In Situ Thiosulfate Generation for Gold Recovery

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Solution Overview

Problem

Conventional cyanidation processes for gold recovery face challenges with high reagent consumption, environmental concerns, and inefficiencies in extracting gold from sulfidic and carbonaceous ores, particularly due to preg robbing and double refractory nature of certain ore types, leading to high costs and gold losses.

Innovation Solution

A process involving partial oxidation of sulfidic ores to produce elemental sulfur, which is then reacted with sulfite or bisulfite to generate thiosulfate lixiviant in situ, allowing for efficient gold recovery using thiosulfate leaching, reducing reagent costs and environmental impact.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional cyanidation process is used for gold recovery, then gold can be solubilized and recovered, but high reagent consumption and environmental harm occur

Engineering Contradiction:
Improvegold recovery efficiencyVSAvoidenvironmental harm from cyanide
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent replaces cyanide with thiosulfate as the lixiviant, fundamentally changing the chemical parameter of the leaching agent. Thiosulfate leaching operates at different pH ranges (9.0-11.0) compared to cyanidation (9.5-11.0) and uses different complexing mechanisms, thereby achieving gold recovery without the environmental toxicity associated with cyanide

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs inexpensive reagents including sodium thiosulfate, copper sulfate, and ammonia to create an environmentally benign leaching system. These reagents are less hazardous and can be handled more safely than cyanide, reducing environmental risk while maintaining gold recovery effectiveness

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

2Productivity

If cyanidation is used on sulfidic ores, then gold recovery is attempted, but oxygen and acid consumption increase and operating temperatures rise

Engineering Contradiction:
Improvegold extraction from sulfidic oresVSAvoidoxygen and acid consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent modifies the chemical environment by introducing thiosulfate instead of cyanide, which changes the reaction kinetics and reagent consumption patterns. Thiosulfate leaching requires different oxygen concentrations and acidification levels compared to cyanidation, thereby reducing the metabolic burden on the bioleaching system

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses thiosulfate as an intermediary complexing agent that facilitates gold dissolution without requiring the extreme conditions needed for cyanide leaching. Thiosulfate forms stable gold complexes under milder conditions, acting as a mediator that reduces the need for high oxygen and acid inputs

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If thiosulfate leaching is used, then gold recovery improves on sulfidic and carbonaceous ores, but reagent losses occur due to oxidation to polythionates or sulfates

Engineering Contradiction:
Improvegold recovery from refractory oresVSAvoidthiosulfate reagent loss
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent implements a reagent regeneration system where polythionates and sulfates produced during leaching are converted back to thiosulfate. This closed-loop feedback mechanism recycles the oxidized thiosulfate species, reducing the need for continuous fresh thiosulfate addition and minimizing reagent loss

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent recovers and regenerates thiosulfate from oxidation products (polythionates and sulfates) through chemical reduction processes. Instead of discarding the oxidized reagents, they are converted back to active thiosulfate form, thereby recovering valuable reagent and reducing waste

Inventive Principle:
Principle #34Discarding and recovering

4Productivity

If ammonium thiosulfate is used for leaching, then gold dissolution occurs, but environmental concerns arise from copper and ammonia presence

Engineering Contradiction:
Improvegold dissolution rateVSAvoidenvironmental impact of copper and ammonia
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent adjusts the pH range to 9.0-11.0 and controls copper concentration to optimize gold dissolution while minimizing environmental impact. By carefully controlling these parameters, the system achieves effective leaching with reduced toxicity compared to conventional cyanidation or ammonium thiosulfate systems

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs sodium thiosulfate instead of ammonium thiosulfate, eliminating ammonia from the system. Sodium thiosulfate is equally effective for gold dissolution but does not produce ammonia emissions or require copper catalysis, thereby reducing environmental concerns while maintaining leaching efficiency

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach decreases oxygen and acid consumption, lowers operating temperatures, and effectively recovers gold from refractory sulfidic and carbonaceous ores by generating thiosulfate in situ, improving process economics and reducing gold losses.

Implementation Method 1

reacted with sulfite or bisulfite to generate thiosulfate lixiviant in situ

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

partial oxidation of sulfidic ores to produce elemental sulfur

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

efficient gold recovery using thiosulfate leaching

Methodology Applied
Scientific EffectLeaching: Solvation

Data Source

PatentUS7572317B2Thiosulfate generation in situ in precious metal recovery
Publication Date: 2009.08.11 BARRICK GOLD CORPORATION
  • US7572317B2 patent drawing
  • US7572317B2 patent drawing
  • US7572317B2 patent drawing

AI summary

Precious metal recovery by thiosulfate leaching where thiosulfate lixiviant is generated in situ employing elemental sulfur generated from partial oxidation of sulfidic precious metal-bearing feed and/or employing reactants from processing effluent.