首页> 外国专利> NITRIC ACID LEACHING PROCESS FOR THE RECOVERY OF COPPER, SILVER AND NICKEL FROM POLYSULFIDE ORES OF THE SAME

NITRIC ACID LEACHING PROCESS FOR THE RECOVERY OF COPPER, SILVER AND NICKEL FROM POLYSULFIDE ORES OF THE SAME

机译:用于从同一硫化物矿石中回收铜,银和镍的硝酸浸出工艺

摘要

Ni, Ag, Cu etc., may be very efficiently extracted from untreated sulphide ores and concentrates by subjecting to a pressure leaching process in which molten sulphur is formed as a separate fluid layer. This is then removed via a flash-tank and purified if necessary. Typical conditions using a 30-50% HNO3 leach soln. are 115-125 degrees C at 3.52-8.44 ats. gas (usually air or gas e.g., N2) pressure. Reaction time is 30-60 mins. with high efficiency i.e. 99.9%. NHO3 can be regenerated from nitrous fumes and returned to the closed system or converted to NH4NO3.
机译:Ni,Ag,Cu等可通过进行压力浸提工艺(其中熔融硫形成为独立的流体层)从未处理的硫化矿石和精矿中非常有效地提取。然后通过闪蒸罐将其除去,并在必要时进行纯化。使用30-50%HNO3浸出液的典型条件。在3.52-8.44 ats下为115-125摄氏度。气体(通常是空气或天然气,例如N2)压力。反应时间为30-60分钟。效率高,即> 99.9%。 NHO3可以从亚硝烟中再生并返回密闭系统或转化为NH4NO3。

著录项

  • 公开/公告号CA992749A

    专利类型

  • 公开/公告日1976-07-13

    原文格式PDF

  • 申请/专利权人 INTERNATIONAL ORE TECHNOLOGY INC.;

    申请/专利号CA19720158174

  • 发明设计人 POSEL JOHN G.;

    申请日0000-00-00

  • 分类号C22B3;C01B17/06;C22B3/44;

  • 国家 CA

  • 入库时间 2022-08-23 02:25:12

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