Bipolar Membrane Galvanic Bath for Zinc Deposition

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Solution Overview

Problem

Alkaline galvanic baths used for zinc or zinc alloy deposition face issues such as color change due to decomposition products, leading to uneven layer thickness and bubble formation, requiring continuous cleaning, which is time-consuming and costly, and the use of ion exchange membranes results in volume excess and cyanide formation.

Innovation Solution

An alkaline galvanic bath with a bipolar membrane separating the anode and cathode compartments, along with an additional ion exchange membrane to prevent anodic decomposition and self-form sodium hydroxide, reducing organic additive oxidation and maintaining high metal deposition efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If organic brighteners and wetting agents are added to enable deposition of functional layers, then the bath can deposit zinc and zinc alloys, but the organic components decompose at the anode causing color change and requiring continuous cleaning

Engineering Contradiction:
Improvedeposition capabilityVSAvoiddecomposition products
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The bath is divided into two separate compartments by an ion-exchange membrane: the cathode compartment containing organic additives for deposition, and the anode compartment free of organics. This segmentation prevents organic decomposition at the anode while maintaining deposition capability at the cathode.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The harmful anodic decomposition function is extracted from the main bath by placing the anode in a separate compartment without organic additives, while the cathode compartment retains the necessary organic components for functional layer deposition.

Inventive Principle:
Principle #2Taking out (Extraction)

2Object-generated harmful factors

If ion exchange membranes are used to separate anode and cathode compartments, then anodic decomposition is prevented, but volume excess occurs in the system

Engineering Contradiction:
Improveanodic decompositionVSAvoidbath volume
Core Design Contradiction:
Object-generated harmful factorsVSVolume of stationary object

Solution Approach 1:

The ion-exchange membrane is selectively placed only where needed to separate the anode compartment from the cathode compartment, rather than using extensive membrane structures. This local application prevents decomposition while minimizing volume excess.

Inventive Principle:
Principle #3Local quality

3Manufacturing precision

If continuous cleaning of the bath is performed to remove decomposition products, then coating quality is maintained, but productivity is reduced due to time-consuming operations

Engineering Contradiction:
Improvecoating qualityVSAvoidproduction efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The design converts the potential harm of organic decomposition into a benefit by using the membrane separation to prevent decomposition at the anode while allowing organics to remain at the cathode, eliminating the need for cleaning operations and improving productivity.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 solution extends the bath's service life, prevents volume excess, maintains high deposition efficiency, and ensures consistent layer thickness with reduced waste treatment, while being cost-effective and environmentally friendly.

Implementation Method 1

the anode space and the cathode space are separated from each other by a bipolar membrane

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

The bipolar membrane preferably has at least one cation exchange membrane, at least one anion exchange membrane and an intermediate layer arranged between these membranes and catalyzing the dissociation of water into protons and hydroxide ions

Methodology Applied
Scientific EffectWater splitting: Electrolysis

Implementation Method 3

an alkaline galvanic bath for depositing zinc or zinc alloys on substrates

Methodology Applied
Scientific EffectElectrodeposition: Electrodeposition

Data Source

PatentEP2235236B1Galvanic bath, method for galvanic deposition, and use of a bipolar membrane for separating in a galvanic bath
Publication Date: 2012.10.03 COVENTYA GMBH
  • EP2235236B1 patent drawingFigure 1
  • EP2235236B1 patent drawingFigure 2

AI summary

The invention relates to an alkali, galvanic bath for applying zinc or zinc alloys to substrates, wherein the anode chamber and the cathode chamber are separated from each other by a bipolar membrane. The galvanic bath is operated with zinc or zinc alloy baths that can comprise further additives. The invention further relates to a method for galvanic deposition of zinc or zinc alloys on substrates, wherein the substrate is placed in the galvanic bath according to the invention. The invention further relates to the use of bipolar membranes for separating the anode chamber and cathode chamber in galvanic baths, and for avoiding anodic disintegration of organic components of the electrolyte in galvanic baths.