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MODELING REACTIVE TRANSPORT IN
NUCLEAR WASTE GEOLOGICAL DISPOSAL
- glass/iron/clay interactions
- atmospheric carbonation of concrete
SeS BENCH – NOVEMBER 11.-13. 2013
CEA (French Alternative Energies and Atomic Energy Commission)
B. Cochepin, I. Munier ANDRA (French Radioactive Waste Management Agency)
21 avril 2023 | PAGE 1CEA | 10 AVRIL 2012
S. Bea (CONICET, Argentina)J. Corvisier, L. De Windt (Mines Paristech, France)D. Jacques (CEN.SCK, Belgium)N. Leterrier (CEA Saclay, France)N. Marty, F. Claret (BRGM, France)C. Steefel (LBNL, USA) D.Y. Su, U. Mayer (UBC, Canada)
DISPOSAL CONCEPT IN A CLAYSTONE FORMATION AT 500 m DEPTH
Current design of deep underground repository for high and intermediate level long-lived waste
S.S.BENCH - November 16-18. 2011
SeS BENCH – Leipzig | NOV. 2013 | PAGE 2
Update onglass/iron/clay
benchmark
S.S.BENCH - November 16-18. 2011
DRD/EAP/11-0219
HLW DISPOSAL CELL
21 avril 2023 | PAGE 4
• different types of material in physical contact, technological gaps
long term calculations of geochemical evolution (100 000 years)
Vitrified wastepackages
Cross section
3 cm gap steel liner
disposal package
0.8 cm gap
3 cm gap
scale
• 1D radial domain
• transport: diffusion only
• water saturated, constant porosity
• isothermal conditions
• H2(g) from anoxic corrosion
pH2(max) = 60 bar
• glass
Φ = 0.42 m, H = 1 m
porosity = 0.12
• metallic components
total thickness = 0,095 m,
porosity = 0.25
• connected fractured zone
0.4 * excavation diameter = 0.268 m
porosity = 0.20; Deff(25°C) = 5.2 10-11 m2/s
• undisturbed claystone (50 m)
porosity = 0.18; Deff(25°C) = 2,6 10-11 m2/s
GEOMETRY AND TRANSPORT PROPERTIES
argilites (50 m – 183 cells)
glass (21cm – 21 cells)
overpack + lining + gaps
(13,8cm – 14 cells)
| PAGE 5
Major challenges come from:-highly reactive system (producing pH and redox perturbation)
-complex geochemical system (15 chemical elements, 80 aqueous species, 60 minerals)
BENCHMARK SUB-COMPONENTS
21 avril 2023 | PAGE 6
Problem 1: iron corrosion only (45 000 yrs)
magnetite, Ca-siderite, and greenalite dominate
(oxide) (carbonte) (silicate)
also smaller amounts of aluminosilicates
(nontronites and saponites)
POROSITY CLOGGING
modeling vs. experimental results iron/claystone at 90°C for 1 year
small amount of magnetite
siderite(-Ca), Fe-silicates
more phenomenological model for corrosion
Canister zone
0,1 µmProblem 2: iron corrosion + glass alteration (100 000 yrs) (Schlegel et al. 2007)
RESULTS IN THE BASE CASE (2)
21 avril 2023 | PAGE 7
A very good agreement is obtained between MIN3P and Crunchflow…
in the iron zone
RESULTS IN THE BASE CASE (3)
21 avril 2023 | PAGE 8
in the glass zone
RESULTS IN THE BASE CASE (4)
21 avril 2023 | PAGE 9
in the clay zone
RESULTS IN THE BASE CASE (5)
21 avril 2023 | PAGE 10
But other codes (Hytec, PhreeqC, PHAST,…) failed at this point to run these cases (timestep too small, CPU time too high,…)
A change in the set up of the benchmark case is under way in order to get more codes to run:-progress with Hytec-PhreeqC-based codes…??-Anyone else…?
Update onconcrete carbonation
benchmark
S.S.BENCH - November 16-18. 2011
DRD/EAP/11-0219
DESIGN: ILLW CELLS, SHAFTS (AND SEALS), ILLW DISPOSAL OVERPACK
Atmospheric carbonation of overpack during the operating period
S.S.BENCH - November 16-18. 2011
| PAGE 12
• Bitumized waste• Compacted metallic waste• Organic waste
SeS BENCH – Leipzig | NOV. 2013
DRYING AND CARBONATION PROCESSES OF ILLW OVERPACK
S.S.BENCH - November 16-18. 2011
Dry air
(Rh = 40 %)
T = 25°C to 50°C
SlWater vapor diffusion
CO2 gas diffusion
T
Aqueous diffusion of reactants
Two phase water/air flow
Dissolution/precipitation : porosity reduction, permeability variations
Brine formation
CO2 gas dissolution
Dry air
(Rh = 40 %)
T = 25°C to 50°C
SlWater vapor diffusion
CO2 gas diffusion
T
Aqueous diffusion of reactants
Two phase water/air flow
Dissolution/precipitation : porosity reduction, permeability variations
Brine formation
CO2 gas dissolution
| PAGE 13SeS BENCH – Leipzig | NOV. 2013
Major challenges come from:-Fast gaseous CO2 transport and highly reactive with portlandite
-Coupling capability with « multiphase » flow and transport
GEOMETRY
1D Cartesian – 5.5 cm divided in 11 cells (5 mm) for concrete 1 extra cell for “atmosphere”
Boundary conditions (EOS 4)
S.S.BENCH - November 16-18. 2011
Symmetry axis
Dry air Dry air
Package thickness 110 mm
| PAGE 14SeS BENCH – Leipzig | NOV. 2013
concrete
CASE 1/3DRYING OF CONCRETE OVERPACK
S.S.BENCH - November 16-18. 2011
DRD/EAP/11-0219
DRYING PHENOMENON : PARAMETERS IN REFERENCE CASE
BHP CEM I
S.S.BENCH - November 16-18. 2011
ROCK1
Density (kg/m3) 2700
Porosity 0.12
Intrinsic permeability to liquid (m²) 1e-19
Intrinsic permeability to gas (m²) 1e-17
Relative permeability m – Slr – Sls - Sgr
0.424 – 0.0 – 1.0 – 0.0
Capillarity pressurem – P0 (MPa) – Pmax (MPa) 0.424 – 15 - 1500
Molecular diffusion coefficient in gaseous phase (m²/s)
2.4e-5
Molecular diffusion coefficient in aqueous phase (m²/s)
1.9e-9
Millington-Quirk a parameter 2
Millington-Quirk b parameter 4.2
Klinkenberg parameter (MPa) 0.45
| PAGE 16SeS BENCH – Leipzig | NOV. 2013
DRYING RESULTS
S.S.BENCH - November 16-18. 2011
| PAGE 17SeS BENCH – Leipzig | NOV. 2013
TOUGH2Full multiphase (EOS4)Richards (EOS9)
OK to use Richards’ equation for benchmarking exercise
Hytec (Richards’ equation)
CASE 2/3CARBONATION WITH CONSTANT SATURATION
S.S.BENCH - November 16-18. 2011
DRD/EAP/11-0219
PHENOMENOLOGY
Constant saturation but unsaturated + diffusion of gas
S.S.BENCH - November 16-18. 2011
Sliq = 0.3
CO2 gas diffusion
Diffusion of aqueous species
Dry AirRH = 60%
25°CpH = 13
CO2 dissolution
Precipitation/dissolution reactions
Sliq = 0.3
CO2 gas diffusion
Diffusion of aqueous species
Dry AirRH = 60%
25°CpH = 13
CO2 dissolution
Precipitation/dissolution reactions
Sliq = 0.3
CO2 gas diffusion
Diffusion of aqueous species
Dry AirRH = 60%
25°CpH = 13
CO2 dissolution
Precipitation/dissolution reactions
| PAGE 19SeS BENCH – Leipzig | NOV. 2013
Sliq = 0.36
CHEMICAL PARAMETERS
Primary phases
Secondary phases
Kinetics of dissolution / precipitation
nnnn Akr 1
15,298
11exp15,298 TR
EkTk a
n
Phase Volume %
Calcite 72.12
Portlandite 5.73
CSH 1.6 13.76
Monocarboaluminate 2.26
Ettringite 3.60
Hydrotalcite 0.39
Hydrogarnet-Fe (C3FH6) 2.05
Phase type Phases
Oxides Magnetite, Amorphous silica
Hydroxides Brucite, Gibbsite, Fe(OH)3
Sheet silicates Sepiolite
Other silicates CSH 1.2, CSH 0.8, Straetlingite, Katoite_Si
Sulfates, chlorides, other salts Gypsum, Anhydrite, Burkeite, Syngenite, Glaserite, Arcanite, Glauberite, Polyhalite
Carbonates Calcite, Nahcolite
Other Hydrotalcite-CO3, Ettringite, Dawsonite
CHEMICAL PARAMETERS
Primary and Secondary phases kinetics parameters
Phase Kinétic
Constant (298.15 K)
Activation Energy
(kJ.mol-1)
Specific Surface (m2.g-1)
C3FH6 1 10-12 30 1
Calcite 1.6 10-6 23.4 1
CSH 0.8 1.6 10-9 50 1
CSH 1.2 1.6 10-9 50 1
CSH 1.6 1.6 10-9 30 1
Ettringite 1.6 10-9 30 1
Gibbsite_am 1.6 10-9 30 1
Gypsum 1.6 10-5 20 1
Hydrotalcite 1.6 10-9 30 1
Iron Hydroxyde 1.6 10-8 30 10
Monocarboaluminate 1.6 10-9 10 1
Portlandite 1.6 10-8 20 1
Sépiolite 1.6 10-12 50 10
Amorphous SiO2 1.6 10-9 30 1
Straetlingite 1.6 10-9 50 1
| PAGE 21SeS BENCH – Leipzig | NOV. 2013
!Precipitation of
secondary minerals using a specific surface
area : involves a « nucleus » volume
fraction:10-4 in Toughreact
(see discussion below)
REACTION TRANSPORT RESULTS AT CONSTANT SL
Making sure the same effective diffusion coefficient is used…
| PAGE 22SeS BENCH – Leipzig | NOV. 2013
For Crunchflow, b = 3.2 has to be used
(instead of b= 4.2 for Toughreact)
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 23
TOUGHREACT
MIN3P
CRUNCHFLOW HYTEC
Carbonation front is similar
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 24Calcite precipitation front is similar
TOUGHREACT MIN3P
CRUNCHFLOWHYTEC
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 25Timing not the same for all codesStraetlingite more persistent with Crunchflow
TOUGHREACT
HYTEC
MIN3P
CRUNCHFLOW
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 26
Dawsonite does not precipitate withCrunchflow and HytecStraetlingite more persistent with Crunchflow
TOUGHREACT
HYTEC
MIN3P
CRUNCHFLOW
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 27More precipitation of gypsum in the simulation with Crunchflow
TOUGHREACT
HYTEC
MIN3P
CRUNCHFLOW
REACTION TRANSPORT RESULTS AT CONSTANT SL
| PAGE 28
Effect of the nuclei volume fraction (CRUNCHFLOW)
Vn = 10-4 Vn = 10-3
Vn = 10-2Vn = 10-1
CASE 3/3FULLY COUPLED CARBONATION
S.S.BENCH - November 16-18. 2011
DRD/EAP/11-0219
Input parameters
Results only with Toughreact so far…
CARBONATION RESULTS
pH decrease, portlandite dissolution and calcite formation over a thickness of about 2 cm after 100 years
CARBONATION RESULTS
Dissolution of CSH 1.6, ettringite, monocarboaluminate and hydrotalcite on 2 cm after 100 years
Precipitation of CSH 1.2, CSH 0.8, straetlingite, amorphous silica and gypsum on the same thickness
Precipitation of small amounts of sepiolite, gibbsite and katoïte-Si is also predicted
CARBONATION: CPU CONCERNS…
CO2 diffusion (gas phase) and reactivity are very fast!
No SIA small time steps CPU times go up (the roof)!
CONCLUSIONS
Glass-iron-clay interactions exercise
very demanding in terms of number of minerals with large domain of kinetics coupled with a strong pH and redox perturbation
(desperately) looking for new teams to jump in!
Concrete carbonation exercise highly reactive CO2 diffusing rapidly in the gas phase
emphasizing the coupling between transport and reactions (GI vs. OS)
Sliq-dependent diffusion coefficient
[ another challenge: Sliq-dependent reactivity? ]
Direction de l’Energie Nucléaire
Département des Technologies
Nucléaires
Service de Modélisation des Transferts et
de Mesures Nucléaires
Commissariat à l’énergie atomique et aux énergies alternatives
Centre de Cadarache | 13108 Saint Paul-lez-Durance
T. +33 (0)4 42 25 37 24 | F. +33 (0)4 42 25 62 72
Etablissement public à caractère industriel et commercial | RCS Paris B 775 685 01921 avril 2023
| PAGE 35
CEA | 10 AVRIL 2012
THANK YOU FOR YOUR ATTENTION
Acknowledgements:S. Bea (CONICET, Argentina)J. Corvisier, L. De Windt (Mines Paristech, France)D. Jacques (CEN.SCK, Belgium)N. Leterrier (CEA Saclay, France)N. Marty, F. Claret (BRGM, France)C. Steefel (LBNL) D.Y. Su, U. Mayer (UBC, Canada)
POSSIBLE EXTENSION:SATURATION-DEPENDENT CHEMICAL REACTIVITY
Considerable reduction in the amplitude of carbonation (less dissolution of portlandite and CSH 1.6 and less precipitation of amorphous silica and other secondary CSH)
Lower reactivity accompanied by a greater penetration of carbonation front due to lower consumption of CO2 at the surface
Effect of water content on reactivity (Bazant type function)
CONCLUSIONS
Drying process of 11 cm thick waste packages depends strongly on the concrete nature and slightly on the flow model (Richards or full multiphase)
Considering full multiphase model, carbonated depth is about 1 cm after 100 years for the High Performance Concrete. degraded thickness is totally carbonated (total dissolution of primary mineral phases)
If we consider a chemical reactivity depending on the liquid saturation (Bazant type function), a considerable reduction in the amplitude of carbonation and a greater penetration of carbonation front are observed.
Progress areas include:
• taking into consideration a protective effect of secondary minerals
• improving knowledge on kinetics parameters and thermodynamic data, especially for CSH with low Ca/Si ratio
• coupling this system with corrosion of rebars