Process for Recovering Base Metals from Spent Hydroprocessing Catalyst
    22.
    发明申请
    Process for Recovering Base Metals from Spent Hydroprocessing Catalyst 有权
    从废水处理催化剂中回收基础金属的工艺

    公开(公告)号:US20090136399A1

    公开(公告)日:2009-05-28

    申请号:US11946736

    申请日:2007-11-28

    申请人: Rahul S. Bhaduri

    发明人: Rahul S. Bhaduri

    IPC分类号: C01G39/06 C01G53/11 C01G31/00

    摘要: A method for recovering metals from a spent dispersed catalyst originating from a Group VIB metal sulfide catalyst containing at least a Group VB and Group VIII metal for hydrocarbon oil hydroprocessing is disclosed. In one embodiment, the method comprises the steps of: contacting the spent dispersed catalyst with a leaching solution containing ammonia and air to dissolve the group VIB metal and the Group VIII metal into the leaching solution at sufficient temperature and pressure; forming a slurry containing at least a group VIB metal complex and at least a group VIII metal complex, ammonium sulfate and solid residue containing at least a Group VB metal complex and coke; separating and removing the solid residue containing ammonium metavanadate and coke from the pressure leach solution (PLS); precipitating from the PLS at least a portion of the Group VIB metal and at least a portion of the Group VIII metal by controlling the pH at a pre-selected pH to selectively precipitate as metal complexes the Group VIB and Group VIII metals.

    摘要翻译: 公开了一种从用于烃油加氢处理的至少含有VB族和VIII族金属的VIB族金属硫化物催化剂的废分散催化剂中回收金属的方法。 在一个实施方案中,该方法包括以下步骤:使废分散的催化剂与含有氨和空气的浸出溶液接触,以将VIB族金属和第VIII族金属溶解在足够的温度和压力下的浸出溶液中; 形成含有至少VIB族金属络合物和至少第VIII族金属络合物的硫酸铵和含有至少VB族金属络合物和焦炭的固体残渣的浆料; 从压力浸出溶液(PLS)中分离除去含偏钒酸铵和焦炭的固体残渣; 通过将pH控制在预先选定的pH以选择性地沉淀,从而从PLS中至少部分VIB金属和至少一部分第Ⅷ族金属沉淀,以选择性地沉淀出VIB族和VIII族金属的金属络合物。

    Exploitation of copper, nickel and cobalt by treating manganiferous
matrix oxidized ores
    23.
    发明授权
    Exploitation of copper, nickel and cobalt by treating manganiferous matrix oxidized ores 失效
    通过处理锰矿基质氧化矿石来开发铜,镍和钴

    公开(公告)号:US4511540A

    公开(公告)日:1985-04-16

    申请号:US315349

    申请日:1981-10-26

    摘要: Process for treating oxidized ores with a manganiferous matrix to recover the small quantities of copper, nickel and cobalt, which consists of attacking the aforementioned ore by means of an aqueous solution of H.sub.2 SO.sub.4 with the simultaneous injection of sulfur dioxide, at a temperature which does not exceed boiling point of the medium, at a pH less than 1.5; introducing an alkaline sulfide to precipitate the copper, nickel and cobalt sulfides in the suspension resulting from the attack; and separating by sulfides and the residue by flotation. The process is applicable to attacks on manganiferous nodules obtained from ocean beds as well as to attacks on land manganiferous matrix oxidized ores.

    摘要翻译: 用含锰基质处理氧化矿石以回收少量铜,镍和钴的方法,其包括在不同时注入二氧化硫的同时注入二氧化硫的H2SO4水溶液攻击上述矿石 超过介质的沸点,pH小于1.5; 引入碱性硫化物以沉淀由于攻击导致的悬浮液中的铜,镍和钴的硫化物; 并通过浮选分离硫化物和残留物。 该过程适用于从海床获得的锰结核的攻击以及对土地锰矿基质氧化矿石的攻击。

    Recovery of nickel and cobalt from leach slurries
    25.
    发明授权
    Recovery of nickel and cobalt from leach slurries 失效
    从浸出浆中回收镍和钴

    公开(公告)号:US4280988A

    公开(公告)日:1981-07-28

    申请号:US137402

    申请日:1980-04-04

    IPC分类号: C01G51/00 C01G53/00 C01G53/11

    CPC分类号: C22B23/0461

    摘要: A slurry, such as might be obtained from acid leaching nickeliferous ores having a high iron content, is treated to separate dissolved nickel or cobalt from iron oxide solids. The treatment involves a controlled precipitation of the non-ferrous metal with the aid of calcium sulfide or barium sulfide followed by flotation to recover a high grade concentrate of the non-ferrous metal.

    摘要翻译: 处理诸如可能从具有高铁含量的酸浸浸炼含镍矿石获得的浆料,以从氧化铁固体中分离溶解的镍或钴。 该处理包括借助硫化钙或硫化钡对有色金属进行受控沉淀,然后浮选以回收有色金属的高级浓缩物。

    Oxidation-resistant nickel and cobalt sulfides and method for preparing
same
    26.
    发明授权
    Oxidation-resistant nickel and cobalt sulfides and method for preparing same 失效
    耐氧化镍和硫化钴及其制备方法

    公开(公告)号:US3975507A

    公开(公告)日:1976-08-17

    申请号:US544498

    申请日:1975-01-27

    IPC分类号: C01G51/00 C01G53/11 C01G53/00

    摘要: The sulfides of nickel and cobalt prepared by sulfiding nickel and cobalt-enriched ammoniacal solutions oxidize rapidly (and often pyrophorically) when exposed to normal atmospheric conditions. The oxidized sulfides then react with water present in the atmosphere in a hydration reaction. This oxidation and hydration may increase the weight of the sulfides by as much as 150% or more, depending upon such factors as the type of sulfides involved and the duration of the exposure. However, when nickel sulfide, cobalt sulfide, or mixtures thereof are dried, dehydrated, heated at temperatures of about 1000.degree.F. or higher in a substantially inert atmosphere, and then cooled in a substantially inert atmosphere, the sulfides can surprisingly be exposed to normal atmospheric conditions for prolonged periods of time without undergoing significant oxidation or hydration. Consequently, only minimal weight increases are observed with the treated sulfides. The invention is of particular utility where the sulfides must be shipped from one location to another for further processing and will be in transit or storage for long periods of time.

    摘要翻译: 通过硫化镍和富钴氨溶液制备的镍和钴的硫化物在暴露于正常大气条件下会迅速氧化(通常是自发地)。 然后氧化的硫化物在水合反应中与存在于大气中的水反应。 这种氧化和水合可以将硫化物的重量增加多达150%或更多,这取决于诸如所涉及的硫化物的类型和暴露持续时间等因素。 然而,当硫化镍,硫化钴或其混合物在基本惰性气氛中干燥,脱水,加热至约1000°F或更高温度时,然后在基本惰性的气氛中冷却,硫化物可以令人惊讶地暴露于 正常大气条件下长时间不经历显着的氧化或水合。 因此,仅使用经处理的硫化物观察到最小的重量增加。 本发明特别有用,其中硫化物必须从一个位置运输到另一个位置用于进一步处理,并且将长时间在运输或储存中。

    METHOD FOR RECOVERING SCANDIUM
    28.
    发明申请

    公开(公告)号:US20210254193A1

    公开(公告)日:2021-08-19

    申请号:US16077821

    申请日:2017-02-21

    摘要: A method for recovering scandium, by which scandium is able to be recovered from nickel oxide ore. The present invention comprises: a leaching step S1 for obtaining a leachate by leaching a nickel oxide ore containing scandium with use of sulfuric acid; a neutralization step by adding a neutralizing agent thereto; a sulfurization step by adding a sulfurizing agent to the post-neutralization solution; an ion exchange step by bringing the post-sulfurization solution into contact with a chelating resin; a dissolution step by obtaining a precipitate of scandium hydroxide by adding an alkali into the scandium eluent, and subsequently adding an acid solution to the scandium hydroxide; a solvent extraction step by bringing the scandium acid dissolution liquid into contact with a neutral extractant; and a scandium recovery step by adding oxalic acid to the extraction residue and subsequently roasting the salt of scandium oxalate.