Flow-Through Porous Electrodes for Microfluidic Fuel Cells

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Solution Overview

Problem

Microfluidic fuel cells face challenges in achieving high fuel utilization per single pass due to limitations in convective/diffusive transport and active surface area, particularly with traditional two-dimensional electrode designs.

Innovation Solution

The implementation of a three-dimensional porous electrode architecture with a flow-through design that directs reactants orthogonally through the electrode, enhancing convective/diffusive transport and increasing the active surface area, combined with hydrophilic or hydrophobic treatment to promote saturation and ion-conducting membranes for efficient ion transport.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If traditional two-dimensional electrode designs are used, then device simplicity is maintained, but fuel utilization per single pass is limited due to insufficient active surface area and convective/diffusive transport

Engineering Contradiction:
Improvefuel utilization per single passVSAvoidelectrode architecture complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent transitions from traditional two-dimensional planar electrodes to three-dimensional porous electrodes with flow-through architecture. This dimensional change creates extensive internal surface area within the electrode bulk, enabling significantly higher fuel utilization per single pass by providing numerous active sites throughout the electrode volume rather than just at the surface.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

Solution Approach 2:

The patent employs porous electrode structures with controlled porosity to enable flow-through operation. The porous matrix provides both mechanical support and a network of channels for reactant distribution, creating a large effective surface area while maintaining structural integrity and enabling enhanced mass transport throughout the electrode.

Inventive Principle:
Principle #31Porous materials

2Productivity

If reactants are supplied in a single liquid phase with simple solid-liquid interfaces, then manufacturing is simplified, but mass transport rates to active sites are insufficient

Engineering Contradiction:
Improvemass transport rate to active sitesVSAvoidreaction zone architecture
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent utilizes porous electrode materials with interconnected pore networks that facilitate rapid convective and diffusive transport of reactants from the bulk liquid phase directly to active sites distributed throughout the electrode interior. This porous architecture dramatically enhances mass transport rates compared to simple planar interfaces.

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

By transitioning to three-dimensional flow-through electrodes, the patent creates multiple transport pathways and reduces diffusion distances from reactant bulk to active sites. Reactants flow through the electrode thickness direction, providing direct access to catalytic surfaces embedded within the porous matrix, thereby enhancing mass transport efficiency.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 significantly improves current density and fuel utilization, achieving higher power densities and energy conversion efficiency, with the potential for in situ regeneration of reactants, while maintaining low operational costs and reduced ohmic resistance.

Implementation Method 1

enhancing rates of convective/diffusive transport to and from the active sites

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 2

enhancing rates of convective/diffusive transport to and from the active sites

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

hydrophilic or hydrophobic electrode treatment that promotes saturation of the porous electrode

Methodology Applied
Scientific EffectCapillary action: Capillary Action

Implementation Method 4

ion-conducting membranes for efficient ion transport

Methodology Applied
Scientific EffectIonic conduction: Conduction (electrical)

Data Source

PatentUS10079391B2Fuel cell with flow-through porous electrodes
Publication Date: 2018.09.18 UVIC INDUSTRY PARTNERSHIPS INC
  • US10079391B2 patent drawing
  • US10079391B2 patent drawing
  • US10079391B2 patent drawing

AI summary

A microfluidic fuel cell with flow-through architecture is provided. The anode and the cathode are porous electrodes and comprise an interstitial pore network. A virtual insulator is located between the electrodes, in an electrolyte channel. The virtual insulator is comprised of a co-laminar flow of an electrolyte. An inlet directs substantially all the flow of liquid reactant through the porous electrode.