Selective Zinc Sulfide Precipitation via pH Segmentation

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Solution Overview

Problem

The existing methods for recovering zinc sulfide from aqueous solutions, such as process wash solutions and acid mine drainage, often result in co-precipitation of gypsum and aluminum hydroxide due to pH adjustment, reducing the purity and value of the zinc product.

Innovation Solution

A method that selectively precipitates zinc sulfide by adjusting the pH to allow iron oxy-hydroxide formation while avoiding copper and zinc precipitation, followed by controlled sulfide addition to separate copper and zinc sulfides without pH adjustment, maximizing hydrogen sulfide efficiency and recycling, and eliminating co-precipitation of contaminants.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If pH is adjusted to precipitate zinc sulfide, then zinc recovery is improved, but co-precipitation of gypsum and aluminum hydroxide occurs reducing product purity

Engineering Contradiction:
Improvezinc recoveryVSAvoidproduct purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent segments the metal recovery process into distinct pH stages: first precipitating iron at pH 2-3, then copper at pH 3.5-4.0, and finally zinc at pH 4.1-4.5. This segmentation allows selective precipitation of each metal at its optimal pH range, preventing co-precipitation of unwanted materials like gypsum and aluminum hydroxide that form at higher pH levels.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent utilizes parameter changes by precisely controlling pH as the critical parameter for selective precipitation. By adjusting pH to specific ranges (2-3 for iron, 3.5-4.0 for copper, 4.1-4.5 for zinc) and maintaining it within narrow windows, the process achieves selective metal recovery while avoiding conditions that would cause co-precipitation of contaminants.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If pH is adjusted with alkali to improve hydrogen sulfide uptake and precipitation kinetics, then precipitation rate is improved, but gypsum and aluminum hydroxide co-precipitate reducing product value

Engineering Contradiction:
Improveprecipitation rateVSAvoidproduct purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent applies preliminary action by removing iron and copper through controlled precipitation at lower pH levels before proceeding to zinc precipitation. This preliminary removal of interfering metals allows zinc to be precipitated at optimal pH without co-precipitation of aluminum hydroxide and gypsum, thereby maintaining both high precipitation rate and high product purity.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent employs parameter changes by precisely controlling pH within narrow ranges for each precipitation stage. By maintaining pH at 2-3 during iron precipitation, 3.5-4.0 during copper precipitation, and 4.1-4.5 during zinc precipitation, the process optimizes precipitation kinetics for each metal while preventing the formation of unwanted co-precipitates.

Inventive Principle:
Principle #35Parameter changes

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 yields a higher purity zinc sulfide product by avoiding co-precipitation of contaminants like gypsum and aluminum hydroxide, while optimizing hydrogen sulfide utilization and recycling, thereby enhancing the efficiency and purity of metal recovery.

Implementation Method 1

Hydrogen sulfide gas is employed to react with the solubilized metal salts (usually sulfates and/or chlorides)

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

The precipitation of heavy metals as metallic sulfides from aqueous solutions is a common and long practiced method of solution purification and metal recovery

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 3

The adjustment and maintenance of solution pH with alkali as required for selective sulfide precipitation of zinc at a pH of 4.1

Methodology Applied
Scientific EffectpH control:

Implementation Method 4

the co-precipitation of gypsum and other metals such as aluminum as aluminum hydroxide

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Data Source

PatentUS7862786B2Selective precipitation of metal sulfides
Publication Date: 2011.01.04 BARRICK GOLD CORPORATION
  • US7862786B2 patent drawing
  • US7862786B2 patent drawing

AI summary

A method for recovering zinc ions by selective zinc sulfide precipitation from an aqueous solution comprising zinc ions and metal ions of a metal that precipitates as a metal sulfide at a pH lower than a pH at which zinc ions precipitate as a zinc sulfide.