advanced particle-based 3d modeling of fuel cell electrodes€¦ · advanced particle-based 3d...

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Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei 1,2 , Vladimir Yufit 2 , Farid Tariq 2 , Nigel Brandon 2 [email protected] 1 Department of Civil and Industrial Engineering, University of Pisa (IT) 2 Department of Earth Science and Engineering, Imperial College London (UK)

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Page 1: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes

Antonio Bertei1,2, Vladimir Yufit2, Farid Tariq2, Nigel Brandon2

[email protected]

1Department of Civil and Industrial Engineering, University of Pisa (IT)2Department of Earth Science and Engineering, Imperial College London (UK)

Page 2: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Solid Oxide Fuel Cells

Main characteristics•Electricity from H2 and air

•Solid electrolyte

•600-1000°C

•Porous composite electrodes

Efficiency and degradation

½O2 + 2e- O2- H2 + O2- H2O + 2e-

*picture taken from H. Zhu, R.J. Kee, J. Electrochem. Soc. 155 (2008) B715-B729**picture taken from V.A.C. Haanappel et al., J. Power Sour. 141 (2005) 216-226

*

**

2

Page 3: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

3D tomography & electrode microstructure

FIB-SEM

X-ray nano-CT*

*picture adapted from Shearing et al., J. Eur. Ceram. Soc. 30 (2010) 1809

3

Page 4: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Averaged results from 3D modelling

Simulating physics and electrochemistry within the 3D microstructure

*

**

*picture adapted from Carraro et al., Electrochim. Acta 77 (2012) 315**picture adapted from Häffelin et al., J. Electrochem. Soc. 160 (2013) F867

Full 3D microstructural details to get… averaged electrochemical response

...which can be predicted by continuum models too

4

Page 5: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Motivation

• 3D simulations must go beyond what 1D macro-homogeneous models can do

• 3D simulations should assess:o heterogeneous distributionso hot spots which may trigger localized degradation phenomenao truly three-dimensional properties

There is the need to exploit the full potential of simulations combined with 3D tomography

5

Page 6: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

A novel approach to fully exploit 3D data

Tomographic microstructure

3D electrochemical model

Resolve individual particles*

0k kD C 0V 1

0k

F FRT RT

TPB kk

i i p e e

linking electrochemical behavior to individual particles*Quiq3D by IQM Elements, London

6

Page 7: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Workflow

1. Produce the mesh (Synopsys Simpleware)

2. Solve the model (Comsol Multiphysics)

3. Export and process the results (Comsol Multiphysics + Matlab)

7

Page 8: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

1) Mesh in Synopsys Simpleware

8

INPUT = segmented microstructural dataset

PROCEDURE1.Assign isolated islands smaller than 125 voxels to the adjacent phase

2.Produce the mesh (smart mask smoothing, coarseness factor -15)

OUTPUT = Nastran mesh file (~ 40 M mesh elements)

Page 9: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

2) Model in Comsol

9

INPUT = Nastran mesh file

PROCEDURE1.Import the mesh2.Define geometric entities (Boolean operations)

Page 10: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

2) Model in Comsol

10

PROCEDURE3. Set the physics (General Form PDE Interface)

Ni:

ScSZ:

Pore:

4. Set the reaction rate as an edge source5. Select stationary solver (segregated)6. OPTIONAL: Reduce element order7. Solve in cluster (> 150 GB RAM)

0 eI Niee VI

0 OI ScSZOO VI

0 HN HHH yRTPDN

H2(g) + O2-(ScSZ) H2O(g) + 2e-

(Ni)

Page 11: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

3) Export data (Comsol + Matlab)

11

INPUT = solved model (field variables within the domains)

PROCEDURE*1.Export data in Gauss points

2.Use an in-house Matlab code to interpolate values in Gauss points to a regular grid

OUTPUT = Field variables in grid to be overlaid with microstructure & particles

*Letting Comsol export as a regular grid is too slow.

Page 12: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Inhomogeneous current distribution

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(Ni)

/ %

Ni

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(ScS

Z) /

% ScSZ

0

5

10

15

20

25

30

0 2 4 6 8 10 12 14Number Ni-Ni neighbors / -

Ni

Num

ber f

requ

ency

(Ni)

/ %

0

5

10

15

20

25

30

0 2 4 6 8 10 12 14

ScSZ

Number ScSZ-ScSZ neighbors / -

Num

ber f

requ

ency

(ScS

Z) /

%

Current transferred

Particle size distribution

Particle connectivity

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0Ni e

lect

roni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0

ScSZ

ioni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

• Inhomogeneous distribution of current transferred by particles• Good particles have more connections, bad particles are disconnected

Ni/ScSZ anode

12

Page 13: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Localized Joule heating and particle dispersion

Particle dispersion

The wider the particle dispersion, the more inhomogeneous the

current distribution

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0Ni e

lect

roni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

Localized Joule heating

8 % of particles experience more current than what continuum

models predict

Hot spots and localized Joule heating

13

Page 14: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

From particle statistics to design indications

• Good particle for transferring current have connections but small reaction sites• Good particles for producing current have reaction sites but small connections• Particles which excel in both functions are a tiny fraction (~1 % of the total)

Connections and reaction sites (TPBs) are mutually exclusive conditions an advanced design is required by decoupling the functionalities

0

5

10

15

20

0 10 20 30 40

Num

ber N

i-Ni n

eigh

bors

/ -

Active TPB length per particle volume / m m-3

Ni

Particles transferring more

current than average

Particles producing more current than

average

Particles transferring and producing more

current than average

14

Page 15: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Conclusions

•3D tomography + physically-based simulation + resolving particles

• Comsol coupled with Synopsys Simpleware and Matlab

• Some tricks to handle big models… a lot of room for improvement!

• There is more 3D information in outliers than in mean trends

15

Page 16: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Acknowledgements

This project has received funding from :1) the European Union’s Horizon 2020 research and innovation programme under the Marie

Skłodowska-Curie grant agreement No 6549152) the EPSRC grant agreements EP/M014045/1 and EP/M009521/1

Have a look at the paper!!!

16

Page 17: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Backup slides

Page 18: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Inhomogeneous current distribution

Current produced

Particle size distribution

TPB length per particle

• Inhomogeneous distribution of current produced by particles• Good particles have more TPBs, bad particles have less or no TPB

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(Ni)

/ %

Ni

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(ScS

Z) /

% ScSZ

0

5

10

15

20

25

0.2 2.0 20.0 200.0Active TPB length per particle volume / m m-3

Ni

Num

ber f

requ

ency

(Ni)

/ %

0

5

10

15

20

25

0.2 2.0 20.0 200.0Active TPB length per particle volume / m m-3

ScSZ

Num

ber f

requ

ency

(ScS

Z) /

%

0

0

0

0

0

0.0 0.2 0.4 0.6 0.8 1.0

Ni T

PB c

urre

nt d

ensi

ty/ A

m

-3

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density at TPB

10-8

10-9

10-10

10-11

10-12

0

0

0

0

0

0.0 0.2 0.4 0.6 0.8 1.0

ScSZ

TPB

cur

rent

den

sity

/ A

m-3

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density at TPB

10-8

10-9

10-10

10-11

10-12

8

Page 19: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Localized Joule heating and particle dispersion

Particle dispersion

The wider the particle dispersion, the more inhomogeneous the

current distribution

Coarsening may induce further coarsening

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0Ni e

lect

roni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

Localized Joule heating

8 % of particles experience more current than what continuum

models predict

Hot spots and localized Joule heating

10

Page 20: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

0.6

0.7

0.8

0.9

1.0

1.1

1.2

0 4,000 8,000 12,000

Volta

ge [V

]

Current density [A/m2]

T [°C]825800775

Macro-homogeneous modelling

Gas transport

Phase-resolved Continuum

Charge transport

Electrochem. reaction

vg TPB TPB

k kg k

i LD CF

vsTPB TPB

s

V i L

Averaged microstructural properties to get averagedelectrochemical response

CH2 [mol/m3]3 4 5 6 7 8

*

*picture adapted from Bertei et al., Int. J. Hydrog. Energy 41 (2016) 22381

Page 21: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Inhomogeneous current distribution

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(Ni)

/ %

Ni

0

2

4

6

8

10

12

14

0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4 2.6 2.8Particle equivalent diameter / m

Num

ber f

requ

ency

(ScS

Z) /

% ScSZ

0

5

10

15

20

25

30

0 2 4 6 8 10 12 14Number Ni-Ni neighbors / -

Ni

Num

ber f

requ

ency

(Ni)

/ %

0

5

10

15

20

25

30

0 2 4 6 8 10 12 14

ScSZ

Number ScSZ-ScSZ neighbors / -

Num

ber f

requ

ency

(ScS

Z) /

%

Current transferred

Particle size distribution

Particle connectivity

• Inhomogeneous distribution of current transferred by particles• Good particles have more connections, bad particles are disconnected

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0Ni e

lect

roni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

1

10

100

1000

0.0 0.2 0.4 0.6 0.8 1.0

ScSZ

ioni

c cu

rren

t den

sity

/ A m

-2

Dimensionless distance from electrolyte / -

Whole datasetParticles with current > 2 times analytical currentParticles with current < 1/2 times analytical currentAnalytical current density

Page 22: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Electrochemical modelling approach

Fabrication

Characterization

Modelling

Model-based design approach

VALIDATION DESIGN

3D tomography:microstructure

-1012345

5 7 9 11 13 15

-ZIm

[c

m2 ]

ZRe [cm2]

Impedance spectroscopy:electrochemistry

Physically-based model

-2

0

2

4

6

8

10

0 2 4 6 8 10 12 14 16 18 20

-ZIm

[c

m2 ]

ZRe [cm2]

exp.sim.

6

4

2

0

650°C 600°C

11 13 15 17 19 21 23 25 27 29 31750°C 700°C2

0

-2

Simulation & validation(1)

(1) Bertei et al., Int. J. Hydrogen En. 41 (2016) 22381-22393

Page 23: Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes€¦ · Advanced Particle-Based 3D Modeling of Fuel Cell Electrodes Antonio Bertei1,2, Vladimir Yufit 2, Farid Tariq ,

Advanced microstructural characterisation tools

0

10

20

30

40

50

0 200 400 600 800 1000 1200 1400

frequ

ency

[%]

Ni-Ni neck equivalent radius [nm]

x19_initial

x19_degraded

Particle analysis (proprietary)•Watershed algorithm to identify particles•Statistics of neighbours, contact areas, TPB, etc.

Tortuosity factor (open-source)*•Solves Fick law in 3D voxels•Segmented or gray-scale datasets•Extended to diffusion impedance

* S.J. Cooper et al., SoftwareX 5 (2016) 203-210