Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM...

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Modelling coating lifetime: First practical application for coating design November 4th, 2008 COMSOL Conference Hannover T. Machado Amorim, C.Allély, J.P.Caire Presented at the COMSOL Conference 2008 Hannover

Transcript of Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM...

Page 1: Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM cross section analysis e-coat CRS Zinc Delaminated zone Anodic delamination evolution

Modelling coating lifetime: First practical application for coating design

November 4th, 2008COMSOL Conference Hannover

T. Machado Amorim, C.Allély, J.P.Caire

Presented at the COMSOL Conference 2008 Hannover

Page 2: Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM cross section analysis e-coat CRS Zinc Delaminated zone Anodic delamination evolution

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Corrosion phenomena on a cut edge Cathodic or anodic delamination mechanism

Corroded automotive samples analysisChoice of main underpaint corrosion mechanism

Cut edge corrosion modellingModelling corrosion at “initial time”Dynamic corrosion model

Conclusions

Summary

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Delamination mechanisms

Corrosion phenomena on a cut edge:

Two possible mechanisms

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Corrosion on a cut edgeRed rust formation and paint delamination

Cathodic delamination => paint/Zn Anodic delamination => paint/EG

Coupling zinc”defect” / zinc”confined” Coupling zinc / steel

pure zinc

PolymerH2O

Defect = anodeZn -> Zn2+ + 2e- Confined zone =

cathodeO2 + 4H+ + 4e- -> 2H2O

O2

steel

Polymer

Defect = cathodeO2 + 4H+ + 4e- -> 2H2O

Front of delamination = anodeZn -> Zn2+ + 2e-

ZnH2O

SteelPaintZinc

Cut edge

Risk of red rust formationRisk of paint delamination

by zinc consumption

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Corrosion modelling

Modelling delamination of automobile samples:

Anodic delamination mechanism

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Automotive system configuration

Real auto systems

clear-coat base-coatprimer ( sealer )

electro -coat

zinc

steel

phosphate layer

clear-coat base-coatprimer ( sealer )

electro -coat

zinc

steel

phosphate layer

clear-coat base-coatprimer ( sealer )

electro -coat

zinc

steel

phosphate layer

clear-coat base-coatprimer ( sealer )

electro -coat

zinc

steel

phosphate layer

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Tiago Machado AmorimChristian Allély

Painted EZ samplesSEM cross section analysis

e-coat

CRS

Zinc

Delaminated zone

Anodic delamination evolution =

Complete dissolution of zinc coat

Full dissolutionof Zn coat

Intact zoneCold Rolled Steel

Paint

Zinc

Cold Rolled Steel

Paint

Magnification

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Zn

steel

Delamination from a cut edge (EG sample)

Delamination from a scribe (EG)

CRS Polymer

Zn

Delamination resulting from

Zn film dissolution

Automotive systemsSame behaviour for cut edge and cosmetic corrosion

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Corrosion modelling

Cut edge corrosion simulation

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Cut edge protection mechanisms

• Galvanic coupling between Steel and Zinc

e-

OH-O2Zn2+

•ZnSteel

• Analyze made using thermodynamics considerations( )++= z

ieq nzF

RTEE

iilog0E0 = -0.76 (V/SHE)

E0 = -0.44 (V/SHE) E0 = 1.23 (V/SHE)

E0 = 0 (V/SHE)

−+ +↔ eZnZn 22

−+ +↔ eFeFe 22

−− ↔++ OHeOHO 442 22

( )

−− +↔+ OHHeOHg

222 22

Steel dissolutionCurrent Density (J)

(Ecorr)

Oxygen flux current limited

Jcorr

−+ +→ e2FeFe 2

-1.05 -0.65

−+ +→ e2ZnZn 2

Zinc dissolution

Hydrogen reduction

-22 OH442O →++ −eOH

1.23

−+→+ OH2He2O2H 2-

2

E (V/SCE)

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Ratio Fe/Zn influence on Galvanic coupling

-2

-1

0

1

2

3

4

-1,4 -1,2 -1 -0,8 -0,6 -0,4 -0,2

Potential (V/SCE)

log(

|i|) (

A)

Steel Ratio 50 Polar Zinc Steel Ratio 1

Ecorr Ecorr’

What is the maximum ratio Fe/Zn able to guarantee cathodic protection of Substrate?

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« Time Zero » Cut edge modeling

20028008000.5800

508800

Ratio Fe/ZnZinc thickness (per face) (µm)

Steel thickness (µm)

• Model configuration sketch

Electrolyte(NaCl-0.03 mol/l)

Insulation

Zn

Steel

Zn

800 µm8 µm 8 µm

O2 diffusion

Oxygen

Electrolyte(NaCl-0.03 mol/l)

Insulation

Zn

Steel

Zn

800 µm8 µm 8 µm

O2 diffusion

Oxygen

O2 diffusion

Oxygen

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Model ConfigurationCOMSOL environment

−+ +→ e2ZnZn 2

−− →++ OHeOHO 442 22

−− +→+ OHHeOH 222 22

Zinc

Atmosphere

Paint Steel

NaCl 0.03 Mol/l

−+ +→ eFeFe 22

Electrolyte

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• Nernst-Planck (species flux)

Mass balance

iii RNtc

=∇+∂∂

Inside electrolyte neutrality0=∑ iicz

In steady-state 0=+∇− ii RN

νΦ iiiii

ii ccDcRTD

FzN +∇−∇−=

Migration ConvectionDiffusion

Governing equations in the electrolyte

→2 Modules from COMSOL MULTIPHYSICSDiffusionNernst Planck with electroneutrality

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Zinc oxidation : Butler-Volmer equation

)())(())((

000 ZnZn EV

RTzFEV

RTzF

ZnZn eejj−

−−

−=βα

Oxygen and water reduction

Water reduction(Butler-Volmer equation)

Oxygen reduction• Mass transfer limitation (Fick’s law)

)())((

020

22

HEVRT

zF

HH ejj−

−=β

δ2

2limOzFDC

jO=

Boundary settings

Steel oxidation: Butler-Volmer equation

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7.845.3121.042.86Ionic Mobility um*1013 (s*mol/K)

1.902.031.335.240.712Diffusion

coefficientD*109 (m²/s)

O2Cl-Na+OH-Zn2+

Physics data

Kinetics Data

Species Flux: Faraday's law ( )F

JZn Zn

*22 =+ ( )

FJ

OH O2−

=−

Physical & kinetic data (literature)

-0.42-0.765Eeq (V/SHE)0.05130.0256β (V/decade)

10-40.71J° (A/m²)

H2O reductionZn oxidationButler Volmer

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Simulation validation with SVET results Distance from cut edge surface 150 µm

•ARSA model •K. Ogle

Good correlation between corrosion modeling and SVET trials realised by K.Ogle

ResultsTotal current density on the Cut edge

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•Steel under protection by galvanic coupling in time Zero

for all ratio Fe/Zn

ResultsTotal current density on the Cut edge

-750 -500 -250 0 250 500 750-1,0

-0,5

0,0

0,5

1,0

1,5

Réduction de l'oxygèneRéduction de l'eau

Den

sité

de

cour

ant (

A/m

²)

Largeur (µm)

Dissolution du Zinc

R=50R=200R=800

Zn dissolution

Water and oxygen reduction

Width (µm)

Cur

rent

den

sity

-750 -500 -250 0 250 500 750-1,0

-0,5

0,0

0,5

1,0

1,5

Réduction de l'oxygèneRéduction de l'eau

Den

sité

de

cour

ant (

A/m

²)

Largeur (µm)

Dissolution du Zinc

R=50R=200R=800

Zn dissolution

Water and oxygen reduction

Width (µm)-750 -500 -250 0 250 500 750

-1,0

-0,5

0,0

0,5

1,0

1,5

Réduction de l'oxygèneRéduction de l'eau

Den

sité

de

cour

ant (

A/m

²)

Largeur (µm)

Dissolution du Zinc

R=50R=200R=800

Zn dissolution

Water and oxygen reduction

Width (µm)

Cur

rent

den

sity

Weak steel corrosion values = cathode protection excepted for ratio 800JFe of model R=800 is 100x more important then that from R=50

15,5%

0,062

Ratio Fe/Zn=800

100%0,45%0,15%Current value relative to pure steel

0,400,00180,0006Steel corrosion kinetics (jFe(A/m²)

Pure SteelRatio Fe/Zn=200

Ratio Fe/Zn=50

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Dynamic cut edge modellingZn consummation in a coupling situation

System Sketch

O2 diffusion

Oxygen

O2 diffusion

Oxygen

Zinc consummation

Electrolyte(NaCl-0.03 mol/l)

Insulator

Zn

Steel

Zn

800 µm8.0 µm

2.0 µm

0.5 µm

8.0 µm

2.0µm

0.5 µm

(NaCl-0.03 mol/l)Zn Zn

800 µm8.0 µm

2.0 µm

0.5 µm

8.0 µm

2.0µm

0.5 µm

Simulation toolsMesh mobile (COMSOL MULTIPHYSICS)Faraday’s law (Zn consummation)

FzMolJV Zncons ⋅⋅

⋅=ρ

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Modelling cut edge corrosion11 days salt spray test simulation

SteelZinc

Steel

Zinc

Data:Corrosion potential t=0

electrolyte

SimulationCut edge after 11 days salt spray test

Corrosion potentialZn consumption

Page 21: Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM cross section analysis e-coat CRS Zinc Delaminated zone Anodic delamination evolution

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APRC – Anticorrosion Solutions

Max Fe/Zn ratio for steel cathodic protection < 800

Cut edge corrosion modellingMain results

0

5 0

1 0 0

1 5 0

5 0 2 0 0 8 0 0

Pro

tect

ion

time

(h)

R a t io F e /Z n

156h

13h0,2h

0

5 0

1 0 0

1 5 0

5 0 2 0 0 8 0 0

Pro

tect

ion

time

(h)

R a t io F e /Z n

156h

13h0,2h

8000,58002002,0800508,0800

Fe/ZnZn (µm)Steel (µm)

8000,58002002,0800508,0800

Fe/ZnZn (µm)Steel (µm)

Effect of Fe/Zn ratio

Cathodic protection duration

Reduction of Zn thickness without loosing cathodic protection properties

Not enough corrosion protection200

Page 22: Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM cross section analysis e-coat CRS Zinc Delaminated zone Anodic delamination evolution

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APRC – Anticorrosion Solutions

For a given steel thickness, the delamination rate increases with the decrease of coating thickness

Modeling cut edge corrosionInfluence of Fe/Zn thickness ratio on delamination rate

0

5

10

15

20

25

8,2 11 20,2Zn thickness (µm)

Del

amin

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m/y

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Accelerated corrosion tests resultsAnodic delamination modelling

Delamination Rate x Zn Coating thickness

00,20,40,60,8

11,21,41,6

4 10 15Zn Thickness (µm)

Del

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(mm

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Delamination Rate x Metal Coating thickness

On-vehicle results

Page 23: Machado Modelling coating lifetime - COMSOL Multiphysics · 2009. 1. 29. · Painted EZ samples SEM cross section analysis e-coat CRS Zinc Delaminated zone Anodic delamination evolution

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APRC – Anticorrosion Solutions

Conclusions

The 2D cut edge delamination model simulates a steady state corrosion situation

It simulates corrosion on cut edges by using Nenrst-Planck Module + Mobile Mesh in COMSOL MULTI PHYSICS

It Calculates cathodic protection evolution with Zn dissolution for different ratio Fe/Zn

Its tendencies are in good agreement with literature data and results obtained from accelerated corrosion tests

It shows that anodic delamination is the main underpaint corrosion mechanism for automotive samples configuration

Ongoing development: undermining corrosion simulation in cyclic corrosion configuration