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    • 83. 发明授权
    • Recovery of non-ferrous metals by thermal treatment of solutions
containing non-ferrous and iron sulphates
    • 通过热处理含有铁和硫酸铁的溶液回收有色金属
    • US4415540A
    • 1983-11-15
    • US346837
    • 1982-02-08
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • C01G9/06C22B1/10C22B3/08C22B3/22C22B15/00
    • C22B3/22C22B1/10C22B15/0017C22B15/0071C22B15/0082C22B15/0086C22B19/22C22B3/08Y02P10/234Y02P10/236Y10S423/02Y10S423/16
    • The specification discloses a method for recovering non-ferrous metals such as zinc or copper iron from their concentrates, ores or any other metal containing materials into a solution containing these non-ferrous metals as sulphates and a minimal amount of dissolved iron. The resultant solution is suited without or with minimum pre-purification treatment for conventional electrowinning processes to recover such non-ferrous metals with less difficulties than the previous methods involving complex iron-removal processing. There is disclosed a method for recovering at least one non-ferrous metal soluble in sulphuric acid from a strong sulphuric acid solution containing said metal and iron as sulphates, said method comprising the following consecutive steps:subjecting said solution in a sub-divided form to thermal decomposition in a fluidized bed reactor at a temperature of from 600.degree. to 750.degree. C. with 20-150% excess air for an average retention time of 1-12 hours to obtain calcine containing ferric oxide and the sulphate of said non-ferrous metal;leaching said non-ferrous metal sulphate out from said calcine with water or dilute sulphuric acid solutions;separating said leach solution containing said non-ferrous metal sulphate from the residue; andrecovering said non-ferrous metal from said leach solution, via electrolysis or any other method.
    • 本说明书公开了一种从其浓缩物,矿石或任何其它含金属材料中回收有色金属如锌或铜铁的方法,该方法含有这些有色金属作为硫酸盐和最少量的溶解铁。 所得到的溶液适合于没有或具有最少的预纯化处理用于常规电解沉积方法以回收这种有色金属,而不是先前涉及复杂除铁处理的方法的困难。 公开了一种从硫酸盐中含有所述金属和铁的强硫酸溶液中回收至少一种可溶于硫酸的有色金属的方法,所述方法包括以下连续步骤:将分解形式的所述溶液 在流化床反应器中在600至750℃的温度下用20-150%过量的空气进行热分解,平均保留时间为1-12小时,得到含有氧化铁和所述有色金属硫酸盐的煅烧物 金属; 用水或稀硫酸溶液从所述煅烧物中浸出有色金属硫酸盐; 从残留物中分离含有所述有色金属硫酸盐的所述浸出溶液; 并通过电解或任何其他方法从所述浸出溶液中回收所述有色金属。
    • 86. 发明授权
    • Method and apparatus for forming a turbulent suspension spray from a
pulverous material and reaction gas
    • 用于从粉状材料和反应气体形成湍流悬浮液喷射的方法和装置
    • US4331087A
    • 1982-05-25
    • US105556
    • 1979-12-20
    • Kalevi J. KunttuLauno L. LiljaValto J. Makitalo
    • Kalevi J. KunttuLauno L. LiljaValto J. Makitalo
    • B01F5/00C22B1/10C22B5/14F23C3/00F23D1/02
    • C22B1/10B01F5/0057C22B5/14F23C3/008F23D1/02
    • A method for forming a turbulent suspension from a pulverous material and reaction gas by causing the pulverous material to flow downwards as an annular flow into the reaction chamber and by directing the reaction gas downwards inside the annular flow of the pulverous material, in which the suspension is produced by bringing the reaction gas into a high-force rotary motion and by then causing it, throttled, to discharge into the reaction chamber so that in the reaction chamber it meets on its outside a substantially vertically downward annular flow of the pulverous material, this flow being formed by utilizing the kinetic energy of the falling pulverous material on a convergent conical glide surface. An apparatus for forming a turbulent suspension from a pulverous material and reaction gas, which apparatus is adapted to be directed centrally downwards into the reaction chamber and consists of a feed pipe for the pulverous material, means for dividing the pulverous material and of a turbulence chamber for reaction gas, in which the feed pipe for the pulverous material has the shape of a downwards convergent cone, and inside the feed pipe there is an axially mounted turbulence chamber at the upper section of which there is a turbulence generator, and the lower section of the turbulence chamber comprises a cylindrical stabilizing member with a diameter less than that of the turbulence chamber.
    • 一种用于通过使粉状材料作为环形流向下流入反应室并通过将反应气体向下引导到粉状材料的环形流动流中而形成来自粉状材料和反应气体的湍流悬浮液的方法,其中悬浮液 通过使反应气体进入高力旋转运动并且然后使其被节流排放到反应室中,使得在反应室中,反应气体在其外部与粉状材料的基本垂直向下的环形流相交, 该流动通过利用落下的粉状材料在收敛的锥形滑动表面上的动能来形成。 一种用于从粉状材料和反应气体形成湍流悬浮液的装置,该装置适于被集中地定向到反应室中,并且由用于粉末材料的进料管组成,用于将粉状材料和湍流室 对于反应气体,其中用于粉末材料的进料管具有向下收敛锥体的形状,并且在进料管内部具有轴向安装的湍流室,其上部具有湍流发生器,下部 湍流室的直径小于湍流室的圆柱形稳定构件。
    • 88. 发明授权
    • Method for in-flight combustion of carbonaceous fuels
    • 碳质燃料的飞行燃烧方法
    • US4217132A
    • 1980-08-12
    • US837234
    • 1977-09-27
    • Harland L. BurgeJohn A. HardgroveWalter F. Krieve
    • Harland L. BurgeJohn A. HardgroveWalter F. Krieve
    • F23D1/00C10J3/46C21B7/16C22B5/14F23C3/00F23C5/32F23C7/02F23D1/02H02K44/08C22B1/10
    • F23C3/008C21B7/16C22B5/14F23C7/02H02K44/08Y10S423/16Y10S48/02
    • An apparatus and method for combusting carbonaceous fuels includes a reaction chamber defining a reaction zone and means for injecting fuel and oxidizer gas in a manner to produce in the reaction zone a wheel-type flow of the fuel-gas mixture. In preferred embodiments, the high velocity wheel-type flow operates to suspend fuel or other reactant particles in the swirling gas for residence times required for substantially complete reaction of the particles prior to the particles impinging against the walls of the reaction chamber. High angular veocities and the resulting centrifugal forces operate to remove substantially all slag from the gas as it approaches the downstream end of the reaction chamber. Operating temperatures are maintained at a level to avoid excessive volatilization of slag and thereby promote separation of liquid slag from the gaseous reaction products. Dense phase flow is employed for transporting pulverized reactants such as coal to the reaction chamber and injecting the reactants through a pintle fuel injector.
    • 用于燃烧含碳燃料的装置和方法包括限定反应区的反应室和用于在反应区中产生燃料 - 气体混合物的轮型流的方式喷射燃料和氧化剂气体的装置。 在优选实施例中,高速轮式流动操作以将涡流气体中的燃料或其它反应物颗粒悬浮在颗粒撞击反应室的壁之前的颗粒基本上完全反应所需的停留时间。 高角度压力,并且由此产生的离心力在其接近反应室的下游端时基本上从气体中除去所有的渣。 操作温度保持在一定水平,以避免炉渣过度挥发,从而促使液态炉渣与气态反应产物分离。 密相流用于将粉煤化反应物如煤运送到反应室,并通过枢轴燃料喷射器注入反应物。
    • 89. 发明授权
    • Process for the suspension smelting of sulfide concentrates
    • 硫化氢精矿悬浮冶炼工艺
    • US4168157A
    • 1979-09-18
    • US888777
    • 1978-03-21
    • Launo L. LiljaSimo A. I. MakipirttiValto J. Makitalo
    • Launo L. LiljaSimo A. I. MakipirttiValto J. Makitalo
    • C22B5/02C22B1/10C22B1/11
    • C22B5/02
    • A process for the suspension smelting of sulfide concentrates by causing a suspension flowing downwards in a suspension reaction zone to impinge against the surface of a melt below the suspension reaction zone in order to unload the solid and molten particles of the suspension into the melt and by causing the gases to flow further in the suspension reaction zone countercurrently in relation to the suspension in order to discharge the gases from the upper section of the suspension reaction zone, in which sulfide concentrate and oxygen or oxygen-enriched air are fed into the suspension reaction zone symmetrically and in the form of so dense a suspension spray that the iron oxide of the high-temperature suspension is in a molten state and absorbs the free oxygen present in the suspension before the suspension, at a temperature of at least 1400.degree. C., unloads into the melt, the heat is recovered indirectly in the suspension reaction zone from the gases rising symmetrically and smoothly around the suspension, and the melt is fed from the suspension reaction zone into a separate melt reaction space.
    • 一种通过使悬浮液在悬浮反应区中向下流动的悬浮液冲击悬浮反应区下方的熔体表面而悬浮熔融硫化物浓缩物的方法,以将悬浮液的固体和熔融颗粒卸载到熔体中,并通过 导致气体在悬浮反应区中进一步相对于悬浮液逆流地流动,以便从悬浮反应区的上部排出气体,其中将硫化物浓缩物和氧气或富氧空气进料到悬浮反应中 区域对称地并以如此致密的悬浮喷雾的形式使高温悬浮液的氧化铁处于熔融状态并在悬浮液之前在至少1400℃的温度下吸收悬浮液中存在的游离氧。 卸载到熔体中,在悬浮反应区间中间歇地从对称平稳地升高的气体中回收热量 悬浮液,并将熔体从悬浮反应区进料到单独的熔融反应空间中。