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    • 45. 发明申请
    • SELECTIVE LEACH RECOVERY OF MINERALS FROM COMPOSITE ORES
    • 从复合矿石中选择性的矿物矿物回收
    • US20120177551A1
    • 2012-07-12
    • US13390960
    • 2010-08-17
    • Robert A. GeislerMadhav P. Dahal
    • Robert A. GeislerMadhav P. Dahal
    • C22B3/04C22B3/08C22B19/00C22B3/06C22B47/00C22B3/16C22B3/10
    • C22B3/165C22B13/04C22B26/20C22B26/22C22B47/00C22B47/0063Y02P10/234
    • Calcium (Ca), manganese (Mn) and magnesium (Mg) carbonate plus lead (Pb) and zinc (Zn) sulphide minerals in a permeable host, crushed ore, concentrates or as mine discharge tailing are selectively solution mined (in-situ or ex-situ) with a selected acid e.g. acetic acid to extract Ca, Mn, and Mg followed by multivalent oxidizing salts e.g. ferric salts to extract Pb and Zn sequentially. For in-situ leaching, an inter relationship has been identified between pressure, temperature, target depth and leachate concentration such that carbonate leaching is performed in a manner to prevent carbon dioxide gas (CO2) discharge thereby plugging host rock permeability avenues to preclude further leaching. This requires controlling the rate of acetic acid leaching to be in step with availability of solution to dissolve the resulting discharged CO2. Sulphide leaching is subsequently conducted on the carbonate-depleted host. The two resulting leachates are chemically treated to selectively recover extracted minerals as value added industrially ready products. The in situ method is particularly advantageous in preparing the high purity manganese products necessary for lithium ion batteries because it prevents occurrence of very fine metallic particles in the products that may happen during conventional mining. Alternatively, the in situ carbonate recovery steps can be independently employed; all in an environmentally friendly manner.
    • 选择性地开采了可渗透的主体,粉碎的矿石,浓缩物或排矿尾矿中的钙(Ca),锰(Mn)和镁(Mg)碳酸盐加铅(Pb)和锌(Zn) 用选择的酸例如 乙酸提取Ca,Mn和Mg,然后是多价氧化盐,例如 铁盐依次提取Pb和Zn。 对于原位浸出,已经确定了压力,温度,目标深度和渗滤液浓度之间的相互关系,使得碳酸盐浸出以防止二氧化碳气体(CO 2)排放的方式进行,从而堵塞主体岩石渗透性通道以排除进一步浸出 。 这需要控制乙酸浸出的速度与溶液的可用性一致,以溶解所产生的排出的CO 2。 随后在碳酸盐贫化的宿主上进行硫化物浸出。 化学处理两种生成的浸出液,以选择性回收提取的矿物质作为工业增值产品。 原位法在制备锂离子电池所需的高纯度锰产品方面特别有利,因为它防止在常规采矿过程中可能发生的产品中发生非常细小的金属颗粒。 或者,可以独立地使用原位碳酸盐回收步骤; 都以环保的方式。
    • 46. 发明申请
    • Treated manganese ore, process for producing the same, and use thereof
    • 处理的锰矿石,其生产方法及其用途
    • US20010033823A1
    • 2001-10-25
    • US09824768
    • 2001-04-04
    • TOSOH CORPORATION
    • Minoru KuniyoshiKouya Honjo
    • C01D005/04C01B017/96
    • C01G45/10C22B3/08C22B47/0063C25B1/21H01M4/50H01M4/52Y02P10/234
    • An object of the invention is to provide: a treated manganese ore for use in manganese sulfate production therefrom which has a high degree of manganese dissolution when dissolved in sulfuric acid and which can hence be effective in reducing the amount of slags generating in a production step and can be reduced in potassium content according to need; a process for producing the treated manganese ore easily and economically; manganese dioxide which is useful in primary batteries, secondary batteries, etc.; and a process for easily producing the manganese dioxide. A treated manganese ore for use in producing manganese sulfate therefrom, the treated ore having a degree of manganese dissolution of 98.0% by weight or higher based on the manganese contained in the treated manganese ore when dissolved in sulfuric acid; a process for producing the treated ore; manganese dioxide obtained from the treated ore; and a process for producing the manganese dioxide are described.
    • 本发明的目的是提供:用于硫酸锰生产的处理过的锰矿石,其在溶解在硫酸中时具有高的锰溶解度,因此可以有效地减少在生产步骤中产生的炉渣的量 并可根据需要降低钾含量; 一种容易经济地生产经处理的锰矿石的方法; 可用于一次电池,二次电池等的二氧化锰; 以及容易制造二氧化锰的方法。 一种用于生产硫酸锰的经处理的锰矿石,当处理的锰矿溶解在硫酸中时,其处理矿石的锰溶解度为98.0重量%或更高,基于处理过的锰矿石中所含的锰; 一种生产经处理的矿石的方法; 从经处理的矿石中获得的二氧化锰; 并描述了制备二氧化锰的方法。
    • 48. 发明授权
    • Process for the treatment of complex manganese ores, such as marine
nodules
    • 处理复杂锰矿石的方法,如海洋结节
    • US4620964A
    • 1986-11-04
    • US742003
    • 1985-06-06
    • Odile PintoHenri Scoazec
    • Odile PintoHenri Scoazec
    • B01D11/02C22B3/00C22B3/04C22B15/00C22B23/00C22B47/00C01G3/12C01G51/00C01G53/11
    • C22B47/0063C22B47/00Y10S423/04
    • A process for the treatment of a complex manganese ore, wherein it comprises the following stages:(a) crushing the ore,(b) subdividing the crushed ore into a first part and a second part,(c) preparing the first pulp from the first part of the crushed ore,(d) reacting the first pulp with a reducing agent to obtain a manganous sulphate solution,(e) separating the liquid phase constituted by the thus obtained manganous sulphate solution from the solid phase of the thus treated first pulp,(f) preparing a second pulp from the second part of the crushed ore,(g) subjecting the second pulp to a solubilization treatment of the nickel, copper and cobalt by reacting it hot with sulphuric acid and the manganous sulphate solution obtained in stage (e),(h) separating the liquid phase and the solid phase of the thus treated second pulp, and(i) recovering the nickel, copper and cobalt from the liquid phase separated in stage (h).
    • 一种处理复杂锰矿石的方法,其中包括以下阶段:(a)粉碎矿石,(b)将粉碎的矿石细分成第一部分和第二部分,(c)从第一部分和第二部分制备第一个纸浆 (d)使第一纸浆与还原剂反应,得到硫酸锰溶液,(e)将如此得到的硫酸锰溶液所构成的液相与经处理的第一纸浆的固相分离 (f)从粉碎矿石的第二部分制备第二纸浆,(g)使第二纸浆通过热与硫酸反应并在阶段中获得的硫酸锰溶液对第二纸浆进行溶解处理, (e),(h)分离如此处理的第二纸浆的液相和固相,和(i)从阶段(h)中分离的液相中回收镍,铜和钴。
    • 49. 发明授权
    • Processes relating to the extraction of metals from laterites and ocean
manganese nodules
    • 与红土和海洋锰结核提取金属有关的过程
    • US4545816A
    • 1985-10-08
    • US616841
    • 1984-06-04
    • Alkis S. Rappas
    • Alkis S. Rappas
    • C22B3/00C22B3/04C22B3/06C22B3/08C22B3/16C22B15/00C22B47/00C22B23/04C22B15/08
    • C22B23/0415C22B15/0067C22B15/0089C22B3/06C22B3/08C22B3/1683C22B47/00C22B47/0063Y02P10/234Y02P10/236Y10S423/04
    • The selective leaching of metal ions from various iron oxide and manganese oxide containing ores employs intermediary solutions. The leaching processes are based upon a redox acid leach step employing stabilized cuprous ions and, in one instance, a combination thereof with ferrous ions. Leaching is conducted at low temperatures, up to about 90.degree. C. and low pressures, up to about 1.5 MPa and at a pH of about 1.5 to 2.5. Nickel and cobalt recoveries from the ores, employing these processes, will usually equal or exceed 90 percent. The intermediary solutions comprise stabilized acidic cuprous ions Cu.sup.+ L wherein L is a stabilizing ligand selected from the group consisting of CO, XRCN and Cl.sup.-, X being --H or --OH and R being aliphatic having from one to about four carbon atoms. In at least one process, ferrous ions are introduced for a separate leaching step. Additional steps include regeneration of the lixiviant cuprous ion solutions and removing a portion of the copper ions from the copper ion solution before or after the step of regenerating. Several processes for the regeneration are possible employing quinolic compounds, H.sub.2, CO or syngas as reductants.
    • 来自各种氧化铁和含氧化锰的矿石的金属离子的选择性浸出采用中间解决方案。 浸出过程基于使用稳定的亚铜离子的氧化还原浸出步骤,在一种情况下,其与亚铁离子的组合。 浸出在低至约90℃,低压,高达约1.5MPa,pH约1.5至2.5的低温下进行。 使用这些工艺的矿石的镍和钴回收率通常会等于或超过90%。 中间溶液包含稳定的酸性亚铜离子Cu + L,其中L是选自CO,XRCN和Cl-的稳定配体,X是-H或-OH,R是具有1至约4个碳原子的脂族基。 在至少一个方法中,引入亚铁离子用于单独的浸出步骤。 另外的步骤包括在再生步骤之前或之后再生氯化锂离子溶液并从铜离子溶液中除去一部分铜离子。 使用喹啉化合物,H 2,CO或合成气作为还原剂的几种再生方法是可能的。
    • 50. 发明授权
    • Extracting metal values from manganiferous ocean nodules
    • 从锰矿海洋结节中提取金属值
    • US4026773A
    • 1977-05-31
    • US648927
    • 1976-01-14
    • Antoine L. Van Peteghem
    • Antoine L. Van Peteghem
    • B01D11/04C22B3/00C22B3/04C22B15/00C22B23/00C22B34/00C22B47/00C01G51/00C01G45/02C01G53/00C25C1/12
    • C22B15/0069C22B15/0093C22B47/0063C22B47/0081Y02P10/236Y10S423/04
    • Metal values are extracted from manganiferous ocean floor nodule ore by treating the ore with hydrochloric acid, thereby producing chlorine and a starting pulp containing a solution of the metal chlorides and a solid residue. The starting pulp is subjected to at least two subsequent acidifications with HCl, each acidification being followed by addition of fresh ore, thereby producing chlorine and a final pulp containing a concentrated solution of metal chlorides and a solid residue. The solid residue is separated from the concentrated solution and substantially all the metal values, except manganese and alkali and alkaline earth metals, are separated from the solution. The manganese is separated from the solution by treatment with chlorine, at least the major portion of which was produced in the preceding leaching steps, while maintaining the solution at a pH of between about 3 and 7 by addition of a neutralizing agent such as MgO or Mg(OH).sub.2 whereby the manganese is precipitated in the form of MnO.sub.(1.sub.+x) in which x is between 0.5 and 0.7. The manganiferous precipitate is separated from the resulting solution of magnesium chloride and the latter is pyrohydrolysed in the atomized state to regenerate the neutralizing agent and HCl, which can be recycled.
    • 通过用盐酸处理矿石,从锰矿海底结核矿石中提取金属值,从而产生氯和含有金属氯化物和固体残渣的溶液的起始纸浆。 起始纸浆经HCl至少两次随后的酸化,每次酸化后,加入新鲜矿石,从而产生氯和含有金属氯化物和固体残余物浓缩溶液的最终纸浆。 将固体残余物与浓缩溶液分离,除了锰和碱金属和碱土金属之外,基本上所有的金属值都与溶液分离。 通过用氯处理将锰从溶液中分离出来,其中至少其主要部分在前面的浸出步骤中产生,同时通过加入中和剂例如MgO或其它溶液将溶液保持在约3和7之间的pH Mg(OH)2,由此锰以MnO(1 + x)的形式沉淀,其中x在0.5和0.7之间。 从得到的氯化镁溶液中分离锰矿沉淀物,并将其以雾化状态进行热解,以再生中和剂和HCl,其可再循环。