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    • 1. 发明申请
    • METHOD FOR TREATING ACID MINE DRAINAGE
    • 用于处理酸性排水的方法
    • US20140251914A1
    • 2014-09-11
    • US13787977
    • 2013-03-07
    • Brandon Ryan BallRahul Shankar BhaduriDerek Anderson EggertPrakhar Prakash
    • Brandon Ryan BallRahul Shankar BhaduriDerek Anderson EggertPrakhar Prakash
    • C02F9/00
    • C02F9/00C02F1/442C02F1/5245C02F1/56C02F1/66C02F1/683C02F2001/007C02F2101/103C02F2101/20C02F2101/206C02F2103/10
    • A process for treating acid mine drainage containing heavy and base metals and soluble contaminants is provided. In one embodiment, at least a metal cation is added to the acid mine drainage at a pre-select pH to form insoluble heavy and base metal complexes. After the removal of the heavy and base metal complexes, the pH is raised to the alkaline range. Following removal of base metal hydroxides and gypsum, membrane filtration is employed to generate a treated membrane permeate having a reduced concentration of heavy and base metals and soluble contaminants, and a membrane reject stream containing a concentrated brine. The concentrated brine is further treated with additional lime and at least an aluminum salt to remove remaining soluble contaminants, thus producing a treated water stream with reduced levels of contaminants. Carbonation with CO2 is employed at the end of the process to neutralize flows and further precipitate residual aluminum and calcium salts.
    • 提供了一种处理含有重金属和贱金属和可溶性污染物的酸性矿井排水的方法。 在一个实施方案中,至少一种金属阳离子以预先选择的pH添加到酸性矿井排水中以形成不溶性重和碱金属络合物。 去除重金属和碱金属络合物后,将pH提高至碱性范围。 在除去碱金属氢氧化物和石膏之后,使用膜过滤产生具有降低的重质和碱金属和可溶性污染物浓度的处理过的膜渗透物,以及含有浓缩盐水的膜排出流。 浓缩的盐水进一步用额外的石灰和至少一种铝盐处理以除去残留的可溶性污染物,从而产生具有降低的污染物水平的处理水流。 在过程结束时采用碳酸化方法中和流动,进一步沉淀出残留的铝和钙盐。
    • 2. 发明授权
    • Process for separating and recovering metals
    • 金属分离和回收方法
    • US08815184B2
    • 2014-08-26
    • US13156589
    • 2011-06-09
    • Rahul Shankar BhaduriLouis Joseph NordrumAlexander E Kuperman
    • Rahul Shankar BhaduriLouis Joseph NordrumAlexander E Kuperman
    • C01G37/14
    • C22B34/345C22B7/009C22B23/026C22B23/0446C22B34/225Y02P10/214Y02P10/224Y02P10/23Y02P10/234
    • A process for treating spent catalyst containing heavy metals, e.g., Group VIB metals and Group VIII metals is provided. In one embodiment after deoiling, the spent catalyst is treated with an ammonia leach solution under conditions sufficient to dissolve the group VIB metal and the Group VIII metal into the leaching solution, forming a leach slurry. After solid-liquid separation to recover a leach solution, chemical precipitation and solids repulping is carried out to obtain an effluent stream containing ammonium sulfate (Amsul), ammonium sulfamate, Group VB, Group VIB and Group VIII metals. Following sulfidation, the Group VIII metal is fully removed and Group VB and Group VI metals are partially removed from the Amsul stream. In the additional steps of oxydrolysis and iron precipitation, an effective amount of ferric ion at a pre-select pH is added to form insoluble complexes with the Group VB and Group VIB metals, which upon liquid-solid separation produces an effluent ammonium sulfate stream containing less than 10 ppm each of the Group VB and Group VIB metals.
    • 提供了一种处理含有重金属的废催化剂的方法,例如VIB族金属和VIII族金属。 在脱油后的一个实施方案中,在足以将VIB族金属和VIII族金属溶解到浸出溶液中的条件下,用氨浸出溶液处理废催化剂,形成浸出浆料。 在固液分离回收浸出溶液后,进行化学沉淀和固体再浆化,得到含有硫酸铵(Amsul),氨基磺酸铵,VB族,VIB族和VIII族金属的流出物流。 硫化后,完全除去第Ⅷ族金属,并从Amsul流部分除去VB族和VI族金属。 在氧解溶解和铁沉淀的附加步骤中,加入预选择pH下的有效量的铁离子以与VB族和VIB族金属组合形成不溶性络合物,其在液固分离时产生流出的硫酸铵流,其含有 VB族和VIB族金属中的每一种都少于10ppm。
    • 6. 发明申请
    • METALLURGICAL EXTRACTION TECHNIQUE TO RECOVER PLATINUM GROUP METALS FROM A FILTER CAKE
    • 从过滤器中回收铂族金属的冶金提取技术
    • US20160115567A1
    • 2016-04-28
    • US14521211
    • 2014-10-22
    • Rahul Shankar BhaduriHye Kyung Cho Timken
    • Rahul Shankar BhaduriHye Kyung Cho Timken
    • C22B11/08C22B7/00
    • C22B11/08C22B3/46C22B7/009C22B11/048Y02P10/214Y02P10/234
    • This application provides a metallurgical extraction technique, comprising: a) re-pulping a feed filter cake to make a filter cake slurry; b) grinding the filter cake slurry; c) leaching the ground filter cake slurry in a hot alkaline cyanide solution to provide dissolved platinum group metals; d) liquid-solid separating of the dissolved platinum group metals; and e) recovering the dissolved platinum group metals by cementing the dissolved platinum group metals with a precipitating metal comprising an aluminum or a zinc; wherein the feed filter cake has the platinum group metals at a total amount from 0.1 to 1.5 wt % and a halide anion content from zero to less than 4 wt %. This application provides a process for platinum group metal recovery, comprising: converting a catalyst which was in contact with a water reactive ionic liquid catalyst into a non-water reactive filter cake and extracting the platinum group metals.
    • 本申请提供冶金提取技术,其包括:a)重新制浆进料滤饼以制备滤饼浆料; b)研磨滤饼浆料; c)将研磨的滤饼浆液浸入热碱性氰化物溶液中以提供溶解的铂族金属; d)溶解的铂族金属的液固分离; 和e)通过用包含铝或锌的沉淀金属固溶溶解的铂族金属来回收溶解的铂族金属; 其中所述进料滤饼具有总量为0.1至1.5重量%的铂族金属和从零至小于4重量%的卤化物阴离子含量。 本申请提供了铂族金属回收方法,包括:将与水反应性离子液体催化剂接触的催化剂转化成非水反应性滤饼并萃取铂族金属。
    • 10. 发明申请
    • PROCESS FOR SEPARATING AND RECOVERING METALS
    • 分离和回收金属的方法
    • US20120039777A1
    • 2012-02-16
    • US13156589
    • 2011-06-09
    • Rahul Shankar BhaduriLouis Joseph NordrumAlexander E. Kuperman
    • Rahul Shankar BhaduriLouis Joseph NordrumAlexander E. Kuperman
    • C22B34/30
    • C22B34/345C22B7/009C22B23/026C22B23/0446C22B34/225Y02P10/214Y02P10/224Y02P10/23Y02P10/234
    • A process for treating spent catalyst containing heavy metals, e.g., Group VIB metals and Group VIII metals is provided. In one embodiment after deoiling, the spent catalyst is treated with an ammonia leach solution under conditions sufficient to dissolve the group VIB metal and the Group VIII metal into the leaching solution, forming a leach slurry. After solid-liquid separation to recover a leach solution, chemical precipitation and solids repulping is carried out to obtain an effluent stream containing ammonium sulfate (Amsul), ammonium sulfamate, Group VB, Group VIB and Group VIII metals. Following sulfidation, the Group VIII metal is fully removed and Group VB and Group VI metals are partially removed from the Amsul stream. In the additional steps of oxydrolysis and iron precipitation, an effective amount of ferric ion at a pre-select pH is added to form insoluble complexes with the Group VB and Group VIB metals, which upon liquid-solid separation produces an effluent ammonium sulfate stream containing less than 10 ppm each of the Group VB and Group VIB metals.
    • 提供了一种处理含有重金属的废催化剂的方法,例如VIB族金属和VIII族金属。 在脱油后的一个实施方案中,在足以将VIB族金属和VIII族金属溶解到浸出溶液中的条件下,用氨浸出溶液处理废催化剂,形成浸出浆料。 在固液分离回收浸出溶液后,进行化学沉淀和固体再浆化,得到含有硫酸铵(Amsul),氨基磺酸铵,VB族,VIB族和VIII族金属的流出物流。 硫化后,完全除去第Ⅷ族金属,并从Amsul流部分除去VB族和VI族金属。 在氧解溶解和铁沉淀的附加步骤中,加入预选择pH下的有效量的铁离子以与VB族和VIB族金属组合形成不溶性络合物,其在液固分离时产生流出的硫酸铵流,其含有 VB族和VIB族金属中的每一种都少于10ppm。