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The Influence of Groundwater Anions on the Impedance Behavior of Carbon Steel
Corroding under Anoxic Conditions
Charmaine Lee, Zack Qin, and David Shoesmith
Sponsored byNational Science and Engineering Research Council of Canada (NSERC)Ontario Power Generation (OPG)
Department of ChemistryThe University of Western Ontario
London, Ontario, Canada
6th International Symposium on Electrochemical Impedance Spectroscopy, Cocoa Beach, Florida, May 16-21, 2004
Nuclear energy produces 16% of the electricity in Canada, 45% in OntarioA proposed used fuel disposal scenario: waste stored in containers and buried deep in granitic rock in the Canadian Shield
Copper corrosion barrier with a carbon steel (CS) liner to provide structural rigidityGroundwater entering a failed container will be anoxicCorrosion of CS could lead to scavenging of radiolytic oxidants thereby preventing corrosion of the fuel
Canadian Nuclear Waste Container
WaterRadiolysis
RedoxScavenging
FuelDissolution
SteelCorrosion
UO2Fuel
Aqueous Solution In A Failed Container CarbonSteelLiner
Cu
H2 O H2 O
O2 FeIII(s) FeII(aq) Fe2e-H2 O
H2
H2 O
H2 O
H2 Oα
H2 O2
2e-
UO22+UO2
CuShell
HCO3-/CO3
2- SO42- Cl- pH
A 1 M - - ~9B 0.2 M 0.1 M - ~9C 0.2 M 0.1 M 2 M ~9D 0.2 M 0.1 M 5 M ~9E - - 4 M ~9
Experimental
SEM
Periodic EIS every 24 hours up to 400 hoursRaman spectroscopy performed in-situ in a second experiment
A
B
C
D
E
0 100 200 300 400-0.90
-0.85
-0.80
-0.75
-0.70
Time (Hours)
Eco
rr (V
/SCE
)
-0.90
-0.85
-0.80
-0.75
-0.70
Corrosion Potential (Ecorr )A. 1 M HCO3
-/CO3=
B. 0.2M HCO3-/CO3
=
+ 0.1M SO4=
C. “B” + 2 M Cl-
D. “B” + 5 M Cl-
E. 4 M Cl-
Ee (H+|H2 )
Ee (Fe|Fe2+)
Ee(Fe|Fe2+) < Ecorr < Ee(H+|H2)Iron dissolution is strongly polarized and rate-determining for solution E For all other solutions with carbonate, no clear rate control by either the cathodic or anodic reaction
Thermodynamics of Solution E
No buffer capacityNo significant thermodynamic driving force for corrosionin absence of HCO3
-
/CO3= buffering, local
pH can increase as the consequence of corrosion A slight local pH increase ( ) would shift Ecorr into the stability region for magnetiteA local increase in Fe2+
concentration would expand the stability field for Fe3O4 to a lower pH
M. Pourbaix, Atlas of Electrochemical Equilibria in Aqueous Solutions, (1966), p312.
0 5000 10000 15000 20000
-15000
-10000
-5000
0
5000
Z'
Z''
Solution D
0 2000 4000 6000 8000 10000 12000
-8000
-6000
-4000
-2000
0
2000
4000
Z'
Z''
Solution C
0 2500 5000 7500 10000 12500 15000
-10000
-7500
-5000
-2500
0
2500
5000
Z'
Z''
Solution B
0 2000 4000 6000 8000
-6000
-4000
-2000
0
2000
Z'
Z''
Solution A
TimeFirst 96h
Thereafter
Time
Up to 168h
0 5000 10000 15000 20000 25000 30000 35000
-25000
-20000
-15000
-10000
-5000
0
5000
10000
Z'
Z''
Solution E
Up to 96h
Impedance Changes with Exposure Time
A. 1 M HCO3-/CO3
=
B. 0.2M HCO3-/CO3
=
+ 0.1M SO4=
C. “B” + 2 M Cl-
D. “B” + 5 M Cl-
E. 4 M Cl-
1 t
CT
RT
Rs
Equivalent Circuits
10- 2 10-1 100 101 102 103 104 105100
101
102
103
104
Frequency (Hz)
|Z|
FitResult
10- 2 10-1 100 101 102 103 104 105
-100
-75
-50
-25
0
Frequency (Hz)
thet
a
Rp
Rpore
2 t
Rs
Cdl
Cfilm
10- 2 10-1 100 101 102 103 104 105100
101
102
103
104
Frequency (Hz)
|Z|
FitResult
10- 2 10-1 100 101 102 103 104 105
-75
-50
-25
0
Frequency (Hz)
thet
a
0 100 200 300 400
103
104
105
Pola
rizat
ion
resi
stan
ce (Ω
cm
2 )
Time (hours)
A: 1M HCO3-/CO3
=
B: 0.2M HCO3-/CO3
=
+ 0.1M SO4=
C: 'B' + 2M Cl-
D: 'B' + 5M Cl-
E: 4M Cl-
Polarization Resistance (Rp )
Rp ∝ 1/icorrCorrosion is fast in the concentrated carbonate solution (category I)Corrosion rates are intermediate and similar for mixed anion solutions (category II) The high Rp for solution E (category III) indicates that corrosion is suppressed in a solution with no buffer capacity
III
II
IRT (1t)
RP (2t)
Pore Resistance (Rpore )
Rpore = ρ lpore/Apore
0 100 200 300 400100
101
102
103
104
Pore
resi
stan
ce (Ω
cm
2 )
Time (hours)
A: 1M HCO3-/CO3
=
B: 0.2M HCO3-/CO3
=
+ 0.1M SO4=
C: 'B' + 2M Cl-
D: 'B' + 5M Cl-
E: 4M Cl-
Rpore Cfilm
r
↑ ↑ —lpore ↑ ↑ ↓
Apore ↑ ↓ ↓
CPE Related to Film Capacitance (Cfilm )
Constant phase element (CPE):ZCPE = 1/[Y(jω)a]Y ~ C, if a ~ 1 Cfilm = εε0Af /dfThe drop in Cfilmand Rpore at the same time suggests an increase in porosity at long exposure times in solution E
0 100 200 300 4000.00000
0.00005
0.00010
0.00015
0.00020
0.00025
0.00030
0.0
0.2
0.4
0.6
0.8
1.0
1.2
CPE
-T (
)
Time (hours)
B: 0.2M HCO3-/CO3
=
+ 0.1M SO4=
C: 'B' + 2M Cl-
D: 'B' + 5M Cl-
E: 4M Cl-
CPE
-P (
)
-1050 -950 -850 -750 -650 -550 -450 -350
-0.4
-0.2
0.0
0.2
0.4
0.6
Cur
rent
Den
sity
(mA/
cm2 )
Potential (mV vs SCE)
1M HCO-3/CO=
3
0.2M HCO-3/CO=
3
+ 0.1M SO=4
Cyclic Voltammetry on a Rotating Disc Electrode (RDE)
Carbonate accelerates both anodic and cathodic processes:
a) iron dissolution is enhanced by ferrous ion complexation
Fe2+ + HCO3- Ø Fe(HCO3 )+
b) proton reduction is maintained by bicarbonate dissociation
2HCO3- + 2e- Ø H2 + 2CO3
=
(a)
(b)
5.5 h
FeCO3 FeCO3 ·H2 O
Fe3 C
Concentrated Carbonate Solution
HCO3-
FeCO3 ⋅H2 O
Fe(HCO3 )+
Fe α-Fe α-Feα-FeFe3 C Fe3 CFe3 C
H2 O H2
98 h
Fe(HCO3 )+
A
e-
Fe2+
Mixed-Anion Solution
Fe
GRFe3 O4
Fe2+
FeCO3 ⋅H2 O
24 h
42 h
79 h
FeCO3 ·H2 OSO4=
Fe3 O4
Fe2+-OH Fe3+-OH
GRGreen rust (GR): 4Fe(OH)2•2Fe(OH)3CO3
FeCO3
HCO3-
GR
B
H2 O
Pure Concentrated Chloride Solution
Fe3 O4 & a-Fe2 O3
FePassive oxide
Ex-situE
Hematite (a-Fe2O3) is not formed in solution, but in air by conversion from magnetite (Fe3O4)
ConclusionsConcentrated carbonate solution
Corrosion is ‘fast’ since carbonate accelerates both anodic (by Fe2+ complexation) and cathodic (by HCO3
- acting as a proton reservoir) reactionsCorrosion is partially blocked by siderite formation but maintained within poresVisibility of carbide residue from the underlying steel confirms the presence of porosity
Mixed-anion solutionCorrosion is suppressed at lower carbonate concentrations which appears to be the primary corrosion controlling factorThe surface is covered by compact green rust deposits, and no carbide residue is exposed
ConclusionsPure concentrated chloride solution
Corrosion is extremely slow since no significant thermodynamic driving force existsDue to the absence of buffer capacity, a slight increase in local pH could substantially reduce the thermodynamic driving force for corrosion and enforce the formation of a passive oxide filmThe increase of porosity after long exposure could indicate breakdown of the oxide film by chloride
Electrochemistry and Corrosion Studies at Western
Group leader: Professor D. W. Shoesmith (NSERC/OPG industry chair in nuclear fuel disposal chemistry)
Website: http://publish.uwo.ca/~ecsweb/