Recover and recycle rhodium from spent partial oxidation catalysts
    1.
    发明授权
    Recover and recycle rhodium from spent partial oxidation catalysts 失效
    从废部分氧化催化剂回收和回收铑

    公开(公告)号:US06764662B2

    公开(公告)日:2004-07-20

    申请号:US10176224

    申请日:2002-06-20

    IPC分类号: C01G5500

    摘要: A method for the recovery of rhodium from spent supported catalysts. In one embodiment, a method for recovering rhodium from a host material includes roasting the host material in air at a temperature sufficient to convert at least a portion of rhodium to Rh2O3, leaching the host material in a solution with a leaching constituent which is reactive with Rh2O3 to form a first intermediate species, reacting the first intermediate species in a solution with an acidifying constituent or complexing agent to form a second intermediate species, and purifying the second intermediate species. Preferably, the roasting temperature is approximately from 600° C. to 800° C. for 0.5 to 10 hours. In some embodiments, the host material is ground to particles in the range of 0.1 to 10 mm.

    摘要翻译: 从废负载型催化剂中回收铑的方法。 在一个实施方案中,从主体材料回收铑的方法包括在足以将至少一部分铑转化为Rh 2 O 3的温度下在空气中焙烧主体材料,将主体材料浸入溶液中,浸出成分与 Rh 2 O 3以形成第一中间物质,使溶液中的第一中间物质与酸化成分或络合剂反应以形成第二中间物质,并纯化第二中间物质。 优选地,焙烧温度为约600℃至800℃,持续0.5至10小时。 在一些实施方案中,将主体材料研磨至0.1至10mm范围内的颗粒。

    Recover and recycle rhodium from spent partial oxidation catalysts
    2.
    发明授权
    Recover and recycle rhodium from spent partial oxidation catalysts 失效
    从废部分氧化催化剂回收和回收铑

    公开(公告)号:US06923922B2

    公开(公告)日:2005-08-02

    申请号:US10828598

    申请日:2004-04-21

    摘要: A method for the recovery of rhodium from spent supported catalysts. In one embodiment, a method for recovering rhodium from a host material includes roasting the host material in air at a temperature sufficient to convert at least a portion of rhodium to Rh2O3, leaching the host material in a solution with a leaching constituent which is reactive with Rh2O3 to form a first intermediate species, reacting the first intermediate species in a solution with an acidifying constituent or complexing agent to form a second intermediate species, and purifying the second intermediate species. Preferably, the roasting temperature is approximately from 600° C. to 800° C. for 0.5 to 10 hours. In some embodiments, the host material is ground to particles in the range of 0.1 to 10 mm.

    摘要翻译: 从废负载型催化剂中回收铑的方法。 在一个实施方案中,用于从主体材料回收铑的方法包括在足以将至少一部分铑转化为Rh 2 O 3 N / N的温度下在空气中焙烧主体材料 >,将主体材料浸入具有与Rh 2 O 3 3反应的浸出成分的溶液中以形成第一中间物质,使第一中间物质溶于 与酸化组分或络合剂形成第二中间体物质,并纯化第二中间物质。 优选地,焙烧温度为约600℃至800℃,持续0.5至10小时。 在一些实施方案中,将主体材料研磨至0.1至10mm范围内的颗粒。