Double-Sided PV Cell Metallization via Segmented Electrolysis

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Solution Overview

Problem

The development of double-sided photovoltaic cells is hindered by the complexity and cost of existing metallization techniques, particularly due to the incompatibility of electrochemical plating methods with both surfaces, leading to performance limitations and high production costs.

Innovation Solution

A method involving a shared electrolysis tank with separate compartments for depositing a metal layer on one surface and a metal oxide layer on the other, assisted by illumination and potential differences, allowing simultaneous electrochemical deposition on both active surfaces of double-sided photovoltaic cells.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If electrochemical plating is used for metallization, then productivity and cost-effectiveness improve, but it cannot be applied to both surfaces of double-sided cells simultaneously due to technical incompatibility

Engineering Contradiction:
Improvedeposition speedVSAvoidapplicability to both surfaces
Core Design Contradiction:
ProductivityVSAdaptability or versatility

Solution Approach 1:

The electrolysis tank is divided into two separate compartments, each dedicated to treating one surface of the double-sided cell. This segmentation allows independent optimization of electrochemical parameters for each surface while enabling simultaneous processing, resolving the incompatibility issue that prevented conventional electrochemical plating from being applied to both surfaces.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

An ion-exchange membrane is introduced as an intermediary between the two electrolysis compartments. This membrane enables selective ion transport while electrically isolating the two compartments, allowing each surface to undergo appropriate electrochemical reactions without interference from the other surface, thus making simultaneous dual-surface metallization possible.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If screen printing with silver paste is used, then metallization is achieved on both surfaces, but shadowing rate increases and electrical conductivity decreases

Engineering Contradiction:
Improveelectrical conductivityVSAvoidshadowing rate
Core Design Contradiction:
ReliabilityVSObject-affected harmful factors

Solution Approach 1:

The mechanical screen printing process is replaced with electrochemical deposition. This substitution enables precise control of metal layer thickness at the micro-scale, producing thinner metallization patterns that reduce shadowing while maintaining or improving electrical conductivity through better contact with the semiconductor surface.

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

Solution Approach 2:

The deposition parameters (current density, deposition time, electrolyte composition) are precisely controlled to optimize the metal layer characteristics. By adjusting these parameters, the metallization pattern width can be reduced by over 50% compared to screen printing, significantly reducing shadowing while achieving superior electrical contact properties.

Inventive Principle:
Principle #35Parameter changes

3Quantity of substance

If conventional electrochemical plating is used, then silver usage is reduced and cost decreases, but deposition speed is too slow for industrial production

Engineering Contradiction:
Improvesilver consumptionVSAvoiddeposition speed
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The electrolysis system is designed to simultaneously perform metallization on both front and rear surfaces in a single processing step. This multi-functionality doubles the effective deposition throughput compared to sequential single-surface treatment, making the process industrially viable while maintaining low silver consumption through efficient electrochemical deposition.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

Both surfaces are metallized simultaneously in continuous operation within the same electrolysis bath system. The dual-compartment design with ion-exchange membrane allows uninterrupted concurrent deposition on both surfaces, eliminating idle time between surfaces and achieving deposition speeds 10 times greater than conventional electroless methods.

Inventive Principle:
Principle #20Continuity of useful action

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 enables faster, cost-effective, and high-performance metallization of both surfaces with reduced shadowing, improved conductivity, and lower silver usage, overcoming the limitations of existing methods while achieving deposition speeds 10 times greater than current electroless methods.

Implementation Method 1

The deposition step comprises in particular a shared operation of depositing on each of the active surfaces, implemented by electrolysis in a shared electrolysis tank

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

deposit induced by light (Light Induced Plating or LIP)... by illuminating the semiconductor, the p-n junction generates electron-hole pairs

Methodology Applied
Scientific EffectLight induced plating: Photovoltaic Effect

Data Source

PatentUS10998457B2Contacts for a photovoltaic cell with two active surfaces
Publication Date: 2021.05.04 ELECTRICITE DE FRANCE
  • US10998457B2 patent drawing
  • US10998457B2 patent drawing
  • US10998457B2 patent drawing

AI summary

Fabrication of a double-sided photovoltaic cell, with two opposite active surfaces, comprising a step of depositing, on each active surface, at least one electric contact. The deposition step comprises in particular a shared operation of depositing on each of the active surfaces, implemented by electrolysis in a shared electrolysis tank comprising: a first compartment for depositing a metal layer on a first active surface of the cell, for fabrication of a contact comprising said metal layer on the first active surface; and a second compartment for depositing, by oxidation, a metal oxide conductor layer on the second active surface of the cell, for the fabrication of a contact comprising said metal oxide layer on the second active surface.