Solid-State Catalysts for Sulfide Leach Kinetics

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Solution Overview

Problem

Conventional low- and moderate-temperature leach processes for metal sulfides face issues such as surface passivation due to elemental sulfur production, which hinders leach kinetics and increases viscosity, and high-temperature processes require high oxygen pressures and produce undesirable byproducts like jarosite, limiting efficient recovery of precious metals.

Innovation Solution

The use of solid-state catalysts like colloidal hematite, goethite, and iron oxides at temperatures below 150°C to promote the oxidation of sulfides to sulfate, reducing elemental sulfur formation and enhancing leach efficiency by facilitating electron transfer and oxidation reactions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by stationary object

If low-temperature leach processes are used, then energy consumption is reduced, but surface passivation occurs due to elemental sulfur production which hinders leach kinetics

Engineering Contradiction:
Improveenergy consumptionVSAvoidleach kinetics
Core Design Contradiction:
Use of energy by stationary objectVSProductivity

Solution Approach 1:

A solid-state catalyst (iron oxide, goethite, or hematite) is introduced as an intermediary substance to facilitate the oxidation reaction between sulfide minerals and oxygen/ferrous ions. The catalyst provides alternative reaction pathways that prevent elemental sulfur formation while maintaining low operating temperatures, thus resolving the contradiction between energy efficiency and leach kinetics.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The invention changes the chemical parameters of the system by introducing catalytic iron oxide species that alter the reaction mechanism. This enables the process to operate at low temperatures without producing passivating elemental sulfur, as the catalyst promotes direct oxidation to sulfate rather than elemental sulfur formation.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If moderate-temperature leach processes are used, then leach reaction rates are improved, but slurry viscosity increases due to elemental sulfur production

Engineering Contradiction:
Improveleach reaction ratesVSAvoidslurry viscosity
Core Design Contradiction:
ProductivityVSStress or pressure

Solution Approach 1:

The solid-state catalyst acts as a mediator that enables efficient leach reaction rates at moderate temperatures without producing elemental sulfur. By providing an alternative catalytic pathway, the iron oxide catalyst prevents sulfur accumulation that would otherwise increase slurry viscosity and hinder mass transfer.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If high-temperature leach processes are used, then sulfide oxidation to sulfate is achieved, but high oxygen pressures are required and jarosite byproducts are formed

Engineering Contradiction:
Improvesulfide oxidation rateVSAvoidoxygen pressure requirements
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The iron oxide catalyst serves as an intermediary that facilitates sulfide oxidation at atmospheric or low oxygen pressures. The catalyst surface activates oxygen and promotes electron transfer, enabling high oxidation rates without requiring the high pressure conditions that would otherwise be necessary to achieve comparable reaction rates.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The introduction of solid-state catalysts changes the kinetic parameters of the oxidation reaction, allowing the process to proceed efficiently at lower oxygen partial pressures. The catalyst modifies the activation energy and reaction pathway, eliminating the need for high-pressure equipment while maintaining high sulfide conversion to sulfate.

Inventive Principle:
Principle #35Parameter changes

4Use of energy by stationary object

If low-temperature leach processes are used, then energy consumption is reduced, but soluble iron production increases which requires neutralization

Engineering Contradiction:
Improveenergy consumptionVSAvoidsoluble iron production
Core Design Contradiction:
Use of energy by stationary objectVSQuantity of substance

Solution Approach 1:

The solid-state iron oxide catalyst acts as an intermediary that promotes the reduction of soluble ferric iron to ferrous iron, which then re-oxidizes on the catalyst surface. This catalytic cycle maintains low soluble iron concentrations in the leach solution, eliminating the need for neutralization while preserving the energy efficiency of low-temperature operation.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 significantly increases sulfide oxidation rates to sulfate, reduces elemental sulfur production, and improves the efficiency of downstream cyanide leaching, allowing for the effective recovery of precious metals at lower temperatures and pressures, while minimizing side reactions and maintaining high oxidation performance.

Implementation Method 1

The use of solid-state catalysts like colloidal hematite, goethite, and iron oxides at temperatures below 150°C to promote the oxidation of sulfides to sulfate

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

promote the oxidation of sulfides to sulfate, reducing elemental sulfur formation and enhancing leach efficiency by facilitating electron transfer and oxidation reactions

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS11124858B2Solid-state catalysts for low or moderate temperature leach applications and methods thereof
Publication Date: 2021.09.21 F L SMIDTH & CO AS
  • US11124858B2 patent drawing
  • US11124858B2 patent drawing
  • US11124858B2 patent drawing

AI summary

A method for removing sulfate iron-containing compounds from a low- to moderate-temperature metal sulfide leach circuit (1) is disclosed. A reactor (6) within a chloride leach circuit (5) and which is preferably maintained at a temperature between 20 and 150 degrees Celsius may be provided with a catalyst (4) comprising a material selected from the group consisting of: colloidal hematite, colloidal goethite, particulate containing FeOOH, particulate containing α-FeOOH, particulate containing γ-FeOOH, particulate containing Fe2O3, particulate containing α-Fe2O3, particulate containing γ-Fe2O3, particulate containing Fe3O4, particulate containing Fe(OH)SO4, and a combination thereof. The catalyst (4) may also be used with heap leach and/or dump leach circuits (22), without limitation. Methods for using and generating the catalyst (4) are also disclosed. In some embodiments, the catalyst (4) may be used as an anti-frothing agent (e.g., for zinc leaching, without limitation).