Electrolytic cell for recovery of metals from metal bearing materials
    1.
    发明授权
    Electrolytic cell for recovery of metals from metal bearing materials 失效
    用于从金属轴承材料回收金属的电解槽

    公开(公告)号:US4639302A

    公开(公告)日:1987-01-27

    申请号:US638485

    申请日:1984-07-26

    申请人: Peter K. Everett

    发明人: Peter K. Everett

    CPC分类号: C25C7/02

    摘要: An electrolytic cell for recovery of metal from mineral ores or concentrates comprising a tank for holding a slurry of electrolyte and the mineral ore or concentrates. Vertical anodes are radially disposed in the tank and vertical cathodes enclosed in diaphragm bags are interposed between the anodes. Agitating means are located in the tank below the anodes and cathodes. Metal is removed from a central collecting container in the tank by pump means.

    Production of lead from ores and concentrates
    2.
    发明授权
    Production of lead from ores and concentrates 失效
    从矿石和精矿生产铅

    公开(公告)号:US4381225A

    公开(公告)日:1983-04-26

    申请号:US220031

    申请日:1980-12-09

    申请人: Peter K. Everett

    发明人: Peter K. Everett

    IPC分类号: C25C1/00 C25C1/18 C25C5/02

    CPC分类号: C25C5/02 C25C1/18

    摘要: Lead is selectively recovered electrolytically from a mixture of metal sulphides in an aqueous chloride electrolyte by controlling the rate of agitation and oxidation conditions so that metal sulphides other than lead remain substantially undissolved.

    摘要翻译: PCT No.PCT / AU80 / 00001 Sec。 371日期1980年12月9日第 102(e)日期1980年12月8日PCT提交1980年4月2日PCT公布。 出版物WO80 / 02164 日期为1980年10月16日。通过控制搅拌速率和氧化条件,从氯化物电解质中的金属硫化物的混合物中电解回收,以使除铅以外的金属硫化物基本上不溶解。

    Programing mechanism
    3.
    发明授权
    Programing mechanism 失效
    编程机制

    公开(公告)号:US3553483A

    公开(公告)日:1971-01-05

    申请号:US3553483D

    申请日:1968-12-09

    发明人: JARVIS JOHN R

    摘要: A programming mechanism is disclosed for controlling the application of power to apparatus performing successive steps in a process. The mechanism includes an electronic timer for controlling the time period of each step. The timer includes an R-C timing circuit, the R-C constant of which may be adjusted to any suitable value for each different step of the process by connecting into the circuit a different R-C circuit element, such as a variable resistor for each step in the process that the circuit controls. For this purpose, a multisection, multiposition stepping switch is connected to the R-C timing circuit and a different variable resistor is connected to one or more of the terminals of the stepping switch so that as the switch is stepped to the next position a different R-C timing constant may be provided to control the time period of the electronic timer.

    Production of zinc from ores and concentrates
    4.
    发明授权
    Production of zinc from ores and concentrates 失效
    从矿石和精矿生产锌

    公开(公告)号:US4684450A

    公开(公告)日:1987-08-04

    申请号:US871402

    申请日:1986-05-06

    申请人: Peter K. Everett

    发明人: Peter K. Everett

    CPC分类号: C25C1/16

    摘要: Recovering zinc from zinc bearing ore or concentrate (1) in an electrolic cell (3) which includes a cathode (5) containing cathode compartment (16) and an anode (4) containing anode compartment (2). The cathode and anode compartments are defined by interposing between such compartments an ion-selective membrane (6) capable of preventing migration of ionic copper from anode compartment (2) to cathode compartment (16). Process includes forming in anode compartment (2) a slurry of ore or concentrate (1) with a chloride and copper-ion containing solution, intimately mixing oxygen bearing gas (7) with the slurry, maintaining the mixture substantially at atmospheric pressure and at a temperature up to the boiling point of the solution, and maintaining the pH of the mixture from 1 to 4. The resultant solution is rich in solubilized zinc. At least a portion of the mixture is withdrawn and resultant solution (12) separated therefrom. Zinc bearing ore or concentrate (1) is contacted with solution (12) precipitating ionic copper therefrom. Resultant solution (15) is introduced to the cathode compartment (16) and zinc electrochemically recovered at the cathode (5).

    摘要翻译: PCT No.PCT / AU85 / 00230 Sec。 371日期:1986年5月6日 102(e)日期1986年5月6日PCT提交1985年9月20日PCT公布。 公开号WO86 / 02107 PCT 日期:1986年4月10日。将含锌矿石或浓缩物(1)的锌从含有阴极(5)的阴极(5)和含有阳极室(2)的阳极(4)的电解槽(3) 。 阴极和阳极室通过在这些隔室之间插入能够防止离子铜从阳极室(2)迁移到阴极室(16)的离子选择膜(6)来限定。 方法包括在阳极室(2)中将矿石或浓缩物(1)的浆料与含氯离子和含铜离子的溶液形成,将含氧气体(7)与浆料充分混合,将混合物保持在大气压和 温度达到溶液的沸点,并保持混合物的pH为1至4.所得溶液富含溶解的锌。 将混合物的至少一部分取出并从中分离得到的溶液(12)。 含锌矿石或浓缩物(1)与溶液(12)接触,沉淀离子铜。 将所得溶液(15)引入阴极室(16),并在阴极(5)处电化学回收锌。