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Treatment of base metal concentrate by a two-step bioleaching process

a bioleaching process and concentrate technology, applied in the field of treatment of a base metal containing concentrate, can solve the problems of recovering a base metal such as copper from a concentrate, which contains arsenic, using a bioleaching process, and achieve the effects of reducing the amount of cyanidation

Inactive Publication Date: 2007-02-08
BHP BILLITON
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The invention provides a method for treating a concentrate containing at least one base metal by bioleaching the concentrate using a primary and a thermophilic secondary bioleaching process. The method includes steps of preleaching the concentrate, processing a residue from the primary bioleaching process, and recovering the base metal from the solution produced by the bioleaching process. The method also includes controlling the pH of the concentrate and adding oxygen to the concentrate during the bioleaching process. The technical effects of the invention include maximizing the leaching of sulphides in the concentrate, minimizing the precipitation of arsenic, and maximizing the oxidation of sulphides minerals and mass loss."

Problems solved by technology

The recovery of a base metal such as copper from a concentrate, which contains arsenic, using a bioleaching process, can be problematic for it is necessary to avoid producing a bioleach residue which is contaminated with arsenic.

Method used

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  • Treatment of base metal concentrate by a two-step bioleaching process
  • Treatment of base metal concentrate by a two-step bioleaching process

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Embodiment Construction

[0027] In the method of the invention a concentrate 10 which contains a base metal such as copper and which may have a high arsenic content is subjected to a preleaching step 12. In this step the fresh concentrate is contacted with bioleach overflow solutions 14 and 16 respectively produced in subsequent primary and thermophilic secondary bioleaching stages 18 and 20.

[0028] The solutions 14 and 16 are rich in ferric and remove easily leachable copper from the feed 10. This ensures a lower residual copper tenor in the bioleaching tanks in the stages 18 and 20.

[0029] The product 22 of the preleaching stage is subjected to solid / liquid separation 24. An overflow solution 26 from the separation step 24 is directed to a pH adjustment stage 28 while the underflow 30, diluted with water 32 and raffinate 34 from a solvent extraction section 36, is fed to the primary bioleaching stage 18.

[0030] The purpose of the primary bioleaching stage 18 is to oxidise sulphide minerals in the feed and...

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Abstract

A method of recovering at least one base metal from a concentrate wherein a residue of a primary bioleach of the concentrate, under mesophilic and moderate themophilic conditions, is processed to recover at least one metal, and the base metal is recovered from a solution, produced by a secondary bioleach under thermophilic conditions, of a residue of the metal recovery process.

Description

BACKGROUND OF THE INVENTION [0001] This invention relates to the treatment of a base metal containing concentrate. [0002] The recovery of a base metal such as copper from a concentrate, which contains arsenic, using a bioleaching process, can be problematic for it is necessary to avoid producing a bioleach residue which is contaminated with arsenic. [0003] U.S. Pat. No. 6,461,577 addresses the problem of arsenic toxicity of extremely thermophilic bacterial cultures by means of a two-stage leaching process. In a first mesophilic stage a major part of the arsenic contained in the material being treated is leached from the material and then oxidised from As(III) to As(V). The remaining leachable metal content of the material being treated is leached out in a second thermophilic stage. The concentration of pentavalent arsenic falls quickly and the toxic effect thereof on the thermophilic bacteria thus falls at the same rate. [0004] It is desirable though to remove the soluble arsenic as...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C22B3/18C22B3/20C22B11/00C22B15/00
CPCC22B3/18C22B15/0089C22B15/0063C22B11/04Y02P10/20
Inventor BOWKER, CLINTHARVEY, PAUL
Owner BHP BILLITON
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