Waste Metal Recovery Using Segmented Ammonia and Thiosulfate Leaching

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Solution Overview

Problem

Existing methods for recovering copper, gold, and other valuable metals from waste materials, particularly E-waste, are inefficient and costly.

Innovation Solution

A method involving ammonia-based lixiviant for leaching copper and base metals, followed by electrowinning, and thiosulfate leaching for noble metals, with countercurrent flows in each circuit to enhance recovery efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a single leaching method is used to recover all metals from waste materials, then the process is simpler, but the recovery efficiency and purity of individual metals deteriorates

Engineering Contradiction:
Improveprocess complexityVSAvoidmetal recovery efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The patent divides the metal recovery process into two separate leaching circuits: a first leaching circuit using ammonia-based lixiviant for base metals (copper, nickel, cobalt) and a second leaching circuit using thiosulfate-based lixiviant for precious metals (gold, platinum). This segmentation allows each circuit to be optimized for specific metal types, improving recovery efficiency and purity while maintaining manageable process complexity through modular design.

Inventive Principle:
Principle #1Segmentation

2Ease of operation

If conventional single-circuit leaching is used, then the equipment and operation are simpler, but the separation precision and purity of recovered metals deteriorates

Engineering Contradiction:
Improveoperation simplicityVSAvoidmetal separation precision
Core Design Contradiction:
Ease of operationVSManufacturing precision

Solution Approach 1:

The patent implements separate leaching circuits for base metals and precious metals, enabling selective recovery and high-purity separation. The first circuit recovers base metals with high efficiency, while the second circuit specifically targets precious metals, achieving superior separation precision that would be impossible in a single mixed circuit.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent uses a solid-liquid separator as an intermediary between the two leaching circuits. This separator divides the treated waste material stream, directing base metal-containing residues to the first circuit and precious metal-containing residues to the second circuit, thereby enabling precise metal separation while maintaining operational simplicity through standardized separation equipment.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Ease of manufacture

If traditional metal recovery methods are used, then the process cost is lower in terms of equipment investment, but the overall cost-effectiveness and recovery value deteriorates due to lower efficiency

Engineering Contradiction:
Improveequipment investment costVSAvoidcost-effectiveness
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent employs segmented leaching circuits with metal-specific reagents (ammonia for base metals, thiosulfate for precious metals), maximizing the recovery value of each metal type. This approach improves cost-effectiveness by ensuring high recovery rates of valuable precious metals while using readily available, low-cost reagents, thereby achieving superior returns on equipment investment compared to conventional single-circuit methods.

Inventive Principle:
Principle #1Segmentation

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

Enhances the recovery of copper and noble metals from waste materials with improved efficiency and reduced costs by utilizing ammonia and thiosulfate leaching processes.

Implementation Method 1

contacting a waste material feed stream with a first ammonia-based lixiviant adapted to leach copper and other base metals

Methodology Applied
Scientific EffectComplexation:

Implementation Method 2

ammonia leaching in the first leaching circuit to leach the copper and the other base metals

Methodology Applied
Scientific EffectLeaching:

Implementation Method 3

thiosulfate leaching in the second leaching circuit to leach the at least one noble metal from the treated waste material feed stream

Methodology Applied
Scientific EffectLeaching:

Implementation Method 4

using Cu2+ as an oxidant for (a) leaching the copper and the other base metals from the waste material feed stream

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 5

using electrowinning in the recovering of the copper metal from the first ammonia-based lixiviant

Methodology Applied
Scientific EffectElectrowinning: Electrodeposition

Implementation Method 6

using a precipitation reaction, such as a Merrell Crowe reaction, for the recovery of gold from the second lixiviant

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS12612680B2Extraction of copper, gold and other elements from waste materials
Publication Date: 2026.04.28 UNIVERSITY OF KENTUCKY RESEARCH FOUNDATION
  • US12612680B2 patent drawing
  • US12612680B2 patent drawing
  • US12612680B2 patent drawing

AI summary

A method for recovering metals from waste materials includes steps of contacting a waste material feed stream with a first lixiviant adapted to leach copper and other base metals from the waste material feed stream and provide a treated waste material feed stream, recovering copper metal from the first lixiviant, contacting the treated waste material stream with a second lixiviant adapted to leach noble metals from the treated waste material feed stream and recovering gold from the second lixiviant.