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    • 4. 发明授权
    • Recovery of V.sub.2 O.sub.5 and nickel values from petroleum coke
    • 从石油焦中回收V2O5和镍值
    • US4443415A
    • 1984-04-17
    • US391027
    • 1982-06-22
    • Paul B. QueneauRobert F. HogsettLeo W. BecksteadDale K. Huggins
    • Paul B. QueneauRobert F. HogsettLeo W. BecksteadDale K. Huggins
    • C01G31/00C22B34/22G21C19/46C01G53/00
    • C01G31/00C22B23/0415C22B34/22Y02P10/234
    • Vanadium and nickel values are selectively recovered from a petroleum coke residue by slurrying the coke in an aqueous solution of sodium carbonate providing an excess of the stoichiometric amount of sodium for formation of sodium vanadate and sodium sulfate, and then digesting the slurry at moderately elevated temperature in a pressurized autoclave under an oxygen overpressure supplying at least the stoichiometric amount of oxygen based on the vanadium and sulfur content of the slurry and advantageously sufficient additional oxygen to provide the thermal requirements of the digestion step by oxidation of carbon. In a continuous embodiment, the feed slurry temperature and feed solids content are adjusted according to a substantially inversely correlated relationship. The digestion temperature for a given total pressure and gas flow rate in the autoclave is adjusted to generate a pregnant liquor containing about 20 gpl to about 100 gpl of vanadate (V.sub.2 O.sub.5) from which at least about 50% of the input water has been converted to steam during the digestion. The vanadate liquor is separated from the digestion residue, which is then sequentially selectively leached for recovery therefrom of nickel and residual vanadium values.
    • 通过将焦炭在碳酸钠水溶液中浆化,提供过量的化学计量的钠以形成钒酸钠和硫酸钠,然后在适度升高的温度下消化浆料,从石油焦炭残渣中选择性回收钒和镍的值 在加压高压釜中,在氧气超压下,基于浆料的钒和硫含量至少提供化学计量的氧气,并且有利地具有足够的额外的氧气,以通过氧化碳来提供消化步骤的热需求。 在连续的实施方案中,根据基本上相反的关系来调整进料浆料温度和进料固体含量。 调节高压釜中给定的总压力和气体流速的消化温度以产生含有约20gp1至约100gp1钒酸盐(V2O5)的怀孕液体,至少约50%的输入水已转化为 蒸煮消化过程中。 将钒酸盐液体与消化残余物分离,然后依次选择性地浸提以从镍中回收镍和残留的钒值。
    • 7. 发明授权
    • Process for conditioning tungsten concentrates
    • 钨精矿调理工艺
    • US4338287A
    • 1982-07-06
    • US225912
    • 1981-01-19
    • Robert F. HogsettDale K. HugginsLeo W. Beckstead
    • Robert F. HogsettDale K. HugginsLeo W. Beckstead
    • C01G41/00C22B34/36
    • C01G41/00C22B34/36
    • A process for conditioning a tungsten concentrate containing tungsten as WO.sub.3, sulfur as sulfide, and calcite to fix at least a portion of the sulfur as calcium sulfate by reaction with the calcite, comprises providing a tungsten concentrate having a calcite content such that less than about 15 wt. % calcium sulfate based on the weight of the WO.sub.3 in the concentrate will be formed and heating the concentrate to a temperature of at least about 500.degree. C. in an oxidizing atmosphere to oxidize substantially all the sulfur in the concentrate to provide a conditioned concentrate having a calcium sulfate content less than about 15% based on the weight of the WO.sub.3, whereby the conditioned concentrate can be efficiently leached with alkali metal carbonates or hydroxides and the resulting alkali metal tungstate solution can be effectively treated to recover an ammonium tungstate solution.
    • 一种用于将含钨的钨浓缩物作为WO 3,硫作为硫化物和方解石调节以通过与方解石反应固定硫酸钙的至少一部分硫的方法,包括提供具有方解石含量的少于约 15重量% 将形成基于浓缩物中WO 3的重量的硫酸钙,并在氧化气氛中将浓缩物加热至至少约500℃的温度,以将浓缩物中的所有硫基本上全部氧化,从而提供具有 基于WO 3的重量计,硫酸钙含量小于约15%,由此可以用碱金属碳酸盐或氢氧化物有效地浸出调理的浓缩物,并且可以有效地处理所得的碱金属钨酸盐溶液以回收钨酸铵溶液。
    • 8. 发明授权
    • Process for metal recovery from steel plant dust
    • 钢厂粉尘回收金属工艺
    • US4610722A
    • 1986-09-09
    • US696977
    • 1985-01-31
    • Willem P. C. DuyvesteynRobert F. Hogsett
    • Willem P. C. DuyvesteynRobert F. Hogsett
    • C01G9/00C22B1/24C22B3/06C22B3/38C22B7/02C22B3/00
    • C22B17/04C01G9/003C22B1/2406C22B13/04C22B19/22C22B19/26C22B3/0063C22B3/06C22B7/02Y02P10/216Y02P10/234Y10S75/961
    • A process is provided for hydrometallurgical processing of steel plant dusts containing cadmium, lead, zinc, and iron values, along with impurities such as chloride and fluoride salts of sodium, potassium, magnesium, etc. The first step in the process involves leaching the dust in a mixed sulfate-chloride medium that dissolves most of the zinc and cadmium. Any iron and aluminum dissolved in this step is precipitated by oxidation and neutralization. Zinc is recovered from the resulting solution by solvent extraction which provides a raffinate which is recycled to the leaching step with a bleed stream also provided for recovery of cadmium and removal of other impurities from the circuit. The lead sulfate residue from the leaching step is leached with caustic soda, and zinc dust is used to cement the lead out from the caustic solution, which then joins the main solution for zinc recovery. The residue from the lead leaching step is mixed with iron-aluminum oxide precipitate and agglomerated into pellets using cement. These pellets can be charged into steel furnaces for iron recovery or stored as a nontoxic waste.
    • 提供了含有镉,铅,锌和铁价值的钢厂粉尘以及钠,钾,镁等氯化物和氟化物等杂质的湿法冶金加工的方法。该方法的第一步涉及浸出粉尘 在溶解大多数锌和镉的混合硫酸盐 - 氯化物介质中。 在该步骤中溶解的铁和铝通过氧化和中和沉淀。 通过溶剂萃取从所得溶液中回收锌,其提供残液,其提供用于回收镉和从回路中除去其它杂质的排出流再循环至浸出步骤。 来自浸出步骤的硫酸铅残留物用苛性钠浸出,锌粉用于从苛性碱溶液中水解铅,然后将其与主溶液接合以进行锌回收。 来自铅浸出步骤的残渣与铁 - 氧化铝沉淀物混合并用水泥凝聚成颗粒。 这些颗粒可以装入钢铁炉中用于铁回收或作为无毒废物储存。