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    • 82. 发明授权
    • Purification of PGM species from mixtures thereof
    • 从其混合物中纯化PGM物质
    • US08092573B2
    • 2012-01-10
    • US12373438
    • 2007-06-28
    • Dmitri TerekhovNanthakumar Victor-EmmanuelOlujide OlurinKamran Khozan
    • Dmitri TerekhovNanthakumar Victor-EmmanuelOlujide OlurinKamran Khozan
    • C22B3/44C22B11/00
    • C22B5/20C22B11/02C22B11/021C22B11/06Y02P10/214
    • A process for the production of a purified PGM selected from the group consisting of platinum and rhodium from an impure PGM source, the process comprising (a) obtaining an anhydrous PGM halide from the impure PGM source; (b) treating the PGM halide with carbon monoxide at an effective temperature; pressure and time to form the PGM carbonyl halide; and (c) (i) wherein the PGM is platinum, heating the platinum carbonyl halide at an effective platinum decomposition temperature to produce the purified platinum; (ii) wherein the PGM is rhodium, heating the rhodium halide at an effective rhodium decomposition temperature to produce the purified rhodium; and (iii) wherein the platinum carbonyl carbonyl halide and the rhodium carbonyl halide are in a gaseous mixture, effecting step (i) at a temperature lower than the rhodium effective decomposition temperature prior to effecting step (ii). The process is of particular value in the recovery and recycle of PGM materials from vehicle exhaust catalytic converters.
    • 一种从不纯的PGM源生产选自铂和铑的纯化PGM的方法,该方法包括(a)从不纯的PGM源获得无水PGM卤化物; (b)在有效温度下用一氧化碳处理PGM卤化物; 压力和时间形成PGM羰基卤化物; 和(c)(i)其中PGM是铂,在有效的铂分解温度下加热铂羰基卤化物以产生纯化的铂; (ⅱ)其中PGM是铑,在有效的铑分解温度下加热卤化铑以产生纯化的铑; 和(iii)其中所述铂羰基羰基卤化物和所述卤化铑为气态混合物,在进行步骤(ii)之前,在低于所述铑有效分解温度的温度下进行步骤(i)。 该方法对于从车辆尾气催化转化器中回收和回收PGM材料具有特殊的价值。
    • 83. 发明申请
    • SEPARATION REAGENT OF PLATINUM GROUP METAL, METHOD FOR SEPARATING AND RECOVERING PLATINUM GROUP METAL, AND AMIDE-CONTAINING TERTIARY AMINE COMPOUND
    • 铂族金属的分离试剂,分离和回收铂族金属的方法,以及含胺的仲胺化合物
    • US20100095807A1
    • 2010-04-22
    • US12640077
    • 2009-12-17
    • Hirokazu NARITAMikiya TANAKAKazuko MORISAKU
    • Hirokazu NARITAMikiya TANAKAKazuko MORISAKU
    • C22B11/00C07C237/02
    • C22B11/04C22B3/001C22B3/0032C22B3/10C22B11/06Y02P10/234
    • The present invention provides a novel separation reagent capable of obtaining a high extraction % of rhodium in a chlorine-based acid solution, which has never existed heretofore, and a method for separating and recovering a platinum group metal using the same. An organic phase composed of an amide-containing tertiary amine separation reagent represented by the structural formula shown below is brought into contact with an acid solution containing a platinum group metal, thereby extracting rhodium, platinum and palladium with the organic phase. Among the metals extracted with the organic phase, rhodium is selectively back-extracted with a highly-concentrated hydrochloric acid solution, while palladium and platinum are back-extracted with a highly-concentrated nitric acid solution: wherein at least one of R1, R2 and R3 represents an amide group represented by: R1 to R3 other than the amide group and R4 to R6 represent a group selected from an optionally branched chain hydrocarbon group of 1 to 18 carbon atoms, an alicyclic hydrocarbon group of 1 to 10 carbon atoms, and an aromatic hydrocarbon group of 1 to 14 carbon atoms.
    • 本发明提供了一种能够在迄今为止从未存在的氯系酸溶液中获得高提取率的铑的新型分离试剂,以及使用该分离试剂的铂族金属的分离和回收方法。 将由下述结构式表示的含酰胺的叔胺分离试剂构成的有机相与含有铂族金属的酸溶液接触,由有机相萃取铑,铂和钯。 在有机相提取的金属中,用高度浓缩的盐酸溶液选择性地反萃取铑,钯和铂用高浓度硝酸溶液反萃取:其中R1,R2和 R3表示由除酰胺基以外的R1〜R3表示的酰胺基,R4〜R6表示选自1〜18个任意支链的烃基,1〜10个碳原子的脂环族烃基, 1〜14个碳原子的芳香族烃基。
    • 85. 发明申请
    • Method for recovering metal from ore
    • 从矿石中回收金属的方法
    • US20090241736A1
    • 2009-10-01
    • US12232103
    • 2008-09-10
    • Yoshifumi AbeHiroshi HosakaKazuaki TakebayashiYasunari IshiguroAkira Yoshimura
    • Yoshifumi AbeHiroshi HosakaKazuaki TakebayashiYasunari IshiguroAkira Yoshimura
    • C22B11/00C22B15/00
    • C22B11/048C22B3/0005C22B3/065C22B3/24C22B7/007C22B7/008C22B7/009C22B11/04C22B11/06C22B15/0069C22B15/0093Y02P10/214Y02P10/234Y02P10/236
    • The copper sulfide ore is leached in the halide bath without using a special oxidant but with the use of only air. The copper and gold in the copper sulfide ore can be leached at high leaching ratio.The treating steps are as follows. (1) Copper leaching process (CL). The raw material is charged into the first acidic aqueous solution, which contains cupric chloride, ferric chloride, 7 g/L of hydrochloric acid, and sodium chloride. The post-leach liquor contains copper in cuprous state ions and copper in cupric state ions. (2) Solid-Liquid separation step. The resultant solid and liquid of CL step are separated. (3) Air oxidation step (OX). Air is blown into the post solid-liquid separation liquor. The copper in cuprous state ions are oxidized to the copper in cupric state ions. The iron leached in the step (1) is oxidized. Simultaneously, the impurities leached in the step (2) are precipitated. (4) Copper extracting step (CEX). The copper is recovered from the post-liquor of the step (3) (5) Gold recovering step (AL). The residue separated in the step (2) is added to the leach liquor similar to that of the step (1). The steps (1) and (5) are carried out under the atmospheric pressure and at the temperature of boiling point or lower, while blowing air into the leach liquor.
    • 硫化铜矿石在卤化物浴中浸出,不使用特殊的氧化剂,但仅使用空气。 硫化铜矿中的铜和金可以高浸出率浸出。 处理步骤如下。 (1)铜浸出工艺(CL)。 将原料装入含有氯化铜,氯化铁,7g / L盐酸和氯化钠的第一种酸性水溶液中。 后浸出液含有铜离子中的铜和铜离子中的铜。 (2)固液分离步骤。 将所得的CL步骤的固体和液体分离。 (3)空气氧化步骤(OX)。 将空气吹入后固体分液中。 铜离子中的铜被铜离子氧化成铜。 在步骤(1)中浸出的铁被氧化。 同时,在步骤(2)中浸出的杂质沉淀。 (4)铜提取步骤(CEX)。 从步骤(3)(5)金回收步骤(AL)的后液中回收铜。 在步骤(2)中分离的残余物加入到与步骤(1)相似的浸出液中。 步骤(1)和(5)在大气压力和沸点或更低的温度下进行,同时将空气吹入浸出液中。
    • 86. 发明申请
    • PROCESS OF LEACHING GOLD
    • 浸金工艺
    • US20090241735A1
    • 2009-10-01
    • US12216447
    • 2008-07-03
    • Yoshifumi AbeHiroshi HosakaKazuaki TakebayashiYasunari IshiguroAkira Yoshimura
    • Yoshifumi AbeHiroshi HosakaKazuaki TakebayashiYasunari IshiguroAkira Yoshimura
    • C22B11/00
    • C22B11/04C22B3/24C22B11/06C22B15/0067Y02P10/234Y02P10/236
    • A process of leaching gold comprising the steps of: a) leaching copper from copper sulfide ore material that contains gold or contains silicate ore containing gold until the copper grade is reduced to 7.9 wt % or less; b) mixing the resulting material having a copper grade of 7.9 wt % or less with a gold leaching solution selected from the group consisting of a first solution containing chloride ions and ferric ions, and a second solution containing chloride ions and iron ions, the iron ions having been oxidized to trivalent ferric ions by air bubbled into the second solution; c) adjusting the pH of the gold leaching solution to 1.9 or less with stirring to leach at least gold in the material into the gold leaching solution by the oxidative activity of the ferric ions contained in the gold leaching solution, wherein the concentration of gold is reduced by selectively removing gold from part or all of the gold leaching solution during gold leaching. This process efficiently leaches at least copper and gold from a copper sulfide ore.
    • 一种浸金的方法,包括以下步骤:a)将铜从含有金的硫化铜矿物料中浸出或含有含有含金的硅酸盐矿石,直到铜等级降低至7.9重量%以下; b)将所得到的铜等级为7.9重量%以下的材料与选自含有氯离子和铁离子的第一溶液的金浸出溶液和含有氯离子和铁离子的第二溶液混合, 已经通过鼓泡入第二溶液的空气氧化成三价铁离子的离子; c)通过搅拌将金浸出溶液的pH调节至1.9或更小,通过金浸出溶液中所含的三价铁离子的氧化活性,将材料中的至少金浸入金浸出溶液中,其中金的浓度为 通过在金浸出期间通过选择性地从部分或全部金浸出溶液中除去金而减少。 该方法有效地从硫化铜矿中浸出铜和金。
    • 88. 发明申请
    • Method for Recovering Gold
    • 恢复黄金的方法
    • US20070245856A1
    • 2007-10-25
    • US11579092
    • 2005-04-25
    • Matti HamalainenOlli Hyvarinen
    • Matti HamalainenOlli Hyvarinen
    • C22B9/00
    • C22B11/044C22B11/06Y02P10/214
    • The invention relates to a method for recovering gold from an intermediate product or residue containing sulphur and iron generated in the leaching of a sulphidic raw material. The recovery of gold and the other valuable metals in the raw material takes place in a chloride environment. The gold contained in the intermediate product or residue is leached with divalent copper and chlorine in a copper (II) chloride—sodium chloride solution in conditions where the oxidation-reduction potential is in the range of 650-750 mV and the pH between 1 and 1.6. The acid generated during the feed of chlorine is neutralized with a suitable alkali. Neutralization avoids the costs of dissolving the iron.
    • 本发明涉及从在硫化物原料浸出中产生的含硫和铁的中间产物或残余物中回收金的方法。 原料中金和其他有价值金属的回收发生在氯化物环境中。 在氧化还原电位在650-750mV的范围内,pH在1和1之间的条件下,氯化铜(II) - 氯化钠溶液中的中间产物或残余物中包含的金被二价铜和氯浸出 1.6。 在氯进料中产生的酸用合适的碱中和。 中和避免了铁的溶解成本。
    • 89. 发明申请
    • Installation and method for processing shredder residues and use of a shred fraction so produced
    • 处理粉碎机残留物的安装和方法,以及使用如此生产的碎片
    • US20040069687A1
    • 2004-04-15
    • US10415507
    • 2003-11-18
    • Daniel GoldmannBram den DunnenMichael Knust
    • B03B001/00
    • C22B7/005B03B9/061B03B2009/068C22B11/06Y02P10/212Y02W30/521
    • The present invention relates to a method for sorting shredder residues of metal-containing wastes, in particular of vehicle bodies, where the shredder residues are separated into a light shredder fraction (SLF) and a non-ferromagnetic fraction (heavy shredder fraction (SSF); as well as to a system for implementing the method. The present invention provides for (a) a crude-lint fraction (Lintcrude) being generated during the processing of the light shredder fraction (SLF) and the heavy shredder fraction (SSF) in preliminary processes (VorL, VorS) and a main process (SRH), by extracting at least a ferromagnetic fraction (Fe/V2A), a fraction (NE) containing nonferrous metals, a granulate fraction (Granulate), and a sand fraction (Sand), and (b) the crude-lint fraction (Lintcrude) being separated into a metal-containing dust fraction (NEdust) , a lint fraction (Lintpure) lacking in metals, and a metallic fraction (NEV) in a refining process, using the successive process steps of metal-balling, dust removal, and density separation.
    • 本发明涉及一种用于分选含金属废物,特别是车体的碎纸机残渣的方法,其中粉碎机残留物分离成轻粉碎部分(SLF)和非铁磁部分(重粉碎部分(SSF) 本发明提供(a)在轻粉碎机部分(SLF)和重粉碎机部分(SSF)处理期间产生的粗棉绒部分(Lintcrude),其中 通过提取至少一种铁磁性部分(Fe / V2A),含有有色金属的部分(NE),颗粒级分(颗粒)和砂级分(砂粒),初步方法(VorL,VorS)和主工艺(SRH) )和(b)分离成含金属粉尘部分(NEdust)的粗棉绒部分(Lintcrude),缺乏金属的棉绒部分(Lintpure)和精炼过程中的金属部分(NEV),使用 金属的连续过程步骤 清灰,密度分离。