Nanofiltration Membrane Separation of Cobalt and Nickel Salts

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Solution Overview

Problem

Existing methods for recovering cobalt and nickel from aqueous solutions, such as solvent extraction and ion exchange resin, are inefficient, environmentally impactful, and require large facilities due to low selective separability and the need for significant organic solvent use.

Innovation Solution

A method using a nanofiltration membrane with specific permeability characteristics and a polyamide separation layer to selectively separate and recover cobalt and nickel salts from an aqueous solution, enhanced by a complex forming step and multiple separation stages.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If solvent extraction method is used to recover nickel and cobalt, then recovery efficiency is improved, but environmental impact increases due to large amount of organic solvent use and facility scale increases

Engineering Contradiction:
Improverecovery efficiencyVSAvoidenvironmental impact
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent replaces the chemical solvent extraction system with a membrane filtration system. The nanofiltration membrane physically separates cobalt and nickel ions from the aqueous solution through size exclusion and charge-based rejection, eliminating the need for organic solvents while maintaining high recovery efficiency

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent employs a nanofiltration membrane with specific pore size and charge characteristics to selectively retain cobalt and nickel ions. The membrane's porous structure allows water and small molecules to pass through while blocking metal ions, enabling solvent-free separation and recovery

Inventive Principle:
Principle #31Porous materials

2Device complexity

If ion exchange resin method is used to recover nickel and cobalt, then recovery process is simplified, but selective separability decreases and additional solvent extraction is required

Engineering Contradiction:
Improveprocess simplificationVSAvoidselective separability
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent changes the separation mechanism from chemical ion exchange to physical membrane filtration with size and charge-based selectivity. By adjusting membrane parameters (pore size, surface charge) and operating conditions (pH, pressure), the system achieves high selective separability while maintaining process simplicity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The nanofiltration membrane combines multiple functional characteristics (porous structure, surface charge, hydrophilicity) into a single composite material that simultaneously provides both simplification and high selective separability, eliminating the need for subsequent solvent extraction steps

Inventive Principle:
Principle #40Composite materials

3Quantity of substance

If conventional nanofiltration membrane is used, then organic solvent permeability is improved, but sucrose permeability increases and selective separability decreases

Engineering Contradiction:
Improveisopropyl alcohol permeabilityVSAvoidselective separability
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The patent applies local quality by creating regions of different pore sizes and charge densities within the membrane structure. The membrane has hydrophilic channels that preferentially allow water and small organic molecules to pass while maintaining charged regions that reject metal ions through electrostatic repulsion

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent uses a specifically designed porous nanofiltration membrane with controlled pore size distribution and surface properties. The porous structure is optimized to allow passage of isopropyl alcohol and water while blocking cobalt and nickel ions through combined size exclusion and electrostatic repulsion mechanisms

Inventive Principle:
Principle #31Porous materials

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 method achieves high selective separability and efficient recovery of cobalt and nickel without large facilities, reducing environmental impact and operational costs.

Implementation Method 1

a separation step of separating, by using a nanofiltration membrane, a cobalt salt and a nickel salt from a rare metal-containing aqueous solution

Methodology Applied
Scientific EffectNanofiltration: Semipermeable Membrane

Implementation Method 2

when a 1,000 mg/L glucose aqueous solution, a 1,000 mg/L sucrose aqueous solution, and a 1,000 mg/L isopropyl alcohol aqueous solution, each having a pH of 6.5 and a temperature of 25° C., individually permeate through the nanofiltration membrane

Methodology Applied
Scientific EffectPermeation: Permeation

Implementation Method 3

the nanofiltration membrane includes a base material, a support membrane on the base material, and a separation function layer on the support membrane, and the separation function layer includes a polyamide

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS12403427B2Method of separating and recovering cobalt salt and nickel salt
Publication Date: 2025.09.02 TORAY INDUSTRIES INC
  • US12403427B2 patent drawing
  • US12403427B2 patent drawing
  • US12403427B2 patent drawing

AI summary

A method of separating and recovering a cobalt salt and a nickel salt includes a separation step of separating, by using a nanofiltration membrane, a cobalt salt and a nickel salt from a rare metal-containing aqueous solution containing at least both the cobalt salt and the nickel salt as rare metals, in which the nanofiltration membrane has a glucose permeability of 3 times or more a sucrose permeability, the sucrose permeability of 10% or less, and an isopropyl alcohol permeability of 50% or more when a 1,000 mg/L glucose aqueous solution, a 1,000 mg/L sucrose aqueous solution, and a 1,000 mg/L isopropyl alcohol aqueous solution, each having a pH of 6.5 and a temperature of 25° C., individually permeate through the nanofiltration membrane at an operating pressure of 0.5 MPa.