Single idealized cracks: a tool for understanding fractured glass block leaching Laure Chomat1, Frédéric Bouyer1, Stéphane Gin1 and Stéphane Roux2 1 CEA Marcoule, DEN/VRH/DTCD/SECM/LCLT, BP 17171, F-30207 Bagnols-sur-Cèze Cedex 2 LMT Cachan, 61 Avenue du Président Wilson F-94 235 Cachan Cedex ABSTRACT Within the scope of the long term behaviour of the R7T7 glass, which is the French nuclear glass, leaching and its coupling with transport mechanisms is studied. Experiments carried out on a SON 68 glass (inactive R7T7 type glass) model cracks in static basic conditions show a strong coupling between solution transport and glass leaching, depending on crack aperture. Moreover, gravity driven convective transport was evidenced for vertical model cracks, whereas only molecular diffusion was detected for horizontal model cracks under the same alteration conditions. In addition, an original device was developed to study the influence of temperature gradients on alteration kinetics as a convective driving force. These experiments show conclusively that thermally- or gravity-induced convective flow must be taken into account, even if such convective effects have not been established experimentally in neutral condition, which is more realistic condition for geological storage. A modeling, based on a porous geochemical software (HYTEC) accounting for both chemistry and transport, has been successfully applied to describe alteration within simple silicate glass cracks. It will be extended to study SON 68 glass model cracks, and more complex fracture networks. INTRODUCTION In France, vitrification is the process used for the immobilization of HL radwastes. A large amount of glass with radioelement is cast into an iron canister. During the cooling process, thermal stresses (unavoidable for such meter scale canisters) lead to a multiple fragmentation and a complex crack network appears in the glass block, thereby increasing its specific surface. Considering the aim of geological disposal, this aspect may have a major influence on the long term behaviour, which must be ensured during several tens of thousand years. Indeed, when exposed to water, the glass leaching rate is proportional to the reactive surface. Moreover, glass dissolution involves complex couplings between incongruent leaching, secondary phase precipitation [1] and transport. Thus the study of the glass block alteration requires to consider separately different scales to single out the relevant elementary phenomena. Therefore, experiments were conducted on single ideal cracks in static and dynamic alteration conditions. The dynamic conditions were produced by a temperature gradient, which induced well defined flow rate. This paper presents the experimental approach designed for the study of an ideal crack and aims to highlight the different transport mechanisms and their couplings with the chemical reactions taking place during water alteration. As a perspective, the alteration modeling within cracks will be briefly presented. EXPERIMENTS Static alteration condition on single model crack Most of these experiments were conducted on SON 68 glass and consisted in leaching simplified model cracks (two well polished glass pieces of 25×25 mm2 or 25×50 mm2 area, separated by a calibrated Teflon spacer or polyamide yarn of variable thickness) maintained in vertical or horizontal position in basic condition (NaOH 0.27 0.03 mol/l) at a constant prescribed temperature of 90 1 °C, inducing a pH value above 11. The use of a basic pH and high temperature enhances chemical reaction rates [2], so that alteration can be conveniently and accurately followed thanks to SEM imaging of the altered surface. Table 1 presents the range of experiments carried out, indicating crack apertures, lengths and positions. Table 1. Studied crack apertures and lengths according to the position imposed to the model crack (uncertainty of measurement is 10 µm (resp. 20 µm) for distances below (resp. above) 160 µm). When the upper aperture is indicated as free, only one clamping device was applied on the bottom of the vertical model crack so that the upper aperture was not ensured to be at the same bottom value. Length (mm) 25 25 25 25 25 25 25 25 25 50 Vertical : aperture (m) Top free free free 200 free free 40 60 60 60 Bottom 60 80 160 200 220 550 40 60 120 60 Horizontal : aperture (m) Right 40 60 80 220 550 x 110 200 x 60 Left 40 60 80 220 550 x 80 100 x 60 In addition, control experiments were conducted on a 60 µm aperture model crack in pure water at 90 1 °C to check whether conclusions derived in basic condition may be extended to neutral conditions. Dynamic alteration conditions in model cracks : Thermoconvection experiments The assessment of the influence of a temperature gradient, as a convective transport drive, on alteration within the model crack is studied thanks to a specific leaching device. The latter is designed to generate a convective transport between two cells filled with pure water and maintained at different controlled and regulated temperatures. The bridging between these two cells consists in two model cracks in parallel with a fixed aperture separated by a 94 mm vertical distance; consequently a convection loop is induced into these two model cracks (see figure 1). In contrast to the previous static experiment, neutral conditions were used. l Glass h water z Top crack x Glass h water T1 T2 Glass 0 Bottom crack a g : gravity acceleration: 9.81 m/s2 h : height between the two cracks (m) : 94 mm a : crack aperture (m) l : crack length (m) : 25 mm T : temperature (°C) : density kinematic viscosity Pa.s : water coefficient of thermal expansion (0,6596 kg/m3/°C) Glass Figure 1. Schematic description of the thermo-convective device (left) with arrows representing the flow loop for T1 > T2 and table of relevant parameters. Because of the small size of the cell and the slow flow rates induced by the thermoconvection, inertial effects can be safely neglected (small Reynolds number) so that a Stokes regime holds. Moreover, the aspect ratio of the model crack is large enough to allow for a further simplication to the so-called Reynolds or lubrication approximation. Henceforth, the flow in the crack is of Poiseuille type (parabolic velocity profile through the thickness). Finally the model crack flows can be described as obeying a simple Darcy law, whereas the pressure in the two lateral isothermal cells is essentially hydrostatics. Yet, because of the temperature difference, both cracks are subjected to a pressure difference, and hence a circulation loop sets in. The solution of this problem is elementary and the mean velocity in the cracks reads [3] (with notations explicited in Fig. 1). gha 2 v (T1 T2 ) 24 (1) Only few degree temperature differences will be studied for the 25 millimeter length model crack to ensure that it won’t change alteration mechanisms. Table 2 summarizes the different conditions studied with the thermo-convective set-up. Table 2. Considered experimental conditions in the thermo-convective set-up. T (°C) Aperture (m) Time (days) 60 44 4–5 82 36 5 +/- 1 1.03 10-4 200 28 4 +/- 1 5.2 10-4 +/- 1 Calculated flow rate (m.s-1) 4.6 10-5 / 5.8 10-5 For a 60 µm aperture crack, two flow rates are calculated corresponding to a temperature difference of 4 °C, maintained during the first ten days of experimentation, and to a temperature difference of 5 °C, reached after twenty days. RESULTS Static alteration conditions The new mineral phase resulting from incongruent glass leaching and silicon recondensation, denoted as the altered glass layer for simplicity, can be clearly observed by SEM in laboratory basic pH conditions experiments. The first observations carried out on a 60 µm aperture model crack revealed a significant influence of solute transport on glass alteration within the cracks. This conclusion is based on the observation of a thicker altered glass layer at the exit edges than in the middle of the crack. Figure 2 shows the altered layer thickness for a horizontal and vertical model crack. 45 Top of the crack Bottom of the crack altered glass thickness (m) 40 35 30 25 20 15 10 5 0 0 5 10 15 20 25 situation in crack (mm) horizontal model crack vertical model crack Figure 2. Altered glass layer thickness as a function of the coordinate along the crack length for a horizontal (empty symbol) and vertical (filled symbol), measured by SEM (model crack of 60 µm aperture). The dissymmetric altered glass layer thickness profile observed for the vertical crack indicates that a convective (gravity driven flow) transport mechanism prevails, whereas for the horizontal crack a simple diffusion mechanism may hold. Indeed, the minimum alteration thickness, where local saturation is reached at an earlier time, is close to the bottom of vertical crack, indicating that convection takes place downward. All experimental observations comfort this conclusion. Figure 3 proposes a synoptic presentation of all alteration thickness profiles. Horizontal crack : Location in crack symmetric Altered layer thickness a 80-110, 100-200 µm 2 a 550-550 µm Altered layer thickness a 40-40, 60-60, 80-80 220-220 µm 1 flat Location in crack Vertical crack : 3 4 Altered layer thickness dissymetric a 220-free, 550-free µm Location in crack a 60-120 µm Location in crack a 60-free 80-free, 160-free µm 40-40, 60-60, 200-200 µm Altered layer thickness flat Figure 3. Synoptic figures presenting different altered glass layer profiles as a function of the aperture and orientation of the model crack. As previously mentioned, experiments carried out in a constant aperture vertical model crack present a minimum alteration position located in the last one-tenth of the crack length. Moreover, those different experiments show that, in basic condition, model crack aperture increase lead to flatter altered glass layer thickness profile. Consequently, the significance of the coupling between transport and chemistry depends on a form factor (a, see figure 1). However, model crack types labelled as 2 and 4 in figure 3 present similar shape profiles to those observed respectively for model crack types labelled as 1 and 3. Therefore, an aperture variation smaller than 100µm, inducing different local leaching conditions, cannot account for a dissymmetric profile. A convective transport appears to be the only way to understand that phenomenon. The whole range of experiments described previously demonstrates in an original way that, in vertical configuration, convective transport induced by water density gradient must be considered. As compared to gravity, temperature gradient seems to be an unlikely cause of convective transport, as experiments were performed under regulated temperature. 25 mm and 50 mm long cracks showed a similar behaviour. For the vertical model crack, the minimum alteration position lies approximately at the same relative position as shown in Figure 4. 50 leaching layer thickness (m) 45 l = 25 mm l = 50 mm 40 35 30 25 20 15 10 5 0 0 0.2 0.4 0.6 0.8 1 nomarlized distance within model crack from the top to the bottom (mm) Figure 4. Altered glass thickness profile along the crack length normalized by the total length, measured by SEM, for a 60 µm aperture. Although the conclusions of the above set of experiments clearly indicate the relevance of convection mechanisms, one has to check that this effect remains present for unaccelerated (i.e. non-basic) leaching conditions. The slow kinetics of neutral leaching did not allow us to conduct similar experiments, however a discussion of this point is proposed in Section 4. Dynamic alteration conditions: Thermoconvection experiments Maintaining temperature gradient with a one degree accuracy is difficult, because of room temperature variations. So, the imposed temperature gradient was chosen to be about 4 or 5 °C. Both temperature and the evolution of a KCl tracer introduced in the hotter cell were monitored. The latter was used to measure the flow rate and is compared in Table 2 to the theoretical expectation as given in Eq. 1 for the three experiments. Table 2. Experimental data of the three different experiments, carried out in thermo-convective device, compared to the theoretical flow rate given from Eq. 1. Aperture (m) Measured flow rate (m.s-1) +/- 15 % Calculated flow rate (m.s-1) 60 1.8 10-5 4.6 10-5 / 5.8 10-5 82 3.5 10-5 1.03 10-4 200 In analysis 5.2 10-4 Considering the large uncertainty of the temperature monitoring, the agreement between measured and calculated flow rates can be considered as fair, thereby validating our set-up and procedure. After leaching, the altered glass layer thickness was intended to be quantified through SEM imaging. The low alteration thickness and the damaging of the layer during coating and polishing lead to measurement and interpretation difficulties. Yet, the analysis of the altered glass layer into the two 60 µm aperture cracks whose profile is shown in Fig. 5 suggests that convective transport plays a significant role because of the absence of typical symmetric shape of the alteration layer thickness profile characteristic of diffusion transport. However, the peculiar w-shape of these profiles is not yet fully understood. This type of experiments constitutes a very discriminating test case for modeling. Flow direction leaching layer thickness (m) 8 7 6 5 bottom crack top crack 4 3 2 1 0 0 5 10 15 20 25 distance within crack according to the termoconvective flow direction (mm) Figure 5. Measurement of the leaching layer thickness within the two cracks altered in the thermo-convective device (60 µm aperture). DISCUSSION Static (carried out in basic conditions) and thermo-convective (neutral) experiments show a significant influence of convective transport on the alteration kinetics within cracks, whatever the convective driving force, gravity or temperature gradient. One may wonder why such a coupling has not, so far, been observed in the case of neutral condition and vertical crack in static conditions? The difficulty is that the altered glass layer thickness obtained after 290 alteration days is close to the SEM detection limit. Moreover, theoretical estimates of the convection flow rates are a subtle issue due to the intricate coupling between chemistry and transport. However, a model, based on simplified assumptions, was developed to get a crude order of magnitude of the involved flow rates. The free surfaces within the crack and out of the crack are considered to be altered at constant (but different) rates, deduced from leached layer thickness within the crack (respectively the average and the maximum deduced rate). This alteration releases different amounts of chemical species in the crack and in the surrounding solution (out of the crack), according to the incongruent leaching [2][4]. They induce different fluid densities within the crack and the surrounding solute, and so convection flow rate. This latter is determined considering Poiseuille law in model crack, diffusion transport negligible and stationary state. This model gives consistent values for flow rates induced by density variations in experiments carried out in basic condition (see table 3). Table 3. Average flow rates determined by a simple model evaluating average flow rate induced by gravity in vertical model crack in basic and neutral conditions. NaOH 0.27 mol/L aperture (m) average flow rate (m.s-1) Pe 40 3.6 10-6 0.14 60 7.1 10-6 0.3 80 8.33 10-6 0.44 160 1.25 10-5 1.3 200 1.70 10-5 2.3 220 1.48 10-5 2.2 2.46 10-5 9 6.32 10-7 0.03 550 Pure water 60 The Péclet number Pe, which characterizes the relative importance of convective versus diffusive flux, is classically defined through [5] [6] Pe av Dm (2) This dimensionless number is constructed from a characteristic length, which is the aperture (a) for cracks, the average flow rate ( v ) and the diffusion coefficient (Dm = 10-9 m2.s-1). A Péclet number larger (resp. smaller) than 1 indicates the predominance of convection (resp. molecular diffusion). The application of this crude model to neutral conditions for a 60 μm aperture vertical crack gives an approximate average flow rate value of one order of magnitude lower than in basic conditions. This model also shows up that, for the pure water experiment on 60 μm aperture vertical crack, the Péclet number is very low compare to 1 which indicates than the dominant transport mechanism, in this case, could be diffusion. Consequently, the flow rate in neutral conditions may be too low to be observable from the altered glass layer thickness dissymmetry. However, convection certainly takes place and should be taken into account in a more detailed modeling of the kinetics of alteration. PERSPECTIVES ON MODELING Resorting to numerical modeling is essential in order to address more complex and realistic geometries, and to investigate long term behavior in a faithful way, and hence understanding the interplay between chemical reaction and transport mechanism. However, glass alteration is very complex as it involves incongruent leaching of different species, secondary phase precipitation and transport. At present, no commercial software addressing both flow and chemistry is available. Since we have seen that in confined geometries such as crack, a simple lubrication approximation is sufficient, the use of a porous geochemical software (HYTEC) (whose ability to take account of the whole chemistry has been validated) appears to be the best compromise. HYTEC [7] is the association of a chemical module and a transport module. Chemical reactions are based on thermodynamic equilibriums and additional kinetic reactions, which is necessary to represent the glass alteration [8]. Transport involves diffusion and advection, but only through Darcy’s law. The extension to a non porous medium (such as a realistic glass and its cracks) can be resolved within the same framework. Firstly, only surface interaction is allowed by imposing molecular diffusion values corresponding to bulk glass and choosing a high contrast of permeabilities between the glass and the solution. Secondly, the dissolution rate depends on a Monod term, which limits chemical interaction to the surface, and on a saturation term. The glass dissolution results in the precipitation of a secondary phase (socalled gel) thermodynamically more stable than the glass itself. The flow rate, determined from the lubrication approximation, is introduced as a constant value within the geochemical model. Kinetics describing the glass alteration as well as the gel formation for a simple pure silicate glass has been investigated, in order to reproduce the alteration profile within a fracture. The introduction of a flow rate in simulation predicts dissymmetric profiles for pure silicate glass. These first results are encouraging for modeling SON 68 glass alteration, for which chemistry has to be refined. CONCLUSION Original experiments performed on SON 68 model cracks in static and basic alteration conditions proved that transport has a strong impact of alteration in model crack, for small aperture cracks. For vertical cracks, the dissymmetric altered glass layer thickness profile shows evidence of a gravity driven convection. The effect of a thermal gradient on leaching in model cracks was also investigated thanks to a specifically designed device. Results indicate the relevance of thermo-convection, in quantitative agreement with the theoretical expectation, which influences notably the glass alteration. Although, vertical crack convection has only been observed in basic conditions, and not for neutral ones, its occurrence has been argued for through a crude modeling. This study shows, in an original way, that convective transport, induced either by concentration variation or by thermal gradient, can have a great influence on the alteration and hence must be taken into account. Modeling with a modified geochemical model is an encouraging direction which is currently investigated for SON 68 glass, after a first validation on pure silicate glass. Another considered perspectives is the extension of the modeling and experiments to more complex geometries, i.e. crack networks involving several hundreds cracks. REFERENCES 1. E. Vernaz, S. Gin, C. Jégou, I. Ribet, J. Nucl. Mat. 298, 27-36 (2001). 2. S. Ribet, S. Gin, J. Nucl. Mat. 324, 152-164 (2004). 3. P. M. Adler, J. F. Thovert, Fractures and Fracture Networks, Kluwer Academic Publishers (mars 1999), p. 75. 4. N. Godon, Technical Report No DIEC/2003/02 (2003). 5. V. V. Mouzenko, S Békri, J-F. Thovert and P. M. Adler, Chem. Eng. Comm. Vols 148-150, 431-464 (1996). 6. R. L. Detwiler and H. Rajaram, R. J. Glass, Water Resour. Res. 36, 1611-1625 (2000). 7. J. Van der Lee, L. De Windt, V. Lagneau and P. Goblet, Comp. & Geosc. 29, 265-275 (2003). 8. G. De combarieu, PhD thesis, Université Paris XI- ORSAY, France (2007).