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Modelling of miniature proton exchange membrane fuel cells for portable applications

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Modelling of miniature proton exchange membrane fuel cells for portable applications. J.O. Schumacher 1 , E. Fontes 3 , D. Gerteisen 1 , F. Goldsmith 1 , R. Klöfkorn 2 , A. Hakenjos 1 , K. Kühn 1 , M. Ohlberger 2 , A.Schmitz 1 , K. Tüber 1 , C. Ziegler 1

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slide1

Modelling of miniature proton exchange membrane fuel cells for portable applications

  • J.O. Schumacher1, E. Fontes3, D. Gerteisen1, F. Goldsmith1, R. Klöfkorn2, A. Hakenjos1, K. Kühn1, M. Ohlberger2, A.Schmitz1, K. Tüber1, C. Ziegler1
    • 1. Fraunhofer Institute for Solar Energy Systems, Heidenhofstr. 2, 79110 Freiburg, [email protected], Germany
    • 2. Institute of Applied Mathematics, University of Freiburg, Herrmann-Herder-Str. 10, 79104 Freiburg, Germany
    • 3. COMSOL AB, Tegnergatan 23, SE-111 40 Stockholm, Sweden
slide2

Overview

  • Examples of portable fuel cell systems
  • Model based analysis of impedance spectra
  • Modelling of self-breathing fuel cells
  • Characterisation of an along-the-channel fuel cell
  • Dynamic simulation of two-phase flow
  • Conclusion and outlook
slide4

Fuel cell system for a professional broadcast camera

  • Completely integrated system with 4 fuel cell stacks
  • 40 W average system power
  • 2 Metal Hydride Storages (100 Nl H2 or 150 Whel)
  • Integrated DC/DC- Converter
  • Miniature fans for air supply
slide5

Mobile power box

  • Portable power supply
  • Power: max. 100 W average 50 W
  • Metal Hydride Storage
  • Control based on micro processor
  • 12 V voltage supply with DC/DC- Converter
slide6

Electrode agglomerate model

  • Electrode is assumed to be made of porous spherical catalyst grains
  • Oxygen is dissolved at the outer surface of the agglomerate
  • Diffusion of dissolved oxygen in the grain and the film in radial direction
  • Local current density is given by the Tafel-equation

Graph: Jaouen et al., 2002

slide7

Cathode agglomerate model

Mass balance

Charge balance

Oxygen flux in agglomerate

slide8

Cathode agglomerate model

Charge balance

Ohm`s law

slide9

Comparision of measured and simulated polarisation curves

Small current density: change of Tafel-slope

Influence of surface-to-volume ratio L of agglomerates

L = 6 105 m-1

L = 9 104 m-1

cell potential / [V]

cell potential / [V]

current density / [A/m2]

current density / [A/m2]

slide10

Simulation of impedance spectra

  • Perturbation of solution variables of PDEs
  • Small perturbations: linearise and Laplace-transform PDEs
  • Calculate impedance:

Resistance [Wm2]

Resistance [Wm2]

slide11

Comparision of measured and simulated impedance spectra

  • Minimum value of the radius of the impedance arc is reached at a current density of 260mA/cm2.
  • Mass transport limitation is observed for higher current density: increase of radius of impedance arc.

current

density [A/m2]

meas sim

slide12

Influence of double layer capacitance on impedance spectra

Double layer capacitance CDL = 3 107 F m-3

Small double layer capacitance:

Two seperate semicircles appear

GDL

current

density [A/m2]

current

density [A/m2]

Influence

of electrode

planar and self breathing fuel cells based on printed circuit board technology
Planar and self-breathing fuel cells based on printed circuit board technology
  • Benefits of technology:
  • Small cell thickness
  • High mechanical strength
  • Low cost components
  • Well known printed circuit board production technology
  • Integration of electronic circuits
modelling domain and assumptions
Modelling domain and assumptions
  • Two dimensional model
  • Plug flow conditions in anodic gas channel
  • Convective flux of species through membrane and on cathode side neglected
  • No phase transition accounted for
slide15

Discretisation mesh and governing equations

  • Multicomponent diffusion of gas species: Stefan-Maxwell equation
  • Electronic and protonic potential: Poisson equation
  • Transport of water across membrane: modified Stefan-Maxwell equation
  • Temperature distribution: heat equation
  • l
slide16

Hydrogen and oxygen distribution

H2 molar fraction

O2 molar fraction

anode

cathode

Arrows: total flux of hydrogen and oxygen.

Vcell = 0.4 V

slide17

Water distribution and flux

H2O molar fraction x 10-3

H2O molar fraction

anode

cathode

Arrows: total flux of water.

Vcell = 0.4 V

slide18

Heat flux and temperature

T [K]

anode

cathode

  • Arrows: total flux of heat.
  • Cooling effect of ribs.
  • Vcell = 0.4 V
electronic and protonic potential current direction
Electronic and protonic potential, current direction

Protonic potential

Electronic potential

fe [V]

fp [V]

Arrows indicate the technical current direction.

comparison of experiment and simulation
Comparison of Experiment and Simulation

Experiment

Simulation

  • Opening ratio = cathode opening width / current collector rib width.
  • Limiting current is determined by oxygen supply through cathode opening.
slide21

Current distribution in cathode gas diffusion layer

cathode

electrode

cut line (e)

GDL

(e)

membrane

(e)

Normalised x-coordinate

Normalised y-coordinate

slide22

PEM fuel cell model based on FLUENT CFD-software

  • Submodels:
  • The electrochemical submodel predicts the local current-to-voltage relation in the MEA.
  • The electrical submodel accounts for electron flow and ohmic heat generation.
  • The MEA submodel describes transport of water and ions through a Nafion membrane.
slide23

Segmented fuel cell

‚Along - the - Channel‘

  • Flow-field geometry:
  • Parallel channels
  • Determination of
  • spatially resolved
  • current density
  • Measured values:
  • temperature,
  • gas flow-rates,
  • relative humidity
slide24

Current distribution along the channel

  • Comparison of measurement (dots) and simulation (lines)
  • Variation of air flow rate on the cathode side
  • All model parameters are kept constant except air flow and average current

gas flow direction:

slide25

Analysis

Relative humidity of air in the channel

Temperature of air in the channel

Relative humidity of air at MEA

Membrane protonic resistivity

slide26

Profiles of flow velocity and temperature including inlet region

velocity profile

temperature profile

slide27

Dynamic simulation of two phase flow

Modelling concept by Mario Ohlberger (Institute for Applied Mathematics, Freiburg).

Solution of the PDEs for:

  • Two phase flow in porous media
  • Species transport in the gas phase
  • Energy balance in the porous media
  • Potential flow of electrons and protons

Adaptive grid generation in space / time

Colours: pressure distribution for counter-flow case.

Problem: Determination of material parameters

slide28

Two-phase flow in porous gas diffusion layer and electrodes

phase-transition

Mass balance

Darcy-law

Water and gas saturation

Capillary pressure

slide30

Simulation examples

Wasser-dampf

flüssigesWasser

H2

O2

Mass fraction of gas components and saturation of liquid water

Colors:

Red: 1, Blue: 0

conclusion
Conclusion

Agglomerate model

  • The agglomerate model reproduces both, measured polarisation curves and impedance spectra.
  • Change of active agglomerate surface-to-volume ratio depending on the operation point?

Planar fuel cells

  • Our two-dimensional one-phase model includes all relevant processes of planar fuel cells: gas transport, heat transport, electrochemical reaction.
  • The model serves as a design tool for self-breathing planar fuel cells.
conclusion1
Conclusion

Current distribution

  • We validated the CDF model with locally distributed current measurements.
  • The CFD model agrees to measurement results if the cell is operated in the one-phase regime.
  • We are working on a dynamic two-phase flow model taking into account liquid water transport in porous media.
  • The model is extended to 3D. Parallel computing and adaptive grid generation is utilised.

Two-phase flow

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