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公开(公告)号:US20180347008A1
公开(公告)日:2018-12-06
申请号:US15771500
申请日:2016-10-25
发明人: Nejc Hodnik , Claudio Baldizzone , Karl Mayrhofer
IPC分类号: C22B3/00
CPC分类号: C22B11/048 , Y02P10/214
摘要: The invention relates to a method for the recovery of precious metal from materials containing precious metal, said method comprises the following steps of: A) bringing the materials containing the precious metal into contact with an oxidizing agent, B) bringing the material containing the precious metal into contact with a reducing agent. Said method offers the possibility of recovering precious metal in a simple manner and in high purity from secondary materials.
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公开(公告)号:US10017839B2
公开(公告)日:2018-07-10
申请号:US14425129
申请日:2013-01-18
发明人: Jin-Young Lee , Joon-Soo Kim , Rajesh Kumar
CPC分类号: C22B34/365 , C22B1/005 , C22B3/22 , C22B7/009 , C22B34/225 , Y02P10/214 , Y02P10/23 , Y02P10/234
摘要: Disclosed is a method for effectively leaching valuable metals such as vanadium and tungsten contained in a waste denitrification catalyst by using roasting and water leaching. According to the present invention, the method for leaching valuable metals contained in a waste denitrification catalyst comprises the steps of: (a) mixing a waste denitrification catalyst containing vanadium (V) and tungsten (W) in the form of an oxide with an alkali metal compound to form a mixture; (b) roasting the mixture to generate a roasting product comprising sodium vanadate (NaVO3) and sodium tungstate (Na2WO4); and (c) injecting the roasting product into water to water leach sodium vanadate and sodium tungstate in the form of a vanadate ion (VO3−) and a tungstate ion (WO42−).
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公开(公告)号:US20180142330A1
公开(公告)日:2018-05-24
申请号:US15355971
申请日:2016-11-18
发明人: Felix STOFFNER , Chris HOBBS
CPC分类号: C22C19/03 , C22B9/00 , C22B9/05 , C22B11/02 , C22B11/026 , C22C1/023 , C22C1/06 , F27B14/143 , F27D3/16 , F27D2003/169 , Y02P10/214
摘要: A process for the production of a PGM-enriched alloy comprising 0 to 60 wt.-% of iron and 20 to 99 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, the process comprising the steps of (1) providing a PGM collector alloy comprising 30 to 95 wt.-% of iron, less than 1 wt.-% of sulfur and 2 to 15 wt.-% of one or more PGMs selected from the group consisting of platinum, palladium and rhodium, (2) providing a copper- and sulfur-free material capable of forming a slag-like composition when molten, wherein the molten slag-like composition comprises 40 to 90 wt.-% of magnesium oxide and/or calcium oxide and 10 to 60 wt.-% of silicon dioxide, (3) melting the PGM collector alloy and the material capable of forming a slag-like composition when molten in a weight ratio of 1:0.2 to 1 within a converter until a multi- or two-phase system of a lower high-density molten mass comprising the molten PGM collector alloy and one or more upper low-density molten masses comprising the molten slag-like composition has formed, (4) contacting an oxidizing gas comprising 0 to 80 vol.-% of inert gas and 20 to 100 vol.-% of oxygen with the lower high-density molten mass obtained in step (3) until it has been converted into a lower high-density molten mass of the PGM-enriched alloy, (5) separating an upper low-density molten slag formed in the course of step (4) from the lower high-density molten mass of the PGM-enriched alloy making use of the difference in density, (6) letting the molten masses separated from one another cool down and solidify, and (7) collecting the solidified PGM-enriched alloy.
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4.
公开(公告)号:US20180112290A1
公开(公告)日:2018-04-26
申请号:US15566332
申请日:2016-02-24
IPC分类号: C22B3/00
CPC分类号: C22B11/044 , C22B5/12 , Y02P10/214
摘要: Process for digestion of fine iridium, comprising the steps of: (a) alkaline oxidative digestion of 1 part by weight fine iridium and 3 to 20 parts by weight of a combination comprising 40 to 70 parts by weight sodium hydroxide, 15 to 30 parts by weight sodium nitrate, and 10 to 40 parts by weight sodium peroxide in the melt, whereby the sum of the weight fractions adds up to 100 parts by weight; (b) cooling the digestion material formed in step (a) to 20 to 70° C.; (c) dissolving the acid-soluble fractions of the cooled digestion material in water/halogen hydracid until an acidic aqueous solution with a pH value in the range of −1 to +1 is obtained; and (d) boiling the acidic aqueous solution obtained in step (c) until the formation of nitrous gases is completed; whereby a step (e) of separating insoluble ingredients from the acidic aqueous solution can take place before or after step (d), if needed.
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公开(公告)号:US20180105435A1
公开(公告)日:2018-04-19
申请号:US15295326
申请日:2016-10-17
发明人: Mitja Medved , Thomas Pierau
CPC分类号: C01G49/10 , B01D7/00 , B01D7/02 , C01G23/022 , C01G23/024 , C01G33/00 , C22B7/001 , C22B34/1218 , C22B34/24 , Y02P10/214 , Y02P10/23
摘要: The invention relates to a method for separating valuable metal chlorides, particularly titanium tetrachloride and niobium pentachloride, from solid residues, in particular the filter dust generated during the chlorination of raw materials containing iron and titanium in the production of titanium dioxide using the chloride process.
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公开(公告)号:US09855563B2
公开(公告)日:2018-01-02
申请号:US14906005
申请日:2014-07-21
申请人: Claudio Sasso
发明人: Claudio Sasso , Mahendra Samaroo
CPC分类号: B03B9/00 , B03B5/48 , B03B7/00 , B07B1/18 , C22B1/00 , C22B11/021 , Y02P10/214
摘要: The value-minerals are captured by gravity-separation, from a low-grade slurry. The ratio of liquids-to-solids in the slurry affects the efficiency of capture, and an ideal liquids/solids ratio is the ratio at which the efficiency of capture is at a maximum. The ideal ratio is different for different particle-sizes. The procedure includes dewatering the slurry, dividing the dry particles by particle-size, and feeding the several size-divided dry-streams into respective capture-stations. Prior to each dry-stream entering its respective capture-station, make-up water is added to the dry-stream in such quantity as to bring the liquids/solids ratio up to the ideal, for that particle-size. The procedure makes it simple to provide accurate measurement of, and accurate control of, the liquids/solids ratio.
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7.
公开(公告)号:US20170349970A1
公开(公告)日:2017-12-07
申请号:US15523757
申请日:2015-10-12
CPC分类号: C22B11/048 , B01J23/96 , B01J38/68 , C22B11/06 , Y02P10/214
摘要: Process for removing precious metal from precious metal-containing catalyst form bodies comprising form bodies and precious metal, whereby the precious metal to be removed is at least one precious metal selected from the group consisting of Au, Ag, Pd, Pt, Ir, Rh, Ru, Os, and Re, comprising the steps of: (a) producing a mixture of precious metal-containing catalyst form bodies in at least one mineral acid that is at least 1N; (b) supplying inert or oxidising gas into the mixture containing noble metal-containing catalyst form bodies and mineral acid; (c) introducing at least one oxidation agent, in solid or liquid form, into the mixture containing noble metal-containing catalyst form body and mineral acid; and (d) separating the form bodies from the liquid.
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公开(公告)号:US20170306442A1
公开(公告)日:2017-10-26
申请号:US15312731
申请日:2014-06-12
CPC分类号: C22B15/0071 , C22B3/04 , C22B3/08 , C22B11/04 , C22B13/04 , C22B19/22 , Y02P10/214 , Y02P10/234 , Y02P10/236
摘要: A hydrometallurgical process for the treatment of polymetallic ores and sulphide concentrates of copper and zinc, and by-products of lead and zinc from smelting plants, treated independently and/or as mixtures thereof, which contain relevant amounts of lead, copper, zinc, iron, gold and silver, such as the matte-speiss mixture of lead foundries, and copper cements from the purification processes of electrolytic zinc plants. Thee process allows the recovery of metallic copper, zinc, copper as copper and zinc basic salts, which may be hydroxides, carbonates, hidroxysulphates or mixtures thereof; the production of stable arsenic residues; and the effective and efficient recovery of Pb, Au and Ag as a concentrate of lead sulphide and/or lead, Au, and Ag sulphate.
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公开(公告)号:US09783870B2
公开(公告)日:2017-10-10
申请号:US14360088
申请日:2012-11-30
发明人: Ari Vaisanen , Jussi Valkonen , Siiri Peramaki , Ville Soikkeli , Risto Ryymin
IPC分类号: C22B59/00 , C01G55/00 , C01G5/00 , C01G7/00 , C22B7/02 , C22B3/00 , C01F17/00 , C22B3/06 , C22B3/08 , C22B3/16 , C22B3/44
CPC分类号: C22B59/00 , C01F17/0006 , C01G5/00 , C01G7/00 , C01G55/00 , C22B3/065 , C22B3/08 , C22B3/165 , C22B3/44 , C22B7/02 , C22B11/044 , Y02P10/214
摘要: Disclosed is a method for processing ash, particularly fly ash, in which method several elements are separated from the ash. In the method both noble metals and rare earth elements are separated.
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公开(公告)号:US20170247772A1
公开(公告)日:2017-08-31
申请号:US15509928
申请日:2015-09-25
申请人: AquaBlok, Ltd.
发明人: John H. Hull
CPC分类号: C21B3/02 , C21B5/023 , C21B2200/00 , C21C7/0025 , C21C7/0037 , C21C2200/00 , C22B1/243 , C22B1/248 , Y02P10/214 , Y02P10/216
摘要: Composite particles are used in combination with ore particles in an ore-refining or purification process, such as in a steel- or iron-making process. The composite particles comprise a core, which may be an aggregate of limestone, dolomite, or another ore particle. The core is surrounded by a coating layer of a metal dust and a binder. The metal dust may be iron oxide dust, which, along with limestone, is prevalent in the iron smelting process anyway. In this way, the composite particles help to recycle otherwise wasted and hazardous iron dust. The binder may be mineral clay such as bentonite, montmorillonite or kaolinite, and may comprise about 2-10% by weight of the particle.
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