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Chloride assisted hydrometallurgical extraction of metal

a hydrometallurgical extraction and chloride technology, applied in the direction of inorganic chemistry, silver compounds, dissolving, etc., can solve the problems of large acid production quantities, expensive neutralization, and unfavourable low-grade concentrates

Inactive Publication Date: 2001-07-03
CESL LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

According to the invention, there is provided a process for the extraction of metal from a sulphide ore or concentrate, comprising the steps of subjecting the ore or concentrate to pressure oxidation in the presence of oxygen and an acidic chloride solution to obtain a resulting pressure oxidation filtrate and an insoluble basic metal sulphate salt, characterized in that the pressure oxidation is conducted in the presence of a source of bisulphate or sulphate ions which is selected from the group consisting of sulphuric acid and a metal sulphate which hydrolyzes in the acidic solution and wherein the amount of the source of bisulphate or sulphate ions which is added contains at least the stoichiometric amount of sulphate or bisulphate ions required to produce the basic metal sulphate salt less the amount of sulphate generated in situ in the pressure oxidation.

Problems solved by technology

Hydrometallurgical treatment of copper sulphide ores, such as chalcopyrite (CuFeS.sub.2), is problematical because the severe conditions required in a pressure oxidation step for the effective leaching of copper from these ores results in oxidation of the sulphide in the ore to sulphate, resulting in the generation of large amounts of acid which requires expensive neutralization.
This is particularly unfavourable for low grade concentrates, where the S / Cu ratio is high.

Method used

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  • Chloride assisted hydrometallurgical extraction of metal
  • Chloride assisted hydrometallurgical extraction of metal
  • Chloride assisted hydrometallurgical extraction of metal

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Embodiment Construction

The process according to the invention is flexible enough to treat a range of copper concentrates in which the grade of copper varies from low, i,e. about 15% copper or less, to high grade, i.e. about 35% copper or more.

Broadly, the process comprises a pressure oxidation stage, an atmospheric leach stage, one or more solvent extraction stages and an electrowinning stage. Different grades of concentrate require different treatment in the pressure oxidation stage, requiring different modes of operation. These modes of operation are termed Mode A and Mode B, respectively. In Mode A, which is effective when high grade copper ores are leached, copper is not leached in the pressure oxidation stage. In Mode B, which is effective when medium and low grade copper ores are leached, copper is leached in the pressure oxidation stage.

Each of the two modes of operation will now be described in turn.

Process Mode A

FIG. 1 is a flow diagram of Mode A. The process comprises a pressure oxidation stage ...

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Abstract

A process for the extraction of a metal from an ore or concentrate comprises subjecting the ore or concentrate to pressure oxidation in the presence of oxygen and an acidic solution containing halogen ions and a source of bisulphate or sulphate ions, such as H2SO4. The metals which can be extracted by the process comprises copper as well as non-cuprous metals such as zinc, nickel and cobalt. During pressure oxidation the metal may be precipitated as an insoluble basic salt, such as basic copper sulphate, or substantially completely solubilized and precipitated later as the basic metal salt.

Description

FIELD OF THE INVENTIONThis invention relates to the hydrometallurgical treatment of metal ores or concentrates. In particular, it relates to the extraction of metals from ores in the presence of halogen ions, such as chloride ions. It also relates to the extraction of nickel and cobalt from laterite ores.BACKGROUND OF THE INVENTIONHydrometallurgical treatment of copper sulphide ores, such as chalcopyrite (CuFeS.sub.2), is problematical because the severe conditions required in a pressure oxidation step for the effective leaching of copper from these ores results in oxidation of the sulphide in the ore to sulphate, resulting in the generation of large amounts of acid which requires expensive neutralization. Attempts have been made to render the sulphide concentrate leachable under relatively milder conditions under which the sulphide would only be oxidized to elemental sulphur and not all the way through to sulphate. These attempts include the pretreatment of the concentrate prior to...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): C22B3/26C22B11/00C22B3/06C22B3/08C22B3/20C22B3/38C22B3/00C22B15/00C22B3/10B01D11/00B01D11/02C01G1/00C22B1/00C25C1/00
CPCC22B3/06C22B3/08C22B3/10C22B3/20C22B11/00C22B15/0067C22B15/0069C22B15/0071C22B15/0084C22B15/0089C22B19/22C22B19/26C22B23/0415C22B23/0423C22B23/043C22B23/0453C22B3/24Y02P10/20C22B3/26C22B3/3842
Inventor JONES, DAVID L.
Owner CESL LIMITED
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