Galvanic Bath Segmentation for Zinc Deposition

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Solution Overview

Problem

The galvanic deposition of zinc-bearing layers from acidic zinc-bearing electrolytes is hindered by zinc anode depletion and passivation, leading to reduced effectiveness and contamination from foreign metal ions.

Innovation Solution

A galvanic bath with a cation-exchange membrane separating two cell chambers, one containing acidic deposition electrolyte and the other neutral or acidic anolyte, where foreign metal ions in the anolyte are replaced by zinc ions or protons using a cation exchanger or precipitant, preventing foreign metal ion passage and maintaining zinc ion levels.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If zinc anodes are used in acidic deposition electrolyte, then zinc ion supply is maintained, but anode passivation occurs and effectiveness is reduced

Engineering Contradiction:
Improvezinc ion supplyVSAvoidanode effectiveness
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

The galvanic bath is divided into two separate cell chambers: a deposition cell containing the acidic deposition electrolyte and an anolyte cell containing a neutral or acidic anolyte. The zinc anode is placed in the anolyte cell, separated from the deposition electrolyte by a cation-exchange membrane. This segmentation prevents passivation of the zinc anode while maintaining zinc ion supply to the deposition cell.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A cation-exchange membrane serves as an intermediary between the anolyte cell and deposition cell. It selectively transports zinc ions from the anolyte to the deposition electrolyte while blocking foreign metal ions. This intermediary mechanism maintains zinc ion supply without allowing contamination from foreign metal ions that would cause passivation.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Adaptability or versatility

If foreign metal ions are present in the electrolyte, then alloy deposition may occur, but contamination and passivation are caused

Engineering Contradiction:
Improvealloy deposition capabilityVSAvoidcontamination and passivation
Core Design Contradiction:
Adaptability or versatilityVSObject-affected harmful factors

Solution Approach 1:

The cation-exchange membrane acts as a selective intermediary that allows controlled transport of zinc ions while blocking foreign metal ions. This enables the system to maintain high zinc ion concentration in the deposition electrolyte without contamination from foreign metal ions that would cause passivation and reduce anode effectiveness.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

Different cell chambers are given different local qualities: the anolyte cell provides a neutral or acidic environment suitable for zinc anode operation, while the deposition cell maintains the specific composition needed for high-quality zinc layer deposition. This local differentiation optimizes each zone for its specific function.

Inventive Principle:
Principle #3Local quality

3Manufacturing precision

If membrane separation is implemented, then ion selectivity is improved, but device complexity increases

Engineering Contradiction:
Improveion selectivityVSAvoidbath structure
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The galvanic bath is segmented into two functional zones separated by a cation-exchange membrane. This segmentation provides ion selectivity while maintaining a relatively simple overall structure. The membrane is positioned to separate the anolyte cell from the deposition cell, creating distinct functional areas without excessive complexity.

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

This configuration enhances the deposition process by preventing anode passivation and maintaining zinc ion levels, reducing contamination and improving the quality and efficiency of zinc-bearing layer deposition.

Implementation Method 1

a membrane permeable to cations

Methodology Applied
Scientific EffectIon Exchange: Ion Exchange

Implementation Method 2

arrangement which replaces any foreign metal ions contained in the anolyte with zinc ions and/or protons

Methodology Applied
Scientific EffectCation Exchange: Ion Exchange

Implementation Method 3

an arrangement which replaces any foreign metal ions contained in the anolyte with zinc ions and/or protons

Methodology Applied
Scientific EffectIon Exchange: Ion Exchange

Implementation Method 4

The precipitant or a cation exchanger is used for this purpose

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 5

a current is applied between the substrate and at least one anode, which current is suitable for inducing the deposition of a zinc-bearing layer onto the substrate surface

Methodology Applied
Scientific EffectElectrodeposition: Electrodeposition

Data Source

PatentUS8282806B2Galvanic bath and process for depositing zinc-based layers
Publication Date: 2012.10.09 MACDERMID ENTHONE INC
  • US8282806B2 patent drawing
  • US8282806B2 patent drawing
  • US8282806B2 patent drawing

AI summary

The preceding invention concerns a galvanic bath as well as a method for depositing a zinc-bearing layer onto a substrate surface. According to the invention, it is provided that the galvanic bath be divided into at least two cell chambers, in which the division occurs by means of a cation-exchange membrane and one cell chamber includes an acidic deposition-electrolyte and the other cell chamber includes a neutral or acidic anolyte. The acidic anolyte here is at least partially removed from the cell chamber containing it and is stripped of the foreign metal ions contained in it by means of a cation-exchange arrangement.