Phosphoric Metal Extractant for Selective Cobalt-Nickel Separation

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Solution Overview

Problem

Existing metal extractants used in wet extraction methods suffer from low selectivity and slow phase separation rates, making them inefficient for separating and recovering valuable metals like cobalt and nickel from aqueous solutions.

Innovation Solution

A metal extractant represented by Formula (I) with specific substituents having molecular weights of 100 or higher, including at least one with 160 or higher, and incorporating a basic structure derived from a phosphoric acid-based compound, enhances selectivity and phase separation rates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional metal extractants (alkylphosphonic acid monoalkyl esters with specific carbon chain lengths) are used for wet extraction, then metal ions can be extracted from water phase to organic phase, but the selectivity of metal ion extraction is insufficient

Engineering Contradiction:
Improveselectivity of metal ion extractionVSAvoidability to selectively separate specific metal ions
Core Design Contradiction:
Manufacturing precisionVSAdaptability or versatility

Solution Approach 1:

The patent applies parameter changes by modifying the molecular weight and structure of the extractant's substituent groups. Specifically, it uses substituents with molecular weights of 100 or more (preferably 160 or more), such as branched alkyl groups with 9 or more carbon atoms, to enhance the selectivity of metal ion extraction. This structural parameter change enables the extractant to preferentially bind with target metal ions like cobalt and nickel over other metal ions in the mixture.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conventional metal extractants are used for wet extraction, then metal ions can be extracted, but the liquid phase separation between water phase and oil phase takes a long period of time

Engineering Contradiction:
Improvephase separation rateVSAvoidtime required for liquid phase separation
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent applies parameter changes by modifying the physical properties of the extractant through specific molecular结构设计. The use of substituents with molecular weights of 100 or more (preferably 160 or more) creates sufficient density and viscosity differences between the organic phase and aqueous phase, enabling rapid phase separation within 5 minutes or less after mixing. This parameter optimization resolves the contradiction between extraction effectiveness and separation speed.

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

The new metal extractant achieves high selectivity and rapid phase separation, allowing for efficient extraction and recovery of specific metal ions, particularly cobalt and nickel, with selectivity ratios of 3.0 or more and recovery rates of 60% or more.

Implementation Method 1

the metal ions to which the metal extractant is coordinated are moved (extracted) to the organic phase

Methodology Applied
Scientific EffectSolvation: Solvation

Implementation Method 2

the metal extractant is represented by Formula (I)... R1 and R2 independently represent a hydrocarbon group

Methodology Applied
Scientific EffectComplexation: Chemical Bonding

Data Source

PatentEP4692383A1Metal extractant, method for separating and recovering metal ions using said metal extractant, and compound
Publication Date: 2026.02.11 FUJIFILM CORP
  • EP4692383A1 patent drawingFigure 1
  • EP4692383A1 patent drawing
  • EP4692383A1 patent drawing

AI summary

Provided are a compound and a metal extractant represented by Formula (I), and a separation recovery method of metal ions using the metal extractant. In Formula (I), R1 and R2 each independently represent a substituent having a molecular weight of 100 or higher, in which at least one of the substituents has a molecular weight of 160 or higher. YP represents a sulfur atom or an oxygen atom. Z represents a hydroxy group, a sulfanyl group, or a hydroxyaryl group. L represents a single bond, in which in a case where n represents 2 or more, L interposed between two adjacent P's represents a single bond or a linking group. n represents an integer of 1 to 6.