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In situ investigation of crevice corrosion on UNS
S32101 duplex stainless steel in sodium chloride
solution

Presented byPintu Kumar (13MT60R30)
1
• Duplex stainless steels (DSSs) consist of ferrite phase
and austenite phase,
Properties it offers
• high strength and
• resistance to localized corrosion
lean DSS with lower nickel contents, have attracted a lot
of attention for its reduced resistance to such form of
corrosion.
• DSS 2101 (UNS S32101) is such a grade of lean DSS

2
The aim of experiment
• To investigate the mechanism of crevice corrosion
on UNS S32101 duplex stainless steel in a
spontaneous passive system
• To provide a better understanding of the diversity of
crevice corrosion morphology

3
critical crevice solution mechanism
• Induction period of crevice corrosion
• Accumulation of aggressive ions within crevice

• Subsequent de passivation and active dissolution of
base metal within crevice
• Migration of chloride and hyroxyl ions into crevice
• depletion of oxygen in the crevice and separation of
anodic and cathodic reactions
According to CCS theory
• The most severely attacked area-deepest regions of
the crevice.
• crevice corrosion can not go into propagation stage
directly to allow significant variation in crevice
solution composition.
Observations made, however, contradicted the CCS
theory
5
IR mechanism
• It states, IR> ΔΦ criterion,for the onset of crevice
corrosion where I is the ionic current flowing out of
the crevice and R is the resistance of the crevice
electrolyte,
• ΔΦ is the difference between the applied potential
on crevice outer surface and the active/ passive
transition potential.

6
Experimental

7
experimental
• The specimens -commercial UNS S32101 duplex
stainless steel plates
• The chemical composition

8
experimental
• plates as specimens were solution annealed at 1050
C for 0.5 h followed by water quenching. Samples
were mounted in epoxy resin to expose an area of 4
cm2 to serve as working electrode
• Prior to tests, the working electrodes were ground
with emery papers.

9
• Followed by cleaning with acetone and methanol,
washed in double-distilled water and derided in air
thoroughly before use.
• The interfaces between the epoxy and sample were
sealed to prevent unwanted crevice corrosion
• then, allowing the system to react for 0.5 hr in 0.1 M
NaCl
10
Fig. 1. Schematic diagram of the experimental setup
for the in situ observation of crevice corrosion
11
Electrochemical measurement
• a potentiostat -To perform the Electrochemical
measurements
• platinum plate- counter electrode
• Saturated calomel electrode- reference electrode
• Cell arrangement is done to realize an artificial
crevice as shown before
• Electrolyte-0.1 M NaCl solun, 0.1M HCl+ 0.1M NaCl
• Applied potential- 0.1V, 0.3V, 0.5V
• Potentiodynamic polarisation curve-(-0.7 to 0.8V)
12
Optical and SEM/EDX characterization
• scanning electron microscope- to investigate
microstructure and corrosion morphologies
• surface profiler- to find surface depth profile
• Camera-For recording the changes on the crevice
wall during crevice corrosion

13
Results and discussion

14
Potentiodynamic polarization curves

15
Potentiodynamic polarization curves
• In acidic-chloride media,
As the crevice solution becomes more concentrated in
aggressive ions, the active peak becomes larger and
active/ passive transition potential increases and ΔΦ
decreases making IR> ΔΦ, as reqd for active dissolution
of base metal.

16
 In 0.1 M NaCl with crevice
• corrosion potential lower-due to restricted area of crevice
hindering reduction of oxygen gas
• Higher passive current density-larger net anodic current
density
• Passive region-current density independent of potential

17
Potentiostatic polarization to initiate crevice
corrosion

18
Potentiostatic polarization to initiate crevice
corrosion
• At 0.1V(applied potential),
Cell current low, crevice corrosion in induction stage.
• At 0.3 V,
A delayed crevice corrosion (induction + propagation).
• At 0.5V,
Immediate crevice corrosion-Measured cell current
increased more rapidly than the one at 0.3V.

19
In situ visual inspection of crevice corrosion

20
In situ visual inspection of crevice corrosion
• During the early stage of crevice corrosion, the
corrosion products increase resistance of crevice
corrosion making IR> ΔΦ, reqd for onset of reaction
• Corrosion products on parts of the wall reduce active
current lowering local IR voltage turning part of the
crevice wall into passive state hence relocation of
active dissolution region occurs.

21
Ex situ morphology analysis

Region-I
(centre
of the
crevice)

Boundary
Between II & III

Region-II
Severe
corrosion

Region-III
Ferrite phase
slightly etche

22
A,C-most severe corrosion ( crevice mouth)
B- lightly corroded(centre of crevice)
23
Fig. a- pot. Distribution on crevice wall
in the induction stage of delayed corrosion

Fig. b- Pot. Distribution in the propagation stage

24
Induction stage
• As the aggressive ions accumulate in the crevice
solution, the passive films become unstable.
• The generated current fluxes result in large IR drop
with which the HER potential was reached in the
crevice.
• The evolution of H2 could further increase the
crevice solution resistance R.
• Consequently, a significant larger IR voltage is
produced by both larger current I and R that the IR >
ΔΦ criterion would be met. The induction stage ends
and propagation stage starts
25
Propagation stage
• a net anodic polarization curve with active peak will
inhabit on the crevice wall.
• The crevice wall is subsequently attacked and the
corroded area expands towards crevice opening with
the moving passive/active boundary

26
Conclusions

27
Experimental results based on IR mechanism
1. Delayed and immediate crevice corrosion can be
initiated by potentiostatic polarization at EAPP = 0.30
VSCE and EAPP = 0.50 VSCE, respectively in neutral
0.1 mol/L NaCl solutions at room temperature.
2. The transition from induction stage to propagation
stage of the delayed crevice corrosion was explained
by IR mechanism with variation of the crevice
electrolyte composition.
28
conclusion
3. Diversity of crevice corrosion morphology –due to
the relocation of active dissolution region on the
crevice wall that occured as a result of the effects
of corrosion products.
4. Reason for the immediate crevice corrosion -The
current fluxes caused by passive/active transition
of passive films on the crevice wall

29
References
• Yang Y. Z., Jiang Y. M., Li J. , in situ investigation of
crevice corrosion on UNS S32101 duplex stainless
steel in sodium chloride solution, corrosion science
76 (2013) 163-169

30
Thank you

31

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In Situ Crevice Corrosion Investigation of DSS UNS S32101

  • 1. In situ investigation of crevice corrosion on UNS S32101 duplex stainless steel in sodium chloride solution Presented byPintu Kumar (13MT60R30) 1
  • 2. • Duplex stainless steels (DSSs) consist of ferrite phase and austenite phase, Properties it offers • high strength and • resistance to localized corrosion lean DSS with lower nickel contents, have attracted a lot of attention for its reduced resistance to such form of corrosion. • DSS 2101 (UNS S32101) is such a grade of lean DSS 2
  • 3. The aim of experiment • To investigate the mechanism of crevice corrosion on UNS S32101 duplex stainless steel in a spontaneous passive system • To provide a better understanding of the diversity of crevice corrosion morphology 3
  • 4. critical crevice solution mechanism • Induction period of crevice corrosion • Accumulation of aggressive ions within crevice • Subsequent de passivation and active dissolution of base metal within crevice • Migration of chloride and hyroxyl ions into crevice • depletion of oxygen in the crevice and separation of anodic and cathodic reactions
  • 5. According to CCS theory • The most severely attacked area-deepest regions of the crevice. • crevice corrosion can not go into propagation stage directly to allow significant variation in crevice solution composition. Observations made, however, contradicted the CCS theory 5
  • 6. IR mechanism • It states, IR> ΔΦ criterion,for the onset of crevice corrosion where I is the ionic current flowing out of the crevice and R is the resistance of the crevice electrolyte, • ΔΦ is the difference between the applied potential on crevice outer surface and the active/ passive transition potential. 6
  • 8. experimental • The specimens -commercial UNS S32101 duplex stainless steel plates • The chemical composition 8
  • 9. experimental • plates as specimens were solution annealed at 1050 C for 0.5 h followed by water quenching. Samples were mounted in epoxy resin to expose an area of 4 cm2 to serve as working electrode • Prior to tests, the working electrodes were ground with emery papers. 9
  • 10. • Followed by cleaning with acetone and methanol, washed in double-distilled water and derided in air thoroughly before use. • The interfaces between the epoxy and sample were sealed to prevent unwanted crevice corrosion • then, allowing the system to react for 0.5 hr in 0.1 M NaCl 10
  • 11. Fig. 1. Schematic diagram of the experimental setup for the in situ observation of crevice corrosion 11
  • 12. Electrochemical measurement • a potentiostat -To perform the Electrochemical measurements • platinum plate- counter electrode • Saturated calomel electrode- reference electrode • Cell arrangement is done to realize an artificial crevice as shown before • Electrolyte-0.1 M NaCl solun, 0.1M HCl+ 0.1M NaCl • Applied potential- 0.1V, 0.3V, 0.5V • Potentiodynamic polarisation curve-(-0.7 to 0.8V) 12
  • 13. Optical and SEM/EDX characterization • scanning electron microscope- to investigate microstructure and corrosion morphologies • surface profiler- to find surface depth profile • Camera-For recording the changes on the crevice wall during crevice corrosion 13
  • 16. Potentiodynamic polarization curves • In acidic-chloride media, As the crevice solution becomes more concentrated in aggressive ions, the active peak becomes larger and active/ passive transition potential increases and ΔΦ decreases making IR> ΔΦ, as reqd for active dissolution of base metal. 16
  • 17.  In 0.1 M NaCl with crevice • corrosion potential lower-due to restricted area of crevice hindering reduction of oxygen gas • Higher passive current density-larger net anodic current density • Passive region-current density independent of potential 17
  • 18. Potentiostatic polarization to initiate crevice corrosion 18
  • 19. Potentiostatic polarization to initiate crevice corrosion • At 0.1V(applied potential), Cell current low, crevice corrosion in induction stage. • At 0.3 V, A delayed crevice corrosion (induction + propagation). • At 0.5V, Immediate crevice corrosion-Measured cell current increased more rapidly than the one at 0.3V. 19
  • 20. In situ visual inspection of crevice corrosion 20
  • 21. In situ visual inspection of crevice corrosion • During the early stage of crevice corrosion, the corrosion products increase resistance of crevice corrosion making IR> ΔΦ, reqd for onset of reaction • Corrosion products on parts of the wall reduce active current lowering local IR voltage turning part of the crevice wall into passive state hence relocation of active dissolution region occurs. 21
  • 22. Ex situ morphology analysis Region-I (centre of the crevice) Boundary Between II & III Region-II Severe corrosion Region-III Ferrite phase slightly etche 22
  • 23. A,C-most severe corrosion ( crevice mouth) B- lightly corroded(centre of crevice) 23
  • 24. Fig. a- pot. Distribution on crevice wall in the induction stage of delayed corrosion Fig. b- Pot. Distribution in the propagation stage 24
  • 25. Induction stage • As the aggressive ions accumulate in the crevice solution, the passive films become unstable. • The generated current fluxes result in large IR drop with which the HER potential was reached in the crevice. • The evolution of H2 could further increase the crevice solution resistance R. • Consequently, a significant larger IR voltage is produced by both larger current I and R that the IR > ΔΦ criterion would be met. The induction stage ends and propagation stage starts 25
  • 26. Propagation stage • a net anodic polarization curve with active peak will inhabit on the crevice wall. • The crevice wall is subsequently attacked and the corroded area expands towards crevice opening with the moving passive/active boundary 26
  • 28. Experimental results based on IR mechanism 1. Delayed and immediate crevice corrosion can be initiated by potentiostatic polarization at EAPP = 0.30 VSCE and EAPP = 0.50 VSCE, respectively in neutral 0.1 mol/L NaCl solutions at room temperature. 2. The transition from induction stage to propagation stage of the delayed crevice corrosion was explained by IR mechanism with variation of the crevice electrolyte composition. 28
  • 29. conclusion 3. Diversity of crevice corrosion morphology –due to the relocation of active dissolution region on the crevice wall that occured as a result of the effects of corrosion products. 4. Reason for the immediate crevice corrosion -The current fluxes caused by passive/active transition of passive films on the crevice wall 29
  • 30. References • Yang Y. Z., Jiang Y. M., Li J. , in situ investigation of crevice corrosion on UNS S32101 duplex stainless steel in sodium chloride solution, corrosion science 76 (2013) 163-169 30