申请号：US15810808
申请日：2017-11-13
申请人： Aqua Metals Inc.
发明人： Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
摘要： 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：US20170352927A1
公开(公告)日：2017-12-07
申请号：US15527749
申请日：2015-05-13
申请人： Aqua Metals Inc.
发明人： Brian Dougherty , Michael John King , Robert Lewis Clarke , Stephen R. Clarke , Michael David Hurwitz
CPC分类号： H01M10/54 , C25C1/18 , C25C5/02 , C25C7/00 , C25C7/005 , C25C7/007 , C25C7/08 , H01M4/14 , H01M10/06 , Y02P10/212 , Y02W30/84
摘要： 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. Spent electroprocessing solvent and/or base utilized to treat lead paste from the lead acid battery scrap can be recycled to the recovery process.
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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
申请人： Aqua Metals Inc.
发明人： Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
摘要： 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：US09837689B2
公开(公告)日：2017-12-05
申请号：US15037318
申请日：2014-11-18
申请人： Aqua Metals Inc.
发明人： Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
CPC分类号： H01M10/54 , C25C1/18 , C25C5/02 , C25C7/00 , C25C7/005 , C25C7/007 , C25C7/08 , H01M4/14 , H01M10/06 , Y02P10/212 , Y02W30/84
摘要： 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：US20190267681A1
公开(公告)日：2019-08-29
申请号：US16407914
申请日：2019-05-09
申请人： Aqua Metals Inc.
发明人： Brian Dougherty , Michael John King , Robert Lewis Clarke , Stephen R. Clarke , Michael David Hurwitz
摘要： 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. Spent electroprocessing solvent and/or base utilized to treat lead paste from the lead acid battery scrap can be recycled to the recovery process.
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公开(公告)号：US10340561B2
公开(公告)日：2019-07-02
申请号：US15527749
申请日：2015-05-13
申请人： Aqua Metals Inc.
发明人： Brian Dougherty , Michael John King , Robert Lewis Clarke , Stephen R. Clarke , Michael David Hurwitz
摘要： 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. Spent electroprocessing solvent and/or base utilized to treat lead paste from the lead acid battery scrap can be recycled to the recovery process.
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公开(公告)号：US20180069276A1
公开(公告)日：2018-03-08
申请号：US15810808
申请日：2017-11-13
申请人： Aqua Metals Inc.
发明人： Stephen R. Clarke , Robert Lewis Clarke , Michael David Hurwitz , Michael John King , Selwyn Mould
摘要： 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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