Fuel Cell Bipolar Plate Layout for Uniform Fluid Distribution

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Solution Overview

Problem

In fuel cell units, the accumulation of water at the gas diffusion layer leads to undersupply of oxidizing agent, reducing electric voltage and increasing aging, while current feed and discharge channels result in uneven distribution of process fluids, affecting efficiency and longevity.

Innovation Solution

The fuel cell unit features separate channels for oxidizing agent, fuel, and coolant with a manifold structure that ensures parallel flow and uniform distribution, minimizing temperature and humidity differences through oriented feed and discharge channels.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If feed channels have small transverse extent with manifold structure, then fluid distribution is achieved, but temperature and pressure become non-uniform across channels

Engineering Contradiction:
Improvefluid distribution uniformityVSAvoidtemperature uniformity
Core Design Contradiction:
Manufacturing precisionVSTemperature

Solution Approach 1:

The patent divides each feed channel into multiple sub-channels (at least two feed channels formed side by side) that distribute process fluids to different regions of the channel structure. This segmentation allows parallel flow paths that maintain uniform temperature and pressure across all channels while still achieving comprehensive fluid distribution through the manifold structure.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent transitions from a single feed channel approach to multiple feed channels arranged side by side in the transverse direction. This dimensional change creates parallel flow paths that enable heat transfer between adjacent channels, uniformizing temperature and pressure while maintaining effective fluid distribution across the entire channel structure.

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

2Device complexity

If process fluids are introduced at a single inlet region, then device complexity is reduced, but heat transfer between fluids is limited and temperature differences increase

Engineering Contradiction:
Improvechannel structure complexityVSAvoidtemperature difference between channels
Core Design Contradiction:
Device complexityVSTemperature

Solution Approach 1:

The patent segments the single inlet region into multiple inlet regions corresponding to each feed channel. Each feed channel has its own inlet region where process fluids are introduced, enabling parallel flow paths that facilitate heat transfer between adjacent channels while maintaining relatively simple channel structures without complex interconnections.

Inventive Principle:
Principle #1Segmentation

3Power

If water accumulates at gas diffusion layer, then electrochemical reaction proceeds, but catalyst layer becomes undersupplied with oxidizing agent and voltage decreases

Engineering Contradiction:
Improveelectric voltageVSAvoidwater accumulation effect
Core Design Contradiction:
PowerVSObject-affected harmful factors

Solution Approach 1:

The patent ensures continuous and uniform distribution of oxidizing agent through multiple feed channels that supply process fluids parallel to all channels. This continuous supply prevents water accumulation by maintaining steady oxidizing agent flow that continuously removes water from the gas diffusion layer, ensuring uninterrupted electrochemical reactions and stable electric voltage generation.

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 design achieves efficient and uniform distribution of process fluids, maintaining high efficiency and reducing aging, with minimal temperature and humidity variations.

Implementation Method 1

Fuel cell units in the form of galvanic cells convert continuously fed fuel and oxidizing agent into electrical energy and water by means of redox reactions at an anode and cathode

Methodology Applied
Scientific EffectRedox reactions: Redox Reactions

Implementation Method 2

The channels are thus formed by a corresponding channel structure of a bipolar plate, and the oxidizing agent, namely oxygen, passes through the gas diffusion layer to the cathode of the fuel cells

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

three separate channel structures with channels for the separate passage of oxidizing agent, fuel and cooling fluid

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 4

at least one feed channel for coolant as process fluid for feeding the coolant into a channel for coolant

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentUS12555814B2Fuel cell unit
Publication Date: 2026.02.17 ROBERT BOSCH GMBH
  • US12555814B2 patent drawing
  • US12555814B2 patent drawing
  • US12555814B2 patent drawing

AI summary

The invention relates to a fuel cell unit as a fuel cell stack for the electrochemical generation of electrical energy, comprising stacked fuel cells, the fuel cells each comprising a proton exchange membrane, an anode, a cathode, a gas diffusion layer, a bipolar plate (10) with three separate channel structures (29) with channels for the separate passage of oxidising agents, fuel and cooling fluid. The channel structures (29) have an inlet region (37) and an outlet region (38) for the oxidising agents, the fuel and the cooling fluid, at least one feed channel (43) for feeding the oxidising agents as process fluid into the gas spaces for oxidising the fuel cells, at least one feed channel (48) for feeding fuel as process fluid into the gas spaces for fuel of the fuel cells, at least one supply channel (50) for the coolant as process fluid for supplying the coolant into a channel for coolant, a distribution structure (45) for directing and distributing the process fluids from the supply channels (43, 48, 50) into the channel structures (29) of the bipolar plates (10), at least two supply channels (43, 48, 50) being formed side by side in the longitudinal direction (57) when the inlet region (37) is formed with an extent predominantly in the transverse direction (58) between a transverse side (56) of the fuel cell (2) and the channel structure (29), or at least two feed channels (43, 48, 50) being formed side by side in the transverse direction (58) when the inlet region (37) is formed with an extent predominantly in the longitudinal direction (57) between a longitudinal side (55) of the fuel cell (2) and the channel structure (29).