I have started developing a tool that numerically solves the Nernst-Planck equations in bentonite on a 1D grid. It treats the bentonite within the homogeneous mixture model, accounting for the structural clay charge via the parameter \(c_\mathrm{IL}\). It also handles external solution reservoirs of finite size, and Donnan equilibrium is maintained dynamically at the interfaces between clay and external solutions. At the moment, the tool does not account for activity coefficients.
Here \(D_c\), \(z\) and \(c^\mathrm{int}\) are the diffusion coefficient, charge number and concentration, respectively, for the considered species. \(\phi\) denotes porosity. For convenience, we denote the spatial derivative (\(\partial/\partial x\)) by \(\nabla\). \(\tilde{\psi}\) is the dimensionless electric potential,1 whose gradient is
As we noted previously, compacted bentonite often only show minor effects of electromigration, with diffusion potentials below 1 mV. This is because substantial counter-ion concentrations reduce the size of the electric field required to counteract effects from differences in ion mobilities (the denominator in eq. 4 is always large). To see some effect when exploring the full solution of the Nernst-Planck equation, let’s therefore focus on one of the hypothetical, “extreme” cases considered in the previous post. This test case considers diffusion of CaCl2 through bentonite of quite low density (\(c_\mathrm{IL}\) = 1.5 M), with a 10 times lower calcium mobility relative to chloride, and has a 0.25 M CaCl2 reservoir on the left side and a 0.05 M CaCl2 reservoir on the right side.
In the previous consideration we did not solve the full Nernst-Planck problem (eqs. 1— 5), but imposed a linear concentration gradient across the clay and calculated the corresponding electric potential (eq. 4) and contributions to the flux (eqs. 2 and 3). For the “extreme” CaCl2-case, the results of this approach looked like this (relevant model parameters are summarized below the figures)
Model parameters: \(c_\mathrm{IL}\)= 1.5 M, \(D_\mathrm{Ca}^\mathrm{clay}\) = 0.203⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.25 M CaCl2,c(2) = 0.05 M CaCl2.
The concentration gradient contributions to the fluxes are constant throughout the clay domain (dashed lines), signifying the imposed linear concentration profile. In contrast, the total fluxes varies significantly (full lines), indicating that the system is not in steady-state. As the calcium mobility is 10 times lower than the chloride mobility, it is no surprise that the calcium flux is dominated by the electromigration contribution (dotted lines). Also the chloride flux is seen to be significantly influenced (retarded) by the electric field. The diffusion potential was evaluated to -12.1 mV, while the Donnan contribution to the membrane potential is +18.8 mV, giving an evaluated membrane potential of +6.7 mV (for a fuller discussion on these potentials, see the previous post). But note that this “membrane potential” is not completely accurately evaluated, as the linear concentration profile does not correspond to steady-state.
By solving the full Nernst-Planck framework (eqs. 1— 5), we can investigate the size of the error in the above treatment. The full solution looks like this
Model parameters: \(c_\mathrm{IL}\) = 1.5 M, \(D_\mathrm{Ca}^\mathrm{clay}\) = 0.203⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.25 M CaCl2,c(2) = 0.05 M CaCl2.
This figure shows snapshots of profiles of the chloride concentration, the electric potential and the chloride flux at 0.25, 0.5, 1, 2 and 8 days; the initial condition is a chloride free calcium clay. In the flux diagram are plotted both the full flux (solid lines) and the concentration gradient contribution3 (dashed lines). Although only barely noticeable, the steady-state has a slightly non-linear concentration profile, resulting in a varying “Fickian” flux contribution (\(j_\mathrm{conc}\)). However, compared with the case with imposed linear concentration profiles, the diffusion potential changes only slightly, to -12.2 mV, giving a true steady-state membrane potential of +6.6 mV.
Below are compared the steady-state fluxes for both calcium and chloride with the fluxes evaluated from imposing linear concentration profiles.
The — now constant — total Cl flux is 3.64⋅10-6 mol/m2/s, to be compared with a variation between 3.0⋅10-6 mol/m2/s and 4.5⋅10-6 mol/m2/s in the previous calculation. Likewise, the previously constant chloride concentration gradient flux of 4.88⋅10-6 mol/m2/s now varies between approximately 6⋅10-6 mol/m2/s and 4⋅10-6 mol/m2/s.
We should remind ourselves that we have considered an “extreme” case, and also take a look at a more realistic/relevant model, to illustrate the often quite insignificant contribution of electromigration in bentonite. In the plot below we are solving the full Nernst-Planck framework for CaCl2 through diffusion, as previously, but now with a denser clay (\(c_\mathrm{IL}\) = 3.0 M) and by setting the Cl/Ca diffusivity ratio equal to the corresponding value in bulk water (2.57).
Model parameters: \(c_\mathrm{IL}\) = 3.0 M, \(D_\mathrm{Ca}^\mathrm{clay}\) = 0.79⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.25 M CaCl2,c(2) = 0.05 M CaCl2.
We considered also this case in the previous treatment. The diffusion potential is here -1.1 mV, and the membrane potential +18.8 mV, which we also evaluated previously. Also the steady-state fluxes are essentially the same as previously evaluated: the chloride steady-state flux is 3.6⋅10-6 mol/m2/s, while in the case with an imposed linear concentration profile, the total flux varies between 3.5⋅10-6 mol/m2/s and 3.6⋅10-6 mol/m2/s. All of these similarities are of course a manifestation of that the linear concentration profiles are very close to being the true steady-state profiles.
Note how similar the concentration gradient contribution is to the total flux for chloride during the entire process, in contrast to the behavior in the “extreme” case. This indicates that chloride here essentially show “Fickian” diffusion, at the rate set by its individual diffusion coefficient. It should be remembered, however, that the full transport process is still influenced by electromigration, since charge neutrality is required (the slower calcium ions are “boosted” by the electric field). But such effects are in principle no different from how salts generally diffuse in ordinary solutions.
In the original publication, these examples consider a clay component consisting of parallel bulk water and “diffuse layer” domains, and linear concentration profiles are imposed in the bulk water; a main NaCl concentration decreases from 0.1 M to 0.001 M in both examples, while different 22Na and 36Cl concentrations are maintained. In “example 2”, the tracer concentrations decrease in proportion with the main bulk electrolyte, from 10-9 M to 10-11 M. In “example 3” the bulk water tracer concentrations are kept at a constant value 10-9 M.
Here we instead consider only the “diffuse layer” domain, and impose the bulk water concentrations as boundary conditions. The “diffuse layer” domain is characterized by the parameter \(c_\mathrm{IL}\) = 0.33 M (Tournassat and Steefel (2015) call this quantity \(q\)) and is assumed initially free of chloride and tracers. Solving the full Nernst-Planck equations gives the following evolution of the electric potential (this is the same for both examples)
Model parameters: \(c_\mathrm{IL}\)= 0.33 M, \(D_\mathrm{Na}^\mathrm{clay}\) = 1.33⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.1 M NaCl, c(2) = 0.001 M NaCl.
For “example 2”, the concentration and flux evolution for the tracers looks like this
Model parameters: \(c_\mathrm{IL}\)= 0.33 M, \(D_\mathrm{Na}^\mathrm{clay}\) = 1.33⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.1 M NaCl, c(2) = 0.001 M NaCl. c(1)tracers = 10-9 M, c(2)tracers = 10-11 M
In this example, the steady-state flux of both the chloride and the sodium tracer mimics the flux of the main electrolyte; the steady-state flux is the same for both species (5.6⋅10-15 mol/m2/s) and a factor 108 smaller than for the main electrolyte (5.6⋅10-7 mol/m2/s). As the clay incorporates much more 22Na than 36Cl in the transient stage, the initial fluxes are considerably larger for 22Na. The 36Cl flux is in essence completely “Fickian”, i.e. differences between total fluxes and the concentration gradient contributions are negligible. The steady-state 22Na flux, in contrast, has a non-negligible contribution from electromigration, in the same proportion as the stable sodium (this is not resolved in the figure above, but looks qualitatively the same as for the stable sodium, displayed below). These results are completely in line with what we earlier have concluded for the flux of these tracers.
For “example 3”, the tracer concentration and flux evolution looks like this
Model parameters: \(c_\mathrm{IL}\) = 0.33 M, \(D_\mathrm{Na}^\mathrm{clay}\) = 1.33⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.1 M NaCl, c(2) = 0.001 M NaCl. c(1)tracers = 10-9 M, c(2)tracers = 10-9 M
The evolution for 36Cl is basically the same as for “example 2”. This is expected, as the right hand side boundary conditions set the clay concentration at this interface to effectively zero in both cases. The behavior of 22Na, on the other hand, is very different as compared with “example 2”. Now a huge 22Na concentration (relatively speaking) is established at the right hand side boundary, which results in a flux in the opposite direction with much larger magnitude (the steady-state flux is -4.3⋅10-12 mol/m2/s). This illustrates the mechanism behind the seeming uphilldiffusion effect. Note that the 22Na flux in this case is essentially completely “Fickian” during the entire simulation.
The only significant effect of electromigration in this model is, as we have concluded previously, for the transport of the main electrolyte sodium (or the corresponding 22Na transport in “example 2”, which mimics the main sodium flux). The concentration and flux evolution for main chloride and sodium looks like this (this is the same in both examples).
Model parameters: \(c_\mathrm{IL}\) = 0.33 M, \(D_\mathrm{Na}^\mathrm{clay}\) = 1.33⋅10-10 m2/s, \(D_\mathrm{Cl}^\mathrm{clay}\) = 2.03⋅10-10 m2/s, c(1) = 0.1 M NaCl, c(2) = 0.001 M NaCl.
The total flux are the same for chloride and sodium at all times, as a consequence of the requirement of charge neutrality.4 To achieve this, the sodium flux is “boosted” by the induced electric field (electromigration). The effect is mainly noticeable on the cation, because it has a much larger concentration.
Footnotes
[1] \(\tilde{\psi}\) is normalized by the thermal voltage as \(\tilde{\psi} = \psi/V_T\), where \(V_T = RT/F\). Here we adopt \(V_T\) = 25.7 mV.
[2] The corresponding description for Fickian diffusion in the homogeneous mixture model is found here.
[3] The concentration gradient contributions to the fluxes (\(j_\mathrm{conc}\)) in the diagrams presented here are not color coded (but black), in order for them to be visible also when \(j \approx j_\mathrm{conc}\). I hope it is still reasonably easy to understand which flux profile corresponds to which time.
[4] Strictly, the main chloride and sodium fluxes differ ever so slightly in “example 3”, because there is also an 22Na/stable Na exchange process ongoing. But this difference is not noticeable for the main ions, as the reservoir tracer concentrations are a factor 106 — 108 smaller.
Let’s begin by reminding ourselves where we are in the “story” of the article. TS15 begun by vaguely suggesting that diffusion in bentonite1 cannot be modeled by assuming “Fickian” diffusion. The argument, however, is based on the inability of the traditional diffusion-sorption model to be reasonably fitted to ion through-diffusion data. This inability is not primarily due to assuming Fickian diffusion, but due to assuming immobility of the “sorbed” ions and due to assuming that the pore volume contains nothing but bulk water.
After being promised to be presented “fundamental properties” of bentonite that apparently will demonstrate the problem with assuming “Fickian” diffusion, we were insteadintroduced to a large set of modeling concepts. As a description of actual compacted bentonite, these concepts are mostly irrelevant (e.g. the Gouy-Chapman model), unjustified (e.g. Stern layers on basal surfaces), or simply fantasies (e.g. the idea of “stacks”, or the idea of Donnan equilibrium on the microscopic scale).
Finally, we were presented the Nernst-Planck approach to ion diffusion, which indeed goes beyond a Fickian description. The presented model, however, which includes “bulk water”, “diffuse layer” and “interlayer” domains assumed to be in equilibrium locally, is not suitable for compacted bentonite. Furthermore, no description whatsoever is presented for how this equilibrium is supposed to be maintained. The model is therefore incapable, even principally, to account for swelling — the most profound feature of bentonite in contact with an aqueous solution. Note also that discrimination between “diffuse layer” and “interlayer” domains is based on the pure fantasy of “stacks” as fundamental structural units.
We also showed that the presented Nernst-Planck framework was incorrectly derived, and after having sorted out how it can be reinterpreted,2 we noted that the suggested “concentration” and “diffusion potential” contributions to the diffuse layer flux where completely unfounded.
“From diffusive flux to diffusive transport equations”
In this section I expected to be given an overview of how all the previously introduced model components are supposed to fit together in an overall description for bentonite. With so many parts, there are a large number of quantities to consider. Apart from all the species concentrations in the different “porosity domains”, TS15 have also introduced e.g. electrostatic potentials (eqs. 17, 18, 21, 22, 39, 48, 56 in TS15), adsorption sites on “basal surfaces” (eq. 19 in TS15), “exchanger” sites (eq. 24 in TS15), “layer edge amphoteric” sites (eq. 28 in TS15), models for activity coefficients and their spatial derivatives (eqs. 58, 60, 64 in TS15), and entertained the possibility of having varying sizes of the “porosity domains” (although no constitutive relations has been stated).
Instead, the only thing related to a model description here is a restatement of the mass conservation law. This was already presented in eq. 4 in TS15, but is here incorrectly called the “diffusion equation” (TS15 eq. 65), and stated with an incorrect sign (TS15 eqs. 65, 66 and 68). TS15 express it in its final form as (I have here corrected the sign error, and suppressed an index \(i\))
where \(\phi_\mathrm{bulk}\), \(\phi_\mathrm{DL}\) and \(\phi_\mathrm{exch}\) denotes the bulk water, “diffuse layer” and “interlayer” porosites, respectively; \(c_\mathrm{bulk}\), \(c_\mathrm{DL}\), \(c_\mathrm{exch}\) are the concentrations of the considered species in these “porosity domains”; and \(j_\mathrm{bulk}\), \(j_\mathrm{DL}\), and \(j_\mathrm{exch}\) are the corresponding domain fluxes (presumably given from the previously presented Nernst-Planck framework?).
That’s it.
As the authors stress the importance of adsorption processes throughout the article (even on montmorillonite basal surfaces), I find it very odd to here present an equation that completely omits them. Somewhat ironically, adsorption was included previously, in the section titled “Diffusion basics” (eq. 6 — 8 in TS15). Instead, the above equation (eq. 1) implies mechanisms that may alter the sizes of the “porosity domains” (i.e. \(d\phi/dt \neq 0\), \( d\phi/dx \neq 0 \)). But the article has not presented any constitutive relations for such mechanisms! This whole model presentation feels like having been handed a heap of irregular puzzle pieces with a promise of a grand result, while the reference photo belongs to a different puzzle.
Although eq. 1 provides little concrete information on the actual model, it still manages to contain a fatal flaw: the three domain fluxes are simply added to form some sort of a “total” flux. But this is not how diffusive fluxes work! The first real post I wrote on this blog covered this issue. There we noticed that domain fluxes are added in essentially all publications where multi-porous models are applied to bentonite. To see that separate domain fluxes are not additive should be as simple as considering some specific domain configuration. A trivial example is two domain types connected in series
It is easy to see that the resulting flux in this case cannot be described as a sum of independent domain contributions (e.g, the flux vanishes if \(D_1 = 0\), independent on the value of \(D_2\)). More generally, we may instead refer to one of the favorite references on diffusion in the bentonite research field: Crank (1975) has an entire chapter on this topic (“Diffusion in heterogeneous media”).
It really feels silly to point out, but the knowledge that domain diffusivites generally don’t add was established long before any numerical reactive transport tools were developed. I have trouble expressing what an incredible own goal this procedure is: even if it made sense to partition compacted bentonite into various “porosity domains”, using eq. 1 will still lead to incorrect inferences.
“Applications”
Rather than providing the reader with an actual model overview, TS15 proceed with presenting three different cases, which were modeled with either “CrunchFlowMC” or “PHREEQC”. These case studies are motivated with that they
[…] are used to illustrate the importance of considering coupled diffusion/surface reaction effects in order to understand and to predict migration processes and associated parameters in charged porous media, especially clays.
Let’s keep this formulation in mind as we go through the cases. (Spoiler: we will not be illustrated the importance of much, nor will we be able to understand or predict anything.)
This is a diffusion and “sorption” study of cesium, sodium and iodide in pure Na-montmorillonite. Tracer through-diffusion has been performed for each of these ions in samples of 0.8 g/cm3, at three different background concentrations (NaCl): 0.01 M, 0.1 M, and 0.5 M.
This is the “uphill” diffusion study. It presents the result of two through diffusion tests in pure Na-montmorillonite (1.9 g/cm3), where a Na tracer is observed to migrate from a 0.1 M NaClO4 reservoir to a 0.5 M NaClO4 reservoir, although the tracer concentration in the 0.1 M reservoir is lower than in the 0.5 M reservoir.
This paper presents the results of performing Ca-to-Na ion exchange on initially pure Ca-vermiculite (1.8 g/cm3). Disc-shaped single crystal vermiculite samples were immersed in initially pure NaCl solutions, and the evolution of calcium concentration in these solutions was monitored. The samples were prepared in such a way that out-diffusion only occurred at the outer edge of the vermiculite discs. Tertre et al. (2015) present four such tests, performed with NaCl concentrations 0.003 M, 0.05 M, 0.1 M, and 1.0 M. In addition, three tests were performed with NaCl concentration 0.05 M, which were terminated after 1.94, 7.01, and 18.06 days, respectively. Subsequently, the radial distribution of calcium was measured in these samples, giving “snapshots” of the internal Ca profile.
A common theme of these studies is that they primarily demonstrate effects of exchangeable cations being mobile. Tachi and Yotsuji (2014) clearly show the commonly observed effect of cation “effective diffusivity” becoming increasingly large as the background concentration is lowered, which has been unambiguously demonstrated to be an effect of “interlayer diffusion being the dominant pathway”. Glaus et al. (2013) is a proof-of-concept demonstration of a consequence of the exchangeable cations dominating mass transfer, as I discussed in some detail here. Tertre et al. (2015) assert from the start that “For this type of model system, the interlayer region is the only pore space that contributes to the overall diffusion process […]”.
Some sort of quality analysis of the data being modeled, e.g. a separation of signal and noise. It should also be motivated why certain data is modeled while other is not.
A summary that relates the model results to actual physical processes, and discusses possible implications.
Tachi and Yotsuji (2014)
Without commenting on it, TS15 only model results obtained at background concentration 0.1 M and only in samples of length 10 mm. A reason for this may be that Tachi and Yotsuji (2014) only present reservoir concentration evolutions and final state concentration profiles for all ions at these conditions. However, TS15 anyway disregard the final state profiles and only compare their model with the concentration evolutions. Furthermore, for cesium, the original article contains plots also for background concentrations 0.01 M and 0.5 M. Tachi and Yotsuji (2014) actually present fitted model parameters for all tests. If TS15 were serious about exploring this type of diffusion they could consequently have made a systematic comparison rather than just fitting a model to some rather arbitrarily chosen test results. This is particularly remarkable, as the most prominent feature of tests like this — that the “effective diffusion coefficient” for cations increases essentially without bound with decreasing background concentration, while the same quantity for anions approaches zero — is not really explored, when they only model results from a single background concentration.
It is also clear that TS15 show no interest in the quality of the data. Looking at Tachi and Yotsuji (2014) in a bit more detail, the data has some flaws and inconsistencies. For example, for all background concentrations, Tachi and Yotsuji (2014) report two quite different values of the “anion accessible porosity”,3 depending on whether the sample is 5 or 10 mm long. (TS15 “conveniently” choose the value 0.421 and ignore the value 0.635.) A further inspection also indicates that filter restriction has influenced some of the data, although they have attempted to eliminate such artifacts.4
TS15 don’t clearly state what model components they include, and it is essentially impossible to figure out the exact model used for this exercise. Half way through the section, the model is referred to as the “bulk + diffuse layer water diffusion model”, so it is quite safe to state that they have only included a bulk water and a “diffuse layer” domain. As the description in TS15 is fundamentally based on the (flawed) idea that we can distinguish between “external” and “internal” surfaces in compacted bentonite, it is quite remarkable that the “interlayer” domain is here completely left out. To me, this suggests that TS15 are not themselves especially serious about differing between “diffuse layers” and “interlayers” (after all, this difference is a fantasy, as I have argued throughout the review). This sloppy approach to modeling is, in my opinion, a recipe for ending up with an overparameterized mess. It is also worth noting that TS15 simply fix the size of the the bulk water domain by requiring the model to be “in close agreement” with measured “anion accessible porosity”.5 Thus, after 34 pages of text containing a myriad of mathematical expressions and a specific “consideration of electrostatic effects,” we ultimately just end up with knob-twiddling.
Speaking of electrostatic effects, TS15 don’t comment how aspects of multi-component diffusion influence the results. It is not even clear that the Nernst-Planck framework has been used in this particular modeling. For example, only a single set of fitted tracer diffusion coefficients are reported6 (and no transport parameters are reported for the main electrolyte). Are these supposed to relate to the bulk or the “diffuse layer” domain? I find this lack of discussion quite remarkable, given the emphasis in the rest of the article on the idea that ion diffusion in bentonite is supposed to be fundamentally “non-Fickian”.
TS15 do not even manage to clearly communicate the principal reason as for why the model “makes it possible to calculate the diffusive flux of neutral species, anions and cations with the same conceptual model and with physically feasible parameters.”7 This reason is — of course — that the model allows for exchangeable ions to move and that it provides a mechanism (Donnan equilibrium) for altering the relative ion concentrations in the “diffuse layer” domain. In fact, a more reasonable analysis demonstrates that tracer through-diffusion in bentonite can be satisfactory modeled using a single homogeneous domain for the clay. A homogeneous description is also compatible with basically all other experimental findings in compacted bentonite, as we have discussed massively on the blog.
In contrast, TS15 assume, not only that the montmorillonite in this particular test contains 50% bulk water, but also the existence of a Stern Layer — with corresponding ion immobilization — on montmorillonite basal surfaces. As neither of these assumptions are justified or reasonable, it is clear that the resulting model is overparameterized. Any successful fit thus provides little real information or insight, which also becomes almost comically clear when it is concluded
Results are plotted in Figure 19. The tortuosity values follow the order \(\tau_\mathrm{I^-} < \tau_\mathrm{HTO} < \tau_\mathrm{Na^+} < \tau_\mathrm{Cs^+}\), indicating that the tortuous diffusion pathways are not the same for all of these species. Or alternatively, that the adsorbed species in the Stern layer, considered in the calculations as immobile, are in fact mobile.
The result of the modeling exercise indicates either one thing, or a completely different thing!
Note that TS15 here put forward the bizarre notion that each separate species diffuse in different pore structures, with different “tortuosities”. They apparently don’t dismiss the untenable idea that cesium (with fitted “tortuosity” 0.136) for some reason diffuses though a much less meandering pore network than water (with “tortuosity” 0.047). In reality, the much larger “tortuosity” (which here means a less tortuous network…) for cesium as compared with water indicates that the model underestimates the amount of mobile cesium in the “diffuse layer” and compensates for this by giving it a too large diffusivity. This is signature behavior of an overparameterized model.
How this treatment and way of reasoning is supposed to “illustrate the importance of considering coupled diffusion/surface reaction effects” should be a mystery to any reasonable reader.
Glaus et al. (2013)
Things get even worse, in my opinion, as TS15 next present a modeling of the “uphill” test. Providing a solid explanation for this test could have been a major contribution to the article, as it earlier has claimed that the “uphill” effect is an example of “non-Fickian diffusion processes” and has implied that the effect is caused by non-trival electrostatic couplings. But TS15 seem genuinely uninterested in analyzing how the “uphill” effect arises in their model. Again, the adopted model is not presented in full, and focus is mainly on irrelevant details, such as filter diffusivity.8 The only attempt at describing a mechanism for “uphill” diffusion is half a sentence that says
[…] the macroscopic driving force of the diffusion is the diffusion potential in the diffuse layer, as shown in Figure 12.
But “Figure 12” shows results of “example 3”, from the section on the Nernst-Planck framework (discussed here), rather than results from the actual “uphill” test modeling. The burden of connecting “Figure 12” with the actual “uphill” test is completely left to the reader. I find this very peculiar for several reasons. To begin with, as TS15 evidently have modeled the actual “uphill” test, why don’t they refer to and show the “diffusion potential in the diffuse layer” in the actual model? And although “Figure 12” shows an “uphill” cation flux, the Nernst-Planck transport equations are not solved in “example 3”; in these examples, flux contributions are calculated from imposed linear concentration profiles in a bulk water domain. But since the “uphill” test here has been modeled with a tool that apparently solves the Nernst-Planck transport equations, I find it incomprehensible that these results are not reported. It is also worth noting that TS15 don’t compare their model with the final-state concentration profiles, even though these are readily available in the original publication.
The earlier examples, moreover, assume a density of approximately 1.0 g/cm3 (porosity 0.64), and a bulk water domain that dominates the pore volume. The “uphill” test, in contrast, was conducted at nominal density 1.9 g/cm3 (porosity \(\sim\) 0.3). TS15 themselves explicitly comment that “[a]t this high degree of compaction, the actual presence of bulk water is not certain”.9 Other conditions also differ strongly between these systems. The “uphill” test was performed with NaClO4 as main electrolyte, while “example 3” uses NaCl. “Example 3” has boundary concentrations 0.1 M and 0.001 M for the main electrolyte, while the actual “uphill” test, in contrast, has 0.5 M and 0.1 M.
Disregarding these glaring differences between the actual “uphill” test and “example 3”, the explanation given by TS15 in the above quotation is that the cation tracer ions move “uphill” due to “the diffusion potential in the diffuse layer”. In an earlier part of this review we demonstrated that the way TS15 define the “diffusion potential” contribution to the flux is obvious nonsense, based on misunderstanding the electric potential. To remind ourselves, in “example 3” TS15 make the absurd claim that a tracer concentration profile in the “diffuse layer” that looks like this (this is part of “Figure 12”)
makes NO “concentration gradient” contribution to the flux (because TS15 define such contributions exclusively in terms of bulk water concentrations). Instead, the diffuse layer cation tracer flux in “example 3” is supposed to be driven by an electric field (the “diffusion potential” contribution) in the wrong direction.
We have shown that these preposterous definitions of flux contributions can be corrected, with the correction term involving the gradient of the Donnan potential.10 With reasonable flux definitions, we demonstrated that the “uphill” flux in “example 3” is essentially completely governed by the contribution from the “diffuse layer” concentration gradient (i.e. that the cation tracer flux is “Fickian”). Recently on the blog, we have also calculated the electrostatic potential within the homogeneous mixture model and specifically demonstrated that effects of electromigration on the tracer flux is negligible in the “uphill” test.
Rather than identifying any of the above points, TS15 instead spend a large part of this section discussing that several models, which “are totally different from a conceptual view”, can be fitted to the “uphill” diffusion test data. But all models that can be fitted to the “uphill” test data have this ability because they (i) assume mobility of exchangeable ions and (ii) provide a mechanism for ion equilibrium with bulk water. From the point of view of fitting the data, it is secondary if a model treats the ion equilibrium via “exchange sorption” or Donnan equilibrium,11 or if the compartment containing the exchangeable ions is referred to as “interlayer”, “diffuse layer” or interlayer. That TS15 choose to emphasize that their model fits “equally good”, while it contains several additional and unjustified assumptions, simply indicates that they don’t consider the dangers with overparameterization.
The presentation of the modeling of the “uphill” test in TS15 does not “illustrate the importance of considering coupled diffusion/surface reaction effects in order to understand and to predict migration processes…”. Rather, it obscures process understanding.
Tertre et al. (2015)
As with the previous cases, the description of the modeling of Tertre et al. (2015) lacks sufficient detail, preventing the reader from determining exactly which model was used. Actually, the only model information given is that the data was “reinterpreted using the interlayer diffusion option of PHREEQC”. This must obviously mean that an “interlayer” domain is included in the model, in contrast to the previous cases. But are other domains included? (we have previously been informed, in passing, that “PHREEQC” requires a bulk water domain).
Furthermore, it is not clear if a Stern layer is included in this model, i.e. if some of the exchangeable ions are assumed immobilized, as in the previous cases. As not a word is spoken about this, we reasonably must assume that no Stern layer is included. If this is the case, the inclusion of an immobilization mechanism when modeling Tachi and Yotsuji (2014) and Glaus et al. (2013) becomes even more conspicuous. In fact, TS15 state about Tertre et al. (2015)
This experiment showed unambiguously that interlayer diffusion exists and it made it possible also to quantify the diffusion coefficient for \(Ca^{2+}\) in the interlayer.
I find this statement remarkable for a couple of reasons. As TS15 don’t say anything similar when discussing the other studies, I here get the impression that they haven’t comprehended that “interlayer diffusion” has been unambiguously demonstrated much earlier than in Tertre et al. (2015). Also, if TS15 now acknowledge that interlayer diffusion “exists” in bi-hydrated vermiculite, how come that they don’t assume this to be the primary mode of transport in the other models, but instead add an immobilization mechanism? Are ions supposed to become less mobile in less dense systems with lower layer charge density? We should also remember that earlier in the article, TS15 describe the “interlayer” as pure Stern layers. So, how is it, are Stern/interlayer ions supposed to be mobile or not? Again, I think this relaxed attitude towards when and how various domains are included, and how they are treated, demonstrates that TS15 themselves don’t take the concepts of “diffuse layer” and “interlayer” seriously.12
Furthermore, the “reinterpretation” of this experiment is entirely untenable. Tertre et al. (2015) put a lot of effort in demonstrating (using “Brownian dynamics simulations”) that the observed diffusion is strongly influenced by processes occurring at the interface between the sample and the external solution. This makes sense, as we may expect huge concentration gradients within the clay when two different cations are involved. Such gradients are difficult to maintain, and the resulting flux can instead be expected to be controlled by interface transfer resistance. This is similar to how filters limit the flux in cation through-diffusion tests at low ionic strength. In the “reinterpretation”, TS15 completely neglect any possible interface transfer resistance, claiming
It was possible to reproduce the data with the same level of quality as the Brownian dynamics calculations by considering an interlayer \(Ca^{2+}\) diffusion coefficient value of \(0.8\times 10^{-11}\) \(\mathrm{m}^2\cdot \mathrm{s}^{-1}\), together with an interlayer \(Na^{+}\) diffusion coefficient of \(4\times 10^{-11}\) \(\mathrm{m}^2\cdot \mathrm{s}^{-1}\), \(1\times 10^{-11}\) \(\mathrm{m}^2\cdot \mathrm{s}^{-1}\), \(0.1\times 10^{-11}\) \(\mathrm{m}^2\cdot \mathrm{s}^{-1}\), and \(0.1\times 10^{-11}\) \(\mathrm{m}^2\cdot \mathrm{s}^{-1}\), for the experiments at NaCl concentration of 1, 0.1, 0.05 and 0.003 \(\mathrm{mol}\cdot \mathrm{L}^{-1}\) respectively. The decrease of the \(Na^{+}\) interlayer diffusion coefficient with NaCl concentration is in agreement with MD results from Tertre et al. (2015), which show a decrease of its value with an increase of the \(Ca^{2+}\)/\(Na^{+}\) occupancy ratio in the interlayer (Fig. 21c).
The last sentence is false. Tertre et al. (2015) indeed report a decrease of the sodium self-diffusion coefficient, but this decrease is lower than a factor 3.13 In the model of TS15, in contrast, this decrease is a factor 40 (!), which certainly cannot be considered “in agreement”. In addition, experimentally, Kozaki et al.(2005) observed no systematic decrease of Na diffusivity with increasing Ca fraction, in bi-hydrated montmorillonite; if anything, they observe a slight decrease (25 — 60%) of Na diffusivity only in pure Ca-montmorillonite. TS15 anyway goes so far as to conclude this part by stating
Consequently, the apparent decrease in \(Ca^{2+}\) interlayer diffusion coefficient can also be interpreted as a result of the decrease of the \(Na^{+}\) interlayer diffusion coefficient that arises from the coupling between the diffusion of these two species through the diffusion potential term in Equation (57).
Let’s unpack the serious error of reasoning on display here: rather than taking into account interface transfer resistance — a process that we have every reason to believe is active, and that is expected to produce the observed behavior — the observed behavior is supposed to be caused by an unjustified 40-fold decrease of the sodium self-diffusivity, as the external concentration decreases. A mobility decrease that do not even correlate directly with the calcium content of the clay! Note also that TS15 state that the decrease in sodium diffusivity is caused by electromigration (“the diffusion potential term in Equation (57)”). But, as far as I understand, these sodium diffusivities were just put in by hand! (See previous quotation.) It is completely unreasonable that TS15 are here allowed to provide this “explanation” without showing a single result from the actual modeling of how this “diffusion potential term” is supposed to change under different conditions.14
It feels silly to point out that this modeling does not in any way “illustrate the importance of considering coupled diffusion/surface reaction effects in order to understand and to predict migration processes…”. Instead, it is a horrific example of “modeling” as a game, where the only aim is to be able to fit a model to some arbitrary data.
The overall impression of these modeling cases is that TS15 do not seem interested in understanding or communicating how compacted bentonite really works: models are not fully described, and components seem included or disregarded pretty much on a whim; no attention is paid to the quality of the data that is modeled, nor to how data is chosen; and discussions are completely absent regarding how the modeling can aid process understanding. I also find it curious how little these modeling cases connect with the main topics discussed in the rest of the article. For example, very little is said about the impact of multi-component diffusion, even though “non-Fickian” diffusion is a a major theme of the article (it is often not even clear when and how multi-component diffusion has been implemented). Likewise, although sorption processes are included in some of the model cases, we are not told anything about their significance. And not a word is spoken about evolving volumes of the various “porosity domains”, even though such processes seem to be taken seriously in other parts of the article.
“Summary and perspective”
We have finally arrived at the last page of the article. The first paragraph of this section mainly concerns the shortcomings of the traditional diffusion-sorption model (“the classical Fickian diffusion model”)
In this context, the classical Fickian diffusion model applied in the framework of a single pore diffusion model with linear adsorption processes (\(K_D\) model) appears to be inappropriate for describing diffusion data without making less than satisfying modeling assumptions, such as i) different definitions of the porosity as a function of the nature of the tracer of interest (see anion accessible porosity) and as a function of the conditions (anion accessible porosity change with time; ii) change of the adsorption parameters from batch to diffusion experiment; and iii) physically unrealistic pore diffusion coefficients (or tortuosity values).
I agree with that the traditional diffusion-sorption model is not suitable for bentonite. But this has been known for a long time, as I have argued from the beginning of this review. That TS15 use this model as a starting point — and argues for modifying it rather than dismissing it — is in my head a recipe for disaster.
I want to emphasize that all empirical evidence points to that compacted water saturated bentonite is a “single pore” material. The main problem with the traditional diffusion-sorption model is not that it assumes a “single pore”, but that this “single pore” is assumed to contain bulk water. Letting go of the bulk water allows for a satisfying bentonite model using a single pore type. I’ve elaborated on these points here and here.
This first paragraph also says
Diffusion processes through clay materials is the result of a complex interplay of transport and non-linear adsorption processes under the influence of electrostatic fields.
This formulation must be interpreted as summarizing what has been covered in the article as a whole. But I don’t agree with this description, and throughout this review we have exposed flaws and shortcomings in much of the presented material. Of course, ion diffusion is generally influenced by electric fields, since the diffusing entities carry charge. But we have shown that the definition of a “diffusion potential” made by TS15 makes no sense and is based on misunderstanding how electric potentials function. With corrected definitions we have further shown that processes described by TS15 as being due to a “diffusion potential” is actually mainly driven by concentration gradients, i.e. the diffusion processes are “Fickian”. I see it as a major problem that many researchers don’t recognize diffusion in compacted bentonite as simpler than usually described.
This sentence also claims that “non-linear adsorption processes” are involved generally in ion diffusion in bentonite. But this is not the case! The ions that the article mostly focuses on — e.g. sodium, calcium, chloride and iodide — don’t show any signs of adsorption15 at all, let alone “non-linear” adsorption.
The second paragraph of this section is fully devoted to “non-linearity of adsorption processes for strongly adsorbed species”, with particular focus on cesium. I find this peculiar, as non-linear sorption is only brought up in a single small part in the article, and as nothing is said about non-linearity in the the reported “application” that involves cesium (Tachi and Yotsuji, 2014)
The third paragraph begins
Recent developments of selected RT [reactive transport] codes that can handle diffusion processes in diffuse layer and interlayer porosities made it possible to model the diffusion data of neutral, anionic and cationic species within the same conceptual framework.
Here is presumed that partitioning of the pore space into “diffuse layer” and “interlayer” domains makes sense. But we have thoroughly discussed that this whole notion — which is based on the fantasy concept of “stacks” as fundamental structural units of compacted bentonite — makes essentially no sense. And, as we noted earlier, TS15 themselves employ these “porosity domains” for convenience, rather than from being constrained by empirical evidence.
Moreover, it is not the ability to define both “diffuse layer” and “interlayer” that makes it possible to treat any type of species “within the same conceptual framework”16 Rather, a coherent model for compacted bentonite is made possible by realizing that exchangeable ions are mobile and by treating the corresponding ion equilibrium when required. This is (and has been) most adequately made in a homogeneous model.
The third paragraph continues
Also, the contribution of the diffuse layer and/or the interlayer to the overall diffusion of ions makes it possible to explain the origin of the apparent acceleration of cation diffusion as compared to water, which otherwise would require unrealistic tortuosity values for cations in classical Fickian diffusion models.
It is not true generally that cation diffusion is “accelerated”. Speaking of “accelerated” cation fluxes is mostly relevant for steady-state in conventional through-diffusion tests at low background concentration. Writing like this makes me suspect that TS15 have not identified this distinction, especially since they do not recognize the importance of interface equilibrium. As I discussed in the first part of the review, e.g. sodium and chloride show almost identical diffusive behavior in bentonite. The additional effects observed in through-diffusion is completely due to Donnan equilibrium at the interfaces to the external solutions, as has been explained in detail long before the publication of the present article. Again, TS15 contrast with “classical Fickian diffusion models” — but it has been fully clear from the start that the traditional diffusion-sorption model does not apply to compacted bentonite. The way TS15 here use the phrasing “diffuse layer and/or interlayer” again indicates that they don’t take their own concepts seriously. The third paragraph ends
RT modeling has also helped to improve our understanding of anomalous diffusion behavior such as that of up-hill diffusion.
This is a horrible statement. That they refer to the “uphill” effect as “anomalous” tells me that they have neither understood this experiment, nor how bentonite works.17 And if they by “RT modeling” mean the previously presented modeling of the “uphill” effect, nothing can be further from the truth than claiming that it has improved understanding. I also find it significant that they don’t connect the “uphill” test to the previous statements in the same paragraph; the “uphill” test was designed to demonstrate that cation diffusion is not simply “accelerated” (it is, in a sense, conventional tracer through-diffusion that is “anomalous”).
The fourth paragraph reads
Despite the successes of these new RT modeling approaches, it must be stressed that the model and its parameters derived from diffusion experiments are not always unique. Two examples given above highlight the fact that several different conceptual models can provide equally good fits of the data. As such, the modeling effort is typically under constrained, a fact that explains the multitude of conceptual and numerical models available in the literature that describe the ionic transport properties of clay media (Leroy et al. 2006; Appelo and Wersin 2007; Gonçalvès et al. 2007; Birgersson and Karnland 2009; Gimmi and Kosakowski 2011; Tachi et al. 2014).
I strongly disagree with this whole line of reasoning. The multitude of models is not explained by them being “under constrained”; it is explained by most of them being overparameterized (which is poison).
Serious modeling work requires that all included components be evaluated and justified on physical grounds. I see very little of this in the contemporary bentonite scientific literature. We can use the “uphill” test modeling to illustrate this point. The model of this test in TS15 includes, among other things, a mechanism for sodium adsorption and immobilization on basal surfaces (a Stern layer). The test, however, has already been demonstrated to be well described by models that don’t include such a mechanism. This test can therefore not in itself be used to motivate the inclusion of a Stern layer. On the contrary, if there are no other reasonable arguments for why sodium is supposed to adsorb and become immobilized in montmorillonite, it is bad modeling practice to include a Stern layer component.
To make an absurd analogy: if I, as a modeler, don’t have to motivate the included components, I may claim that bentonite contains invisible unicorns that eat anions (or whatever), as long as my model can be fitted to some arbitrary data. This may sound funny, but at least in my head, contemporary bentonite models are quite full of “unicorns”, e.g.
They include significant amounts of bulk water
They rely on the fantasy concept of stacks
Equilibrium between various domains is maintained without a mechanism
They postulate regions completely devoid of anions
Diffusive fluxes from various domains are added
Simple ions, e.g. sodium, are assumed to bond covalently (or whatever) to montmorillonite basal surfaces
In the last paragraphs of this section, TS15 argue for that more research is needed to overcome the claimed problem of models being “under constrained”, using e.g. molecular dynamics simulations and developing new observation techniques. In contrast, I firmly believe that for modeling activities to be meaningful, researchers instead need to spend much more effort scrutinizing and analyzing their models — and the data they are fitting them to. This is much of what I’m trying to do on this blog.
Final comments
My main interest in doing this review has not been in the specific article that we have dissected, but in how it reflects the state of a broader part of the bentonite research field. After finishing, my initial opinion is strengthen: this research field is in a terrible state. I am now fully convinced that reasonable support is nowhere to be found for several of the concepts frequently adopted in contemporary bentonite descriptions. This applies in particular to the ideas of “stacks” as fundamental structural units, the presence of bulk waterwithin the bentonite, and a general adsorption/immobilization mechanism for ions on montmorillonite basal surfaces (Stern layer). To me, it is also clear that this research field lacks knowledge of how salt exclusion and swelling actually work in compacted bentonite, as well as insight into how central these phenomena are for an adequate description.
In today’s bentonite scientific literature, you can simply close your eyes and point at random to find articles that peddle much of the type of nonsense listed above. An illustrative (literally!) example of this legacy is found in Chen et al. (2024)
In the past decades, scholars have carried out a lot of research on the pore structure of compacted bentonite, and it is now generally accepted that there are three different types of pores, including inter-aggregate pores, inter-particle pores and interlayer (or inter-laminar) pores (Lloret and Villar, 2007; Wang et al., 2014), as shown in Fig. 1.
[…]
In existing research, water existing inter-aggregate pores, interparticle pores and interlayer pores are usually referred to as free water, double layer water and interlayer water. In general, anions only diffuse in free water because anions are expelled from the interlayer water and double layer water owing to exclusion effect (Glaus et al., 2007; Wu et al., 2020). Adversely [sic] cation diffusion is supposed to occur in all three types of water due to positive adsorption, corresponding to free water diffusion, surface diffusion and interlayer diffusion, respectively (Melkior et al., 2009; Tachi and Yotsuji, 2014; Yang and Wang, 2019)
“Fig. 1” in Chen et al. (2024) looks very similar to this18
The saddest aspect of this quotation is that it is partly correct: “Scholars have carried out a lot of research” for “decades”, and this view is “generally accepted”.
I cannot say that doing this review has answered my question as to why this is the state of the bentonite research field, but maybe a hint is given by the attitude expressed in TS15 towards modeling and model development. I believe this field will have trouble progressing as long as “modeling” is synonymous with getting arbitrary mathematical descriptions to fit arbitrarily chosen data, padded with empty talk.
Footnotes
[1] As I have commented in the earlier parts: TS15 are fond of using the general terms “clays” and “clay minerals”, while it is clear that the publication mainly focus on systems with substantial ion exchange capacity and swelling properties. Here we will continue to use the term “bentonite” for these systems, and ignore the frequent references in TS15 to more general terms.
[2] Such reinterpretation involves the gradient of the bulk water electrical potential — a potential that TS15 put strictly equal to zero. It also involves the gradient of the Donnan potential — a potential that TS15 mistake for the electric potential in the diffuse layer, when it actually describes the potential difference between bulk and diffuse layer.
[3] Tachi and Yotsuji (2014) report “rock capacity factors” for iodide, which erroneously often are interpreted as anion-accessible porosities. TS15, as we have seen, go “all in” on this concept, while simultaneously admitting that it is fictitious. (?!)
[4] We have noted earlier that it seems very difficult to completely eliminate the effects of interface transfer resistance.
[5] Note that the “correct” value is the arbitrarily selected experimental result 0.42, while the other experimental result of 0.64 is ignored. Also remember that the way this parameter varies with ionic strength is not at all explored by TS15, as they only model results from tests with 0.1 M background concentration.
[6] TS15 report “tortuosities”, rather than actual diffusion coefficients. In a bentonite context, the only way such quantities make sense is as a measure of the diffusion coefficients in terms the corresponding bulk water value, as we discuss here.
[7] I object to that the model parameters are “feasible”. It is in my head a completely ludicrous idea that half the pore volume in pure sodium montmorillonite at 0.8 g/cm3 should contain bulk water — the swelling pressure for a 0.1 M NaCl background concentration is expected to be above 0.4 MPa! Also, the idea that the diffusivity of cesium in montmorillonite is much larger than for sodium, iodide or water is completely unreasonable. In fact, TS15 state that “feasible” simply means a cesium diffusivity that is smaller than for pure bulk water. This shows that they are under the impression that “\(D_e\)”, rather than “\(D_a\)”, quantifies the actual diffusivity in the clay. For a further discussion on this, see here.
[8] Including filter diffusivity in this modeling is certainly not irrelevant per se. However, TS15 merely assign a seemingly random value to this quantity and do nothing more about it. All subsequent inferences are thus contingent on this particular value, yet the authors have neither demonstrated if nor how it influences the overall process.
[9] Although I agree with that these systems don’t contain any appreciable amount of bulk water, we note that no reference is given for this claim. I find this annoying, as TS15 simultaneously don’t hesitate to ascribe 50% bulk water to pure Na-montmorillonite at 0.8 g/cm3. As commented earlier, such a system is expected to have swelling pressure above 0.4 MPa.
[10] We still found serious problems with the model formulation, as further discussed in part 5 of the review.
[12] As always, we should also remember that the distinction betweeen “diffuse layers” and “interlayers” (with quotation marks), or similarly, between “inner” and “outer” basal surfaces, is pure fantasy.
[13] It’s not completely straightforward to extract exact MD values from Tertre et al. (2015). But, discussing them in terms of “surface mobility”, they write: “the mobility for Na is variable from approximately 0.04 to approximately 0.015 when the equivalent fraction of Ca in the solid increases from 0 to 1.” This is a decrease by a factor 2.7.
[14] Note, for instance, that sodium is set to be faster than calcium for the cases of 1.0 M and 0.1 M NaCl, while it is set to be slower than calcium for the cases of 0.05 M and 0.003 M NaCl. Is calcium supposed to be able to retard the sodium flux to such an extent that the sodium ion in the end diffuses slower than the calcium ion?! Note also that the sodium mobility in the TS15 model is lowered by an order of magnitude as the external concentration is only lowered from 0.1 M to 0.05 M! (Or, if the corresponding figure rather than the text is correct, the mobility is even lowered by a factor 40 (the later sections of the paper contain an unacceptable amount of typos of this kind).)
[15] Of course, if ion exchange is supposed to be an “adsorption” process, any cation do “adsorb”. But using such a label for a process that actually may enhance the diffusive flux is, in my opinion, a very bad idea.
[16] To me, the “conceptual framework” promoted in TS15 is “add stuff as you please (but keep bulk water at all costs)”.
[17] Calling the “uphill” effect “anomalous” also seems to contradict the previous general statement that “Diffusion processes through clay materials is the result of a complex interplay of transport and non-linear adsorption processes under the influence of electrostatic fields.”
[18] This only represents a part of “Fig. 1” in Chen et al. (2024), which is explicitly stated to represent compacted water saturated bentonite. I will not elaborate on what is wrong with this figure, but here are some questions to ask: 1. Does this figure represent a realistic size distribution of montmorillonite TOT-layers? 2. Does it represent a typical size distribution of accessory minerals? 3. What is the effective montmorillonite dry density of the depicted system? 4. How is swelling pressure maintained? 5. What keeps “particles” and “aggregates” together? 6. How did this illustration pass peer-review?
Lately on the blog we have had a certain focus on the electric potential in compacted bentonite systems. In the ongoing post-publication review of Tournassat and Steefel (2015), for example, we have deep-dived into how electric potentials are treated in multi-porous models. We have also discussed the seeming “uphill” diffusion effect in different contexts. Although this effect is principally explained by the same mechanisms as for traditional cation tracer through-diffusion, we should address the potential difference that is present across the sample in an “uphill” test.
Here is presented a somewhat more general description of the electric potential difference across a bentonite sample, within the homogeneous mixture model. This treatment is essentially equivalent to how this so-called membrane potential is conventionally evaluated within the ion-exchange membrane scientific discipline. As usual on the blog, the message here is that compacted bentonite should not be modeled with various “porosities” and sorption “sites” (for ion exchange). Rather, from the perspective of ion transport,1 compacted bentonite appears to be well described as a conventional charged ion-exchange membrane.2
Multi-component diffusion in the homogeneous mixture model
The external solutions (labeled “1” and “2”) are specified by general species compositions, with the only constraint that they should be electrically neutral. We consequently consider a situation with possible chemical gradients — and corresponding mass transfer — across the bentonite sample, while the hydrostatic pressures in the two reservoirs are assumed equal.3 The values of the electric potential in the external solutions have been labeled \(\psi^{(1)}\) and \(\psi^{(2)}\), respectively.
Treating the bentonite as a single homogeneous phase, the electric potential has discontinuities at the external solution/clay interfaces, due to Donnan equilibrium. In addition, the potential may vary within the bentonite, due to diffusion of charged species with different mobilities (electromigration). Schematically, the steady-state electric potential profile can be illustrated like this
Here, \(\Delta \psi_\mathrm{Donnan}^{(1)}\) and \(\Delta \psi_\mathrm{Donnan}^{(2)}\) denote the potential changes due to Donnan equilibrium at the two interfaces.4 \(\Delta \psi_\mathrm{diff}\), which conventionally is named the diffusion potential, denotes the total change in potential across the sample due to electromigration. The membrane potential, \(\Delta \psi_\mathrm{m}\), can be expressed
Given the reservoir concentrations, the Donnan contributions can be calculated using the general framework, if also a value of \(c_\mathrm{IL}\) — which expresses the montmorillonite structural charge as a monovalent interlayer species concentration — is specified for the bentonite component. Such calculations also provide the corresponding sets of internal interface concentrations, i.e. \(\left \{c_{1}^\mathrm{int}(0), c_{3}^\mathrm{int}(0), c_{3}^\mathrm{int}(0), \ldots \right \}\), and \(\left \{c_{1}^\mathrm{int}(L), c_{3}^\mathrm{int}(L), c_{3}^\mathrm{int}(L), \ldots \right \}\), where we denote by \(c_i^\mathrm{int}(x)\) the concentration for species \(i\) at position \(x\) within the clay, and we assume the clay domain located between \(x=0\) and \(x=L\).
The sets of internal interface concentrations, in turn, constitute boundary conditions for solving e.g. the Nernst-Planck equation in the clay domain. Within the Nernst-Planck framework, the gradient of the electrostatic potential in the clay is expressed in terms of species concentrations and diffusivities as
where \(z_i\) and \(D_i\) denote, respectively, the charge number and diffusion coefficient in the clay domain, for species \(i\), and \(V_T = RT/F\) is the thermal voltage (we assume \(V_T\) = 25.7 mV here). From eq. 2 the diffusion potential can be evaluated.
Note that the problem of ending up with a too constrained model when both the Donnan equilibrium and the Nernst-Planck frameworks are invoked does not occur here. This is in contrast to the problems we recently discussed in the model of Tournassat and Steefel (2015). That model requires Donnan equilibrium at each point within the clay, while here it is only imposed at the two interface points.
In the following we will evaluate the membrane potential numerically in some different cases. We start, however, by analyzing the 1:1 system analytically, in order to get a better feel for these processes in compacted bentonite.
1:1 system
The pure 1:1 system has a single type of monovalent cation and a single type of monovalent anion (e.g. Na-montmorillonite in contact with NaCl solutions). The requirement of charge neutrality dictates equal concentrations of cations (\(c_+\)) and anions (\(c_-\)) in each external solution, and we write
where \(c^{(n)}\) is the electrolyte concentration in reservoir \(n\) (\(n\) = 1 or 2).
In this analytical treatment, we assume the often relevant condition of having small external concentrations as compared with the concentration of structural charge in the clay, i.e.
where \(\psi^{\star, (n)}\) is the Donnan potential. In eq. 6 we have ignored the activity coefficient correction factor; contributions to the membrane potentials from activity coefficient differences are expected to be small, and here we will not consider them.5 Note that Donnan potentials are negative, and that \(\Delta \psi_\mathrm{Donnan}^{(1)} = \psi^{\star, (1)}\) and \(\Delta \psi_\mathrm{Donnan}^{(2)} = -\psi^{\star, (2)}\). Utilizing eq. 6, we can express the total Donnan contribution to the membrane potential as6
where we also have continued assuming low external concentrations (eq. 4).
If we impose a constant internal concentration gradient, i.e. \(\nabla c_-^\mathrm{int} (x) = \Delta c_-^\mathrm{int}/L\), where \(\Delta c_-^\mathrm{int} \equiv c_-^\mathrm{int}(L) – c_-^\mathrm{int}(0)\), the diffusion potential can be written
The first term — the ideal Donnan contribution — depends only on the ratio of the concentration in the two reservoirs, and usually dominates over the diffusion potential (second term).
The diffusion potential is expected to be small under most circumstances, as it is seen to explicitly depend on \(1/c_\mathrm{IL}\). This behavior reflects that potential variations within the bentonite are reduced due to the presence of counter-ions (bentonite is a decent conductor). But the factor \(\Delta c_-^\mathrm{int}\) in eq. 11 contributes with an additional factor \(1/c_\mathrm{IL}\) to the diffusion potential, because of Donnan equilibrium (see eq. 6)
Note also that the diffusion potential only depends on the relative values of the diffusivities, and consequently vanishes if there is no difference in mobility between the cation and the anion.
Comparisons with experiment
We can compare the present theory and approximations with measurements reported in Yaroshchuck et al. (2007). In this study, the membrane potential (called the “concentration potential”) was measured across sodium montmorillonite of density 2.0 g/cm3, with one external solution kept at 0.1 M NaCl and the other raised to 0.2 M, 0.3 M, or 0.5 M. The very high density corresponds to a value of \(c_\mathrm{IL} \approx\) 6.0 M,7 and thus eq. 12 applies (see eq. 4).
In order to also investigate the influence of a diffusion potential we should adopt values for the individual diffusivities of chloride and sodium. Experimental tracer diffusion results indicate that these ions have quite similar mobility. E.g., in pure Na-montmorillonite at 1.8 g/cm3 and 298 K, Kozaki et al. (1999, 2001, 2005) report values in the range \(1.5\cdot 10^{-11}\) — \(2.5\cdot 10^{-11}\) m2/s for chloride, and \(2.1\cdot 10^{-11}\) — \(2.4\cdot 10^{-11}\) m2/s for sodium. From these values we can estimate a range for the factor (\(D_-/D_+-1\)) of -0.4 — 0.2. Rather than adopting such a value, however, we here assume the diffusivities to have the corresponding bulk water ratio (1.53), giving \((D_-/D_+ -1)\) = 0.53. This is similar to the treatment in the examples in Tournassat and Steefel (2015), which we have discussedrecently. Theoretical and experimental results are compared in the table below
Evaluations using cIL = 6.0 M, c(2) = 0.1 M, (D–/D+ – 1) = 0.53:
App-
rox-
ima-
tion
Full
Frame-
work
Exp.
\(c^{(1)}\) (M)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
\(\psi_\mathrm{m}\) (mV)
0.2
-87.4
-105.2
17.8
-0.011
17.8
-87.4
-105.2
17.8
-0.011
17.8
18
0.3
-77.0
-105.2
28.2
-0.030
28.2
-77.1
-105.2
28.1
-0.030
28.1
28
0.5
-63.9
-105.2
41.4
-0.090
41.3
-64.0
-105.2
41.2
-0.088
41.1
41
This table compares calculations performed using eq. 12 (columns 2 — 6), calculations performed using the full frameworks for Donnan equilibrium and the Nernst-Planck potential (columns 7 — 11), and experimental values (last column). We note that, for this very high value of \(c_\mathrm{IL}\), the calculated Donnan contributions (\(\Delta \psi_\mathrm{D}\)) are essentially identical whether or not the full framework is adopted. We also see that the calculated diffusion potential contributions are completely negligible: the largest value calculated is still below 0.1 mV! Finally, we note excellent agreement between calculated and measured membrane potentials.
The agreement with experiment suggests, not only that the membrane potential is completely determined by Donnan equilibrium in these systems, but that bentonite essentially play by the same rules as conventional ion-exchange membranes.2 In particular, these results8 are even more evidence for that all exchangeable cations are mobile in bentonite.
To explore the NaCl system further, let’s investigate how the results change for lower clay density. In the tables below are shown corresponding results as above, but for \(c_\mathrm{IL}\) = 3.0 M and \(c_\mathrm{IL}\) = 1.5 M, which roughly correspond to densities 1.6 g/cm3 and 1.1 g/cm3, respectively.
Evaluations using cIL = 3.0 M, c(2) = 0.1 M, (D–/D+ – 1) = 0.53:
App-
rox-
ima-
tion
Full
Frame-
work
\(c^{(1)}\) (M)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
0.2
-69.6
-87.4
17.8
-0.045
17.8
-69.7
-87.4
17.7
-0.044
17.7
0.3
-59.2
-87.4
28.2
-0.120
28.1
-59.4
-87.4
28.0
-0.116
27.9
0.5
-46.0
-87.4
41.4
-0.361
41.0
-46.7
-87.4
40.7
-0.336
40.4
Evaluations using cIL = 1.5 M, c(2) = 0.1 M, (D–/D+ – 1) = 0.53:
App-
rox-
ima-
tion
Full
Frame-
work
\(c^{(1)}\) (M)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
\(\psi^{\star,(1)}\) (mV)
\(\psi^{\star,(2)}\) (mV)
\(\Delta \psi_\mathrm{D}\) (mV)
\(\Delta\psi_\mathrm{diff}\) (mV)
\(\psi_\mathrm{m}\) (mV)
0.2
-51.8
-69.6
17.8
-0.18
17.6
-52.2
-69.7
17.5
-0.170
17.3
0.3
-41.4
-69.6
28.2
-0.48
27.8
-42.3
-69.7
27.4
-0.434
26.9
0.5
-28.2
-69.6
41.4
-1.44
39.9
-30.7
-69.7
39.0
-1.146
37.8
For \(c_\mathrm{IL}\) = 3.0 M, the difference between using the full framework or eq. 12 is seen to still only affect the evaluated membrane potentials on the order of tenths of mV. Only for the higher external concentrations in the system with \(c_\mathrm{IL}\) = 1.5 M are the differences becoming above 1 mV. Similarly, the diffusion potential is seen to be essentially negligible for all these cases.
Further investigation of potentials and fluxes
It should be emphasized that we are not actually solving the full Nernst-Planck transport framework in these examples. Rather, we calculate the corresponding potential difference as we impose a linear internal concentration profile. This is similar to the evaluation made by Tournassat and Steefel (2015) — although they impose concentration profiles in a presumed bulk water phase within the clay. Similar to that publication, we will here visualize the corresponding fluxes in some cases of interest.
The total flux of a charged species in the Nernst-Planck framework can be written as the sum of a “Fickian” contribution (i.e. proportional to the corresponding concentration gradient) and a contribution from electromigration (i.e. flux induced by the presence of an electric field).9
Below are plotted imposed concentration profiles, Nernst-Planck fluxes, and the electric potential profile, for the NaCl-system with \(c_\mathrm{IL}\)=3.0 M, \(c^{(1)}\) = 0.5 M, and \(c^{(2)}\) = 0.1 M (for which we previously calculated \(\Delta \psi_\mathrm{m}\) = 40.4 mV and \(\Delta \psi_\mathrm{diff}\) = -0.3 mV). To calculate fluxes we must choose absolute values of the diffusion coefficients, which we take to be \(D_\mathrm{Na}=1.33\cdot 10^{-10}\) m2/s and \(D_\mathrm{Cl}=2.03\cdot 10^{-10}\) m2/s.10
The total NaCl flux is essentially constant throughout the sample (we have adopted a sample length of 10 mm), demonstrating that the imposed linear concentration profile in essence is the steady-state solution. We see that the flux of chloride — which has a much smaller concentration than sodium — is completely dominated by the concentration gradient contribution (eq. 15), while the sodium flux has significant contributions from both the concentration gradient and the electric field (eq. 16). The picture is clear: the faster chloride ions diffuse with a rate set by their individual diffusion coefficient, while the induced electric field boosts the less mobile (but more abundant) sodium ions in order to “keep up”. The behavior is similar to what would be experienced in a bulk solution with a NaCl gradient. In that case, however, the chloride is as much retarded as the sodium is boosted, resulting in a diffusivity for the full salt that is between the two individual values. In compacted bentonite, on the other hand, the electromigration flux is mainly significant for sodium (the counter-ions). Therefore the full salt diffuse with a rate essentially set by the chloride mobility.
We can quantify the relative influcence of electromigration for a specific species by taking the ratio of eqs. 15 and 16, and also utilizing the approximation for \(\nabla \psi (x)\) in eq. 10
This expression explicitly shows that the electromigration flux is negligible for chloride (because \(c^\mathrm{int}_\mathrm{Cl}(x) \ll c_\mathrm{IL}\)), while the \(j_\mathrm{E}/j_\mathrm{conc}\)-ratio for sodium is essentially determined by the factor \(\left (D_\mathrm{Cl}/D_\mathrm{Na} – 1 \right )\) (because \(c^\mathrm{int}_\mathrm{Na}(x) \approx c_\mathrm{IL}\)).
For a similar NaCl-system at lower density, the picture is quite similar (here \(c_\mathrm{IL}\)=1.5 M, with the other parameters as previously; \(\Delta \psi_\mathrm{m}\) = 37.8 mV and \(\Delta \psi_\mathrm{diff}\) = -1.1 mV)
Let’s also play with the relative mobility between anion and cation. In the plot below we have decreased the chloride diffusivity to \(D_\mathrm{Cl}=0.133\cdot 10^{-10}\) m2/s, while keeping with the same values as before for the other parameters (for \(c_\mathrm{IL}\) = 3.0 M).
In this case, the diffusivity factor for the electromigration is \((D_-/D_+ -1) = -0.9\). The negative value indicates an electric field directed in the opposite direction as compared to the previous cases (chloride is now the slower ion). The diffusion potential is \(\Delta \psi_\mathrm{diff}\) = +0.6 mV, which still is quite small, given that the chloride is assumed to have ten times lower mobility as compared with sodium. The evaluated membrane potential is \(\Delta \psi_\mathrm{m}\) = 41.3 mV. We note that the flux is constant throughout the domain and that chloride is completely governed by the concentration gradient contribution, while the sodium flux is composed of two oppositely directed much larger contributions of similar magnitude.
If we instead make the sodium diffusivity 10 times smaller than the chloride diffusivity (\(D_\mathrm{Na}=0.203\cdot 10^{-10}\) m2/s, \(D_\mathrm{Cl}=2.033\cdot 10^{-10}\) m2/s), the effect is more dramatic
With \((D_-/D_+ -1)\) = 9.0, the diffusion potential becomes considerably larger than in any of our previously investigated cases: \(\Delta \psi_\mathrm{diff}\) = -5.2 mV (\(\Delta \psi_\mathrm{m}\) = 35.5 mV). This is reasonable, since a significantly smaller mobility of the counter-ions requires a larger electric field to produce similar fluxes. The sodium flux is therefore dominated by electromigration, and we also note a non-negligible contribution from electromigration for chloride. The overall flux varies quite significantly throughout the clay domain; we’re not really in steady-state.
“Uphill” diffusion
With a solid understanding of the principles for diffusion of a 1:1 electrolyte in compacted bentonite, let’s turn our attention to the “uphill” test (Glaus et al., 2013). The conditions for the main electrolyte (NaClO4) and clay in this study are the same as in our previous case: one reservoir is at concentration 0.1 M, and one at 0.5 M, and the clay is pure high-density Na-montmorillonite. For a further discussion of this study, see this previous post. Here we adopt the value \(c_\mathrm{IL}\) = 4.5 M and set \(c^{(1)}\) = 0.1 M and \(c^{(2)}\) = 0.5 M (in order to have a positive tracer flux). In addition to a main electrolyte, the “uphill” test has a sodium tracer (\(^{22}\mathrm{Na}\)) as a third component, with equal concentration in the two reservoirs (\(10^{-11}\) M). Here we choose sodium diffusivity \(D_\mathrm{Na}=3\cdot 10^{-11}\) m2/s, similar to what is evaluated in Glaus et al. (2007) and Birgersson and Karnland (2009). For perchlorate we choose \(D_\mathrm{ClO_4}=4\cdot 10^{-11}\) m2/s, in order to keep the same diffusivity ratio as for bulk (the perchlorate bulk value is \(1.79\cdot 10^{-9}\) m2/s (Heil, 1995)).
Since the only difference between the “uphill” study and the pure 1:1 case is the presence of a tracer, it is no surprise that concentrations, fluxes and potential behave very similarly
The membrane potential is here \(\Delta \psi_\mathrm{m} = -41.0\) mV, which is essentially identical to what we have evaluated for the NaCl system (the minus sign simply reflects that the left reservoir here has the lower concentration). With a smaller mobility difference between anion and cation, the diffusion potential is even more negligible than for NaCl, \(\Delta \psi_\mathrm{diff} = 0.1\) mV. The tracer flux is not resolved in the above plot, but looks like this
An analytical evaluation of the \(j_\mathrm{E}/J_\mathrm{conc}\)-ratio becomes a bit more complicated for the tracer as compared with the main salt (eq. 17). At the two interfaces, it can be shown that11
We see that this ratio is expected to be small as long as the reservoir concentrations are small as compared with \(c_\mathrm{IL}\). This is also confirmed in the above plot; the electromigration contribution is completely negligible.
This result is the ultimate support for the claim I made in the “uphill” blog post: the phenomena is first and foremost an effect of ordinary Donnan equilibrium, just as conventional cation tracer diffusion is explained. Here we have explicitly included the electric potential in the analysis, and not only showed that electromigration is negligible for the tracer component, but qualitatively described how and where possible effects due to ion mobility differences occur in the set-up as a whole.
Tertre et al. (2024) — the publication critisized in the “uphill” blog post — states that the “uphill” study
[…] demonstrated the marked influence of background electrolyte concentration gradient on tracer diffusion, and thus the necessity to understand the couplings between diffusion of several charged species present at contrasting concentrations and experiencing different concentration gradients.
In contrast to Tertre et al. (2024), we have here presented this understanding and — in contrast to the statement — demonstrated that the “uphill” effect does not depend critically on any additional mechanisms or couplings as compared with conventional cation tracer diffusion.
As for the previous cases, we can play around with the parameters to explore more “extreme” conditions in an “uphill” test. Here we have increased the perchlorate diffusivity to \(D_\mathrm{ClO_4}=9\cdot 10^{-11}\) m2/s (i.e. three times the sodium diffusivity), and lowered \(c_\mathrm{IL}\) to \(c_\mathrm{IL} = \) 2.0 M (corresponding roughly to a density of 1.25 g/cm3).
Predictably, the main counter-ion transport is now dominated by electromigration, and we see some influence of electromigration also on the perchlorate and the sodium tracer. Nevertheless, even for this extreme case, the “uphill” tracer flux is mainly “Fickian” and is principally explaind as an effect due to Donnan equilibrium at the sample interfaces. For this case we have \(\Delta \psi_\mathrm{m}\) = -37.4 mV and \(\Delta \psi_\mathrm{diff}\) = 2.6 mV.
CaCl2
Let’s also examine the pure 2:1 system, which corresponds e.g. to CaCl2 solutions in contact with Ca-montmorillonite. As we discussed in a recent blog post, the Donnan equilibrium for this system is quite different as compared with the 1:1 system. This will naturally also impact the membrane potential. Moreover, experiments indicate that calcium diffuses several times slower than chloride in bentonite (Kozaki et al., 2000), which suggests a larger effect on the diffusion potential. But, similar to previous cases, let’s begin by assuming the same diffusivity ratio as for bulk. With \(D_\mathrm{Cl}=2.03\cdot 10^{-10}\) m2/s, \(D_\mathrm{Ca}=0.79\cdot 10^{-10}\) m2/s, \(c_\mathrm{IL} = \) 3.0 M, and having \(c^{(1)}\) = 0.25 M and \(c^{(2)}\) = 0.05 M12 we get the following picture
The membrane potential is here \(\Delta \psi_\mathrm{m} = 18.8\) mV and the diffusion potential \(\Delta \psi_\mathrm{diff} = -1.1\) mV. Thus, even if the relative influence of the diffusion potential is larger han for NaCl, the main contribution to the membrane potential is still due do Donnan equilibrium; the considerably lower membrane potential in this case (about half of the NaCl value with the same amount of chloride in the reservoirs) is primarily a consequence of Donnan equilibrium: the Donnan factors have in this case a square-root dependence on external concentration. However, as a consequence of calcium mobility being considerably lower than sodium mobility (\(D_-/D_+ – 1\) = 1.57), the magnitude of the diffusion potential is about three times larger than for the NaCl case. The resulting flux is also seen to be not completely constant throughout the clay domain. Nevertheless, the same qualitative picture of the transport mechanism as for NaCl is valid here: chloride transport is dominated by its “Fickian” contribution, diffusing with the rate set by the individual mobility, while the less mobile calcium is boosted by an electromigration contribution, which here is actually larger than its concentration gradient contribution. The salt as a whole diffuses with the rate essentially set by the chloride diffusivity.
Let’s also explore an “extreme” case. Below we have set the Ca mobility to be a factor 10 lower than Cl (\(D_\mathrm{Cl}=2.03\cdot 10^{-10}\) m2/s, \(D_\mathrm{Ca}=0.203\cdot 10^{-10}\) m2/s) and lowered \(c_\mathrm{IL}\) to \(c_\mathrm{IL} = \) 1.5 M.
Here the membrane potential is only \(\psi_\mathrm{m} = 6.7\) mV due to a large contribution from the diffusion potential (\(\Delta \psi_\mathrm{diff} = -12.0\) mV), The calcium flux is seen to be strongly dominated by electromigration, and chloride transport is also strongly affected. We are far from steady-state.
Mixing sodium and calcium
As a final case we consider systems containing both a mono- and a di-valent type of cation. Since cation concentrations are enhanced within the clay, a significant diffusion potential may develop, even for relatively small variations of the external solutions. For instance, with a pure 0.1 M NaCl solution on one side (2), and a mixture of 0.003 M CaCl2 and 0.094 M NaCl on the other (1), we get the following result
Here we have assumed \(c_\mathrm{IL} = \) 3.0 M, \(D_\mathrm{Cl}=2.03\cdot 10^{-10}\) m2/s, \(D_\mathrm{Ca}=0.79\cdot 10^{-10}\) m2/s, and \(D_\mathrm{Na}=1.33\cdot 10^{-10}\) m2/s.
Note that the Donnan equilibrium at the left interface acts as to make the clay contain 50% sodium and 50% calcium (charge wise) even though the calcium content in the reservoir is only 6%! A quite minor “disturbance” in the external solution consequently induce huge transport processes.13 This transport is essentially independent of the presence of an anion, and is governed by mutual diffusion of calcium and sodium. The mobility difference for these two ions thus results in a large diffusion potential: \(\Delta \psi_\mathrm{diff}\) = -5.0 mV. The membrane potential is quite substantial: \(\Delta \psi_\mathrm{m}\) = 11.4 mV. The calcium transport is dominated by the concentration gradient flux, while the oppositely directed sodium flux is more profoundly retarded by the electric field (although it is still dominated by the concentration gradient). We conclude that the full Na-Ca transport process occurs approximately at the rate set by the individual mobility for calcium. This process is essentially charge neutral, i.e. as much Ca charge is transported to the right as Na charge is transported to the left.
It may also be worth noticing that although the chloride concentration is the same in the two external solutions, an internal gradient — and a corresponding chloride flux — is induced
This chloride flux, which is directed to the right and seen to be quite influenced (retarded) by electromigration, is more than two orders of magnitude smaller than the Ca-Na flux. This result implies that also anions may experience seeming “uphill” diffusion (though I’m not sure how easy it would be to detect experimentally).
A lesson here is that calcium concentrations often must be very small in order to be treated as a tracer when added to a sodium system. For example, Tinnacher et al. (2016) incorrectly treats calcium as a tracer when adding 0.001 M CaBr2 to an otherwise pure 0.1 M NaCl-montmorillonite system at 0.8 g/cm3.14 At that density, we may approximate \(c_\mathrm{IL} = 1.0\) M, which gives the following situation (\(D_\mathrm{Cl} = 2.03 \cdot 10^{-10}\) m2/s, \(D_\mathrm{Br}=2.01\cdot 10^{-10}\) m2/s, \(D_\mathrm{Ca}=0.79\cdot 10^{-10}\) m2/s, and \(D_\mathrm{Na}=1.33\cdot 10^{-10}\) m2/s; CaBr2 in reservoir 1)
The amount of calcium in the clay at the left interface is in this case predicted to be about 15% — which certainly cannot be regarded a trace level. Consequently, the main mode of transport in this test is oppositely directed sodium and calcium fluxes that essentially does not involve the anions. In addition, we predict a non-zero membrane potential of \(\Delta \psi_\mathrm{m} = 2.5\) mV, with \(\Delta \psi_\mathrm{diff} = -1.5\) mV.
The bromide, in contrast, can be treated as tracer, and its flux look like this
This flux is about two orders of magnitude smaller than the dominating Ca-Na flux,15 and is seen to be essentially unaffected by the electric field (i.e. mainly “Fickian”).
Additional comments
Here we have investigated transport processes that occur in the presence of chemical gradients between two external reservoirs sandwiching a compacted bentonite component. For this case, compacted bentonite appears to function similar to a conventional charged ion exchange membrane.2 However, compacted bentonite used e.g. for waste storage is quite different from ordinary ion exchange membranes, in that we are more interested in what is going on inside it, rather than directly utilizing its semi-permeable properties. The results discussed in this blog post are useful when interpreting tests that involve bentonite sandwiched between external solutions. For a description of what is going on inside the bentonite component, such results and tests may be very useful, but do not provide a full picture.
As with many topics discussed on the blog, I find the lack of relevant experimental results quite extraordinary. I mean that many labs should routinely measure membrane potentials as part of exploring bentonite systems. Instead, as far as I understand, the study by Yaroschchuck et al. (2007) is the only one published on actual compacted bentonite.16 Moreover, this study appears to be completely forgotten!8
Yaroschchuck et al. (2007) use extremely high density, and it would be interesting with data also at lower densities (1.6 — 1.3 g/cm3, say); the present theory predicts only minor changes in membrane potentials. A “simple” further test of the present description would be to measure the membrane potential in e.g. a pure CaCl2-montmorillonite system. We end this post by presenting such potentials as predicted from the present theory (the calculation uses \(D_\mathrm{Cl} = 2\cdot 10^{-10}\) m2/s and \(D_\mathrm{Ca} = 0.5\cdot 10^{-10}\) m2/s).
Update (260922): The full Nernst-Planck framework is treated within the homogeneous mixture model here.
Footnotes
[1] The
focus here is on what I call
simple ions, i.e. ions that only interact with the bentonite by beeing
part of a diffuse layer. In bentonite, more complex processes are
active for certain species that interact with e.g. montmorillonite
edges. Here
is presented an extension of the homogeneous mixture model for
“truly” sorbing species.
[2]
What is presented in this blog post is, as far as I understand, the
“Teorell-Meyer-Sievers”
model for the membrane potential, applied to compacted
bentonite. This model, which was originally developed in the 1930s,
isusedroutinely within
the ion-exchange membrane scientific discipline. I’m currently reading
up on this literature, and is here using my “usual” terminology
(for bentonite). I have not yet come across sources with specific
focus on bentonite/montmorillonite, and I’m not sure how well
established these are as a membrane materials within this
discipline. In a well-cited review by
Xu (2005),
bentonite is mentioned once — misspelled! Perhaps this is
indicative of a missing link between the ion exchange membrane and
compacted bentonite research fields.
[3] Although different water
chemistries will induce different
swelling pressure repsonses, and thus
couple to mechanical processes in the bentonite, we here ignore
pressure altogether (but we certainly will have reason to return to
this).
[4] Note that
Donnan potentials generally are negative, while
\(\Delta \psi_\mathrm{Donnan}^{(1)}\) and
\(\Delta \psi_\mathrm{Donnan}^{(2)}\) are negative or positive,
depending on whether the contribution decreases or increases the
potential as we move to the right.
[5] Including
activity coefficients, eq. 6 becomes
and the interlayer activity coefficients (\( \gamma^\mathrm{int}\)) will therefore cancel (to the extent that the this quantity can be considered independent of external solution concentration). The contribution from Donnan equilibrium to the membrane potential thus become
[7] The value of \(c_\mathrm{IL}\) (eq. 5) depends on the cation exchange capacity of the material: montmorillonite “from Milos”. Differentsources report this value in the range 0.80 — 0.85 eq./kg.
[8] The obscurity of Yaroshchuck et al. (2007) amazes me. This paper is part of a “trilogy” published in 2007, by the same authors (to a large extent). The other two studies are featured massively on the blog: Glaus et al. (2007) demonstrates that interlayer diffusion dominates mass transfer in compacted bentonite (see here and here), and Van Loon et al. (2007) is the only study that passed our assessment of published chloride equilibrium concentrations in compacted bentonite (see here, here, and here). Glaus et al. (2007) has at the moment 178 citations on Google Scholar, and Van Loon et al. (2007) has 333 citations. Yaroshchuck et al. (2007), in contrast, has 7 citations… Perhaps even more weirdly, Yaroshchuck et al. (2007) is not cited in Van Loon et al. (2007), although the former study presents the framework for Donnan equilibrium between compacted bentonite and a 1:1 electrolyte, and relates it to the findings of Glaus et al. (2007). It should thus had been an “easy win” for Van Loon et al. (2007) to provide a proper explanation for anion exclusion in bentonite, and to make the correct connection between anion and cation tracer through-diffusion. Instead, and for reasons I can’t get my head around, van Loon et al. (2007) get lost in ideas on “anion-accessible porosity”.
[9] Generally, the flux may also have an advective component, which we don’t consider here.
[10] The absolute values of the diffusivities are chosen rather arbitrarily; in this example we have adopted values ten times smaller than the corresponding values in bulk. The absolute value of the corresponding flux is therefore also arbitrary. Here, however, we are mainly interested in how constant the flux is throughout the clay, and in the relative contributions from concentrations and electric fields, rather than the absolute values. In some cases in this section we have adopted empirical values for diffusivities in order to compare also the absolute value of the flux.
[11] The electromigration and concentration gradient fluxes for the tracer in the “uphill” test can be written (see eqs. 15 and 16)
where we have explicitly written the gradients in terms of the internal interface concentrations. Using the relation between Donnan factors and concentrations, this concentration difference ratio can in turn be rewritten
where we have written \(c_\mathrm{tr}\) for the tracer concentration in the reservoirs (it’s equal in the two solutions). The flux ratio can thus be written
[15] The actual measured bromide and calcium fluxes in Tinnacher et al. (2016) differ only by about one order of magnitude. This may be in part due to filter limitations, and in part be an indication that a completely homogeneous treatment begins to break down at these densities.
[16] Some results on bentonite samples of somewhat lower density are presented by Heister (2005).
So far in this review we have showed that the model for bentonite proposed in TS15 has both conceptual and mathematical flaws. In the previous part we showed that the “diffuse layer” flux is not derived adequately, although the resulting expression nevertheless can make some sense, if the involved electric potentials are completely reinterpreted. We also noted that the suggested “contributions” to the flux — related to “concentration gradients” (Fickian contribution) and “diffusion potential” (electric field contribution) — make no sense. These “contributions” can, however, be corrected, with the correction term (\(j^\star \)) involving the gradient of \(\Psi^\star\), the electric potential difference between bulk and “diffuse layer”
Here \(c_\mathrm{bulk}\) is the bulk water concentration of the considered species (generally a function of the model coordinate \(x\)), \(D_\mathrm{DL}\) is the corresponding diffusion coefficient in the “diffuse layer” domain, \(z\) the charge number, \(F\) the Faraday constant, and \(RT\) the usual thermal energy factor. \(A\) is what TS15 call the “DL enhancement factor”, and is given by (when correctly derived)
\begin{equation}
A = e^{-\frac{zF}{RT}\Psi^\star}
\end{equation}
The electric potentials in the bulk and “diffuse layer” domain are
denoted \(\Psi_\mathrm{bulk}\) and \(\Psi_\mathrm{DL}\), respectively,
giving the relation
With these corrections and reinterpretations it may appear as if the
transport model presented in TS15 actually has some merit. Here,
however, I would like to point out what I think is a deeper problem,
related to the assumption of requiring the various “porosity
domains” to be locally in equilibrium. As in the previous part, we
focus on the equilibrium between the bulk and “diffuse layer”
domains.
In the previous part we did not pay detailed attention to the electric potential difference \(\Psi^\star\). TS15 suggest that \(\Psi^\star\) is to be calculated using the Donnan equilibrium framework. This makes some sense, from the perspective that the model assumes bulk water and “diffuse layer” to be in equilibrium locally, and in the provided examples \(\Psi^\star\) is calculated using the Donnan formula for a 1:1 electrolyte,2
\begin{equation}
e^\frac{F\Psi^\star}{RT} = – \frac{q}{2c_\mathrm{bulk}} +
\sqrt{\frac{q^2}{4c_\mathrm{bulk}^2} + 1}
\end{equation}
where \(q\) is a measure of the structural charge in the “diffuse
layer”, in the examples set to \(q\) = 0.33 M.
But the requirement of Donnan equilibrium constrains the overall model
quite heavily. For example, if we — as in the provided examples —
impose concentration profiles in the bulk water, these determine the
electric potential profile in this domain, via the Nernst-Planck
framework. At the same time, the bulk water concentrations, together
with a specified value of \(q\), also completely determine \(\Psi^\star\)
(as a function of \(x\)), as well as all “diffuse layer” ion
concentrations, via the
Donnan equilibrium framework. These “diffuse layer” concentrations
will, in turn, determine the electric potential (up to a constant) in
this domain, via the Nernst-Planck framework.
But note that the electric potentials in the bulk and “diffuse layer” domains determined in this way, cannot in general also fulfill the requirement for Donnan equilibrium, i.e. \(\Psi^\star \neq \Psi_\mathrm{DL} – \Psi_\mathrm{bulk}\) (cmp. eq. 1). We consequently end up with a contraction, where we have used eq. 1 to determine the “diffuse layer” concentrations, while eq. 1 no longer applies after invoking the Nernst-Planck condition of requiring zero electric current!
This incompatibility is illustrated in the figure above.3 Note that there is nothing special with that the contradiction is here expressed in terms of \(\Psi_\mathrm{bulk}\) and \(\Psi_\mathrm{DL}\) not fulfilling eq. 1. Rather, all of the four relations illustrated in the above figure cannot in general be fulfilled simultaneously. In other words, as far as I see, for an imposed set of concentration profiles in one of the domains, the TS15 model cannot in general simultaneously fulfill these conditions
Zero electric current in the bulk water domain
Zero electric current in the “diffuse layer” domain
Donnan equilibrium between bulk and “diffuse layer”
This flaw is well illustrated in examples 2 and 3 in TS15 (the
electric potential is the same for these cases). The electric
potential in the bulk water can be calculated from the imposed
concentration gradients of the main electrolyte, and is plotted in the
figure below (blue line)
In the figure is also plotted the electric potential in the “diffuse
layer”, as calculated from the Nernst-Planck framework and the
concentration profiles in this domain (orange line; also shown
here). As we noted previously, the reason for the much smaller
variation of \(\Psi_\mathrm{DL}(x)\) as compared with
\(\Psi_\mathrm{bulk}(x)\) is the ever-present counter-ions in the
“diffuse layer” domain. Notice further that TS15, in contrast, are
under the impression that the electrostatic potential in the “diffuse
layer” equals the Donnan potential (red line), while such a
profound potential variation is not supposed to affect the
electromigration, for unclear reasons.
For \(\Psi_\mathrm{DL}\) we have here chosen the reference point \(\Psi_\mathrm{DL}(0) = \Psi^\star(0)\), i.e. we dictate that the bulk and “diffuse layer” potentials should differ by the Donnan potential when \(x=0\). But this is the only point where this condition is fulfilled: The difference between the electric potentials as calculated in this way (green line) does not at all resemble the Donnan potential!
At the moment, I don’t have the energy to sort out if there is any way out of this paradox, but my guess is that the problem is related to the very different treatments of transport in the \(x\)- and \(y\)-directions in the TS15 model. Remember that the assumption of equilibrium between all domains for a given \(x\)-value is equivalent to assuming infinite mobility in the \(y\)-direction of all species. To me, it appears as the TS15 model attempts to squeeze an intrinsically two-dimensional problem into a one-dimensional form. Note that this problem is not unique for the TS15 model, but arise in any multi-porous, multi-component description which assumes local equilibrium between domains (e.g. Appelo and Wersin (2007)).
Appendix: Comments on Figure 8
Disclaimer: This part functions as an appendix to this already appendix-like part of the review. The reader has been warned.
When considering electric potentials in the TS15 model I have
developed a need to further comment on “Figure 8”. I
alluded to this figure in the previous part of the review when
discussing the term “Pseudo 2-D Cartesian system” used by TS15 (a
term I don’t understand). “Figure 8” looks like this
The caption reads
Pseudo-2-D Cartesian system with diffusion along the x-axis and electrostatic potential developing along the y-axis due to the negative charge at clay mineral surfaces.
The only reference to this figure in the article text is at the
beginning of the section presenting the transport model (Nernst-Planck
equation in several “porosity domains”)
In the following, we will consider a pseudo 2-D Cartesian system in
which diffusion takes place along the x axis only (Fig. 8).
The more I think about how this figure is included in the article, the more peculiar I find it. The figure clearly shows a quantitative result, as it displays specific values of a two-dimensional electric potential function outside “negative charge at clay mineral surface”. Yet, any real information about this calculation is nowhere to be found, which I see as a major problem (especially as the text is supposed to be a “fully developed text which can be used for self-study, research, or as a text-book for graduate-level courses”). Here we will first discuss information that is not provided, before continuing with speculating about how this figure may have been produced.
Stuff we are not told anything about
The ionic strength
Note that the “ionic strength gradient in bulk water” is only indicated in the figure, but not at all mentioned in the caption or in the text snippet that refers to this figure. Apparently, the physical situation depicted involves “bulk water” where the ionic strength, i.e. the concentration, falls of with the coordinate \(x\). But what is the actual value of this gradient? What are the boundary concentrations? And how has this ionic strength been used when calculating the electrostatic potential? We are not even told what type of electrolyte is considered! Is it 1:1?
Pseudo-2D and length scales
The only twoplaces in TS15 where “Figure 8” is referenced are also the only places where the concept of a “pseudo-2D Cartesian system” is brought up. But what is meant by this term?! To me, it is more than a little strange to base an entire model presentation on a concept that is not really explained.
Taken at face value, the presented figure does not seem to show any “pseudo-“, but a “real” 2D coordinate system. Guided by the variation of the potential in the \(y\)-direction and by the clue that we are outside a negatively charged mineral surface, it’s quite safe to say that we — in the \(y\)-direction — are looking at an actual diffuse layer, as calculated e.g. in the Gouy-Chapman model. The \(y\)-dimension is thus reasonably on the nanometer scale. An ionic strength gradient, however, only makes sense as being on the macroscopic scale. The scale of the \(x\)-dimension is thus reasonably comparable to e.g. that of a laboratory sample, i.e. centimeters or even meters. Although “Figure 8” consequently is oddly scaled (the \(x\)-dimension is at least a million times larger than the \(y\)-dimension), I don’t see any reason to refer to it as “pseudo-2D”. It should of course be completely mandatory to state the length scales when presenting such a figure in a peer-reviewed scientific journal.
Further, we note that the figure seems to depict two copies facing each other of the same potential function, with one copy being flipped vertically (this explains the two oppositely pointing \(y\)-axes). Is this the reason for calling the coordinate system “Pseudo-2D”? But this manipulation (two copies facing each other) seems only to be for illustrative purposes, and has no impact on what actually seems to have been calculated.4
Surface charge
The potential is supposed to be “developing […] due to the negative charge at the clay mineral surfaces”. But then a surface charge density must have been specified when calculating the potential. Needless to say, this value should have been stated.
Stuff that is incorrect or odd
“Developing” potential
The figure caption “explains” that an electrostatic potential “develop[s] along the \(y\)-axis”. But what is significant is that an electric field is present near the surface. And, as we have brought up earlier, an electric field is equivalent to a potential variation. To put focus on that a potential “develops”, rather than that the potential varies, mostly misses the point. Also, why is the word “develop” used here? It suggests some sort of ongoing (unexplained) process.
“Developing” potential along the y-axis
A clear illustration that something is missed when speaking of potentials rather than fields is that TS15 implies that this “development” occurs exclusively in the \(y\)-direction. Note that an electric field is directed normal to the lines of constant electric potential. It is thus completely clear from the figure itself that the electric field is not in general directed solely in the \(y\)-direction!
This type of manifestation of an electric field in the \(x\)-direction relates to the complications discussed earlier of having a Donnan potential that varies with \(x\).
The potential has not resulted from solving the Nernst-Planck equation
Even though the purpose of the section is a treatment of the Nernst-Planck framework for transport of ionic charges, “Figure 8” does not present the result of a Nernst-Planck calculation. A main objective of such a treatment is to calculate the gradient of the electric potential (in the \(x\)-direction), i.e. an electric field. In contrast, the figure clearly shows that the potential is essentially zero, some distance away from the surface.
My guess is that “Figure 8” has been produced by calculating a set of potential profiles (in the \(y\)-direction) from the Gouy-Chapaman model for a given set of values of the ionic strength. These profiles have then simply been “stacked” in the \(x\)-direction. Below are some attempts to recreate “Figure 8” using this approach.
Since no parameters are given in TS15, we have to make several assumptions. For the figure below is assumed a linear profile of a 1:1 electrolyte that falls from 1000 mM at \(x=0\) to 100 mM at \(x=12\). We furthermore assume a surface charge density of 0.04 C/m2.
The magnitude and variation of this potential is comparable to that in “Figure 8” (the unit for the electric potential is here mV). We may note, however, that the linear ionic strength profile results in lines of constant electric potential that more and more “bends away” from the surface. This is because the Debye length in a 1:1 electrolyte depends on ionic strength as \(1/\sqrt{I}\). In contrast, the lines of constant potential in “Figure 8” are seen to “bend back”, suggesting a leveling off of the ionic strength, like this
If the present speculations are correct, why on earth has such a concentration profile been chosen? More broadly, why is this type of figure at all presented? If the authors simply want to show the quantities being calculated, why not provide a schematic illustration rather than a quantitative calculation? And if they want to present an actual calculation — which for unclear reasons does not involve the Nernst-Planck framework — they must of course provide a reader with enough information to make it understandable.
Update (260824): Part VI of this review is found here.
Footnotes
[1] As I have commented in the earlier parts: TS15 are
fond of using the general terms “clays” and “clay minerals”, while
it is clear that the publication mainly focus on systems with
substantial ion exchange capacity and swelling properties. Here we
will continue to use the term “bentonite” for these systems, and
ignore the frequent references in TS15 to more general terms.
[2] TS15 are under the impression that \(\Psi_\mathrm{bulk}= 0\), and they believe that they calculate \(\Psi_\mathrm{DL}\) rather than \(\Psi^\star\). They furthermore emphasize that a more accurate calculation involves integrating the Poisson-Boltzmann equation (and claim falsely that the Donnan equilibrium “model” is based on an approximation of the Poisson-Boltzmann equation). But under all circumstances, the TS15 model requires specifying an arbitrary size of the “diffuse layer”; in the examples is used a width of 3 nm, which approximately corresponds to 3, 1 and 0.3 Debye lengths, respectively, for 1:1 background concentrations 0.1 M, 0.01 M, and 0.001 M. As we have discussed in the blog post on why multi-porosity models cannot be taken seriously, such a partitioning requires that a mechanism is provided for how equilibrium is maintained (i.e. why the “diffuse layer” does not occupy the full pore volume). TS15 do not supply such a mechanism, and neither does any other author promoting multi-porous models.
[3] In this figure,
\( \left \{ c_{\mathrm{bulk} ,i} \right \} \) denotes the
complete set of imposed concentrations in the bulk water domain. The
corresponding set of species concentrations in the “diffuse layer”
is denoted \(\left \{ c_{\mathrm{DL},i}\right \}\).
[4] Even if this
choice is only “cosmetic”, I actually don’t understand why the
figure is presented like this. Is it supposed to depict an
(insanely long) interlayer? Perhaps with a “bulk water” phase
squeezed in the middle? The same authors have actually presented
such types of figures in later publications. As I discuss
here, such a representation of a “bulk water” phase is
nonsense.
In some of the simulations that we discussed in a previous blog post on molecular dynamics (MD) studies on anion exclusion, chloride never enters the montmorillonite interlayers. From such results, authors have argued for complete anion exclusion from interlayers, and thereby supported ideas of a multi-porous structure of compacted water saturated bentonite. It is, however, glaringly obvious that these simulations are not even close to being converged, and that they should not have been published in the first place. It is also clear that chloride does enter interlayers in properly conducted MD studies, in both tri- and bi-hydrated sodium montmorillonite.
Reasonably, it should only be a matter of time before researchers that support ideas of complete exclusion manage to perform MD simulations that better reflect anion equilibrium in montmorillonite. As such possible future simulations will confirm that anions have access to interlayers,1 I have in the back of my mind wondered about potential consequences. Will earlier publications be retracted? Will the entire “mainstream view” of the structure of compacted bentonite fall into oblivion? (I wish.) From this perspective I find it a bit amusing that no further MD simulation has been published to support complete anion exclusion for the last ten years (as far as I’m aware).
Hsi15 simulated bi-hydrated sodium montmorillonite interlayers in contact with a bulk compartment with two different NaCl concentrations (1.67 M and 0.55 M), and showed that these systems obey the rules for Donnan equilibrium, albeit with a substantial non-electrostatic contribution to the free energy (non-ideal conditions). Hsi22 continue this work by presenting a complementary simulation at a third NaCl concentration (1.0 M), and by performing corresponding simulations for CaCl2, at bulk concentrations 0.14 M, 0.28 M, 0.52 M, and 0.84 M (with all interlayer cations then being calcium, obviously). With chloride equilibrium simulations for several background concentrations for both Na- and Ca-montmorillonite, but for otherwise identical systems, Hsi22 are able to make thorough comparisons with Donnan equilibrium theory.
Chloride equilibrium — just as any other ion equilibrium — is conveniently expressed via the ratio \(\bar{\mathrm{c}} / c^\mathrm{ext}\), where \(\bar{\mathrm{c}}\) is the clay concentration and \(c^\mathrm{ext}\) is the corresponding bulk concentration. In a Donnan equilibrium context this concentration ratio may be identified with the ion equilibrium coefficient2 \begin{equation} \Xi_\mathrm{Cl} \equiv \frac{c^\mathrm{int}_ \mathrm{Cl}} {c^\mathrm{ext}_\mathrm{Cl}} \end{equation} where \(c^\mathrm{int}_\mathrm{Cl}\) is the interlayer concentration of chloride in a homogeneous bentonite domain in equilibrium with an external solution with chloride concentration \(c^\mathrm{ext}_\mathrm{Cl}\).
For a 1:1 system (e.g. NaCl in contact with Na-montmorillonite) a good approximation for \(\Xi_\mathrm{Cl}\) at low external concentration is3 \begin{equation} \Xi^{1:1}_\mathrm{Cl} \approx \Gamma^2 \frac{c^\mathrm{ext}_\mathrm{Cl}}{c_\mathrm{IL}} \tag{1} \end{equation} where \(c_\mathrm{IL}\) is the structural montmorillonite charge expressed as a monovalent interlayer concentration (in the model of Hsi22 and Hsi15, \(c_\mathrm{IL} = 4.23\) M) and \(\Gamma\) is a mean activity coefficient ratio for NaCl (more on that below).
While the ion equilibrium coefficient in eq. 1 depends linearly on the external concentration, the corresponding quantity for a 2:1 system (e.g. CaCl2 in contact with Ca-montmorillonite) depends on the square-root of the external concentration (note that the Cl concentration in a CaCl2 solution is twice that of CaCl2) \begin{equation} \Xi^{2:1}_\mathrm{Cl} \approx \Gamma^{3/2} \sqrt{\frac{c^\mathrm{ext}_\mathrm{Cl}}{c_\mathrm{IL}}} \tag{2} \end{equation} where \(\Gamma\) here is to be understood as a different mean salt activity coefficient ratio (for CaCl2).
The different dependencies on \(c^\mathrm{ext}_\mathrm{Cl}\) for Na- and Ca-systems, expressed in eqs. 1 and 2, are clearly reproduced in the MD results presented in Hsi22 as shown here
The dots show the chloride equilibrium coefficients as calculated in Hsi22 and Hsi15, primarily from evaluated potentials of mean force evaluated using the adaptive biasing force method. The corresponding curves in the above diagram are my attempt at fitting eqs. 1 and 2 to these MD results.
It should be noted that the linear and square-root dependencies of eqs. 1 and 2, respectively, presume that the activity coefficient ratios (\(\Gamma\)) are essentially independent of \(c_\mathrm{Cl}^\mathrm{ext}\). The successful fits of eqs. 1 and 2 thus demonstrate that this is the case for the MD equilibrium coefficients.4 Hsi22 make a deeper analysis and show that the specific values of the activity coefficient ratios correspond to differences in excess chemical potential for the salt of 1.35 kT and 1.25 kT, respectively, for the Na- and Ca-systems. Such values reflect a quite profound non-ideal behavior, which may be related to the details of the simulations (e.g. non-polarizable force fields) rather than corresponding to an actual excess barrier.
The main message in Hsi22 is nevertheless clear: Results from MD
simulations of chloride in Na- and Ca-montmorillonite are consistent
with Donnan equilibrium theory. This means, in particular
\(\Xi_\mathrm{Cl}\) is linear for NaCl and has a square-root dependence for CaCl2
For a given external chloride concentration and density, the amount chloride entering the interlayers is much larger in Ca-montmorillonite as compared to Na-montmorillonite
To be clear, the much larger amount of chloride predicted to be found
in Ca-montmorillonite has nothing to do with any notions of different
“anion-accessible” pore spaces, but is a direct consequence of
Donnan equilibrium. In these simulations, all chloride is located at
the exact same place within the clay, as shown here
This figure shows evaluated chloride density profiles in the direction perpendicular to the mineral layers in MD simulations of Na-montmorillonite (Hsi15) and Ca-montmorillonite (presented in the supporting information to Hsi22). While I have arbitrarily scaled the profiles along the y-axis in the above figure for visualization purposes, emphasis is here on the identical position within each interlayer. Note that the simulated system contains two separate interlayers, indicated by dotted vertical lines.5
One lesson from these results is that researchers who struggle with getting chloride to enter interlayers in their simulations could use CaCl2 rather than NaCl. At e.g. an external chloride concentration of \(\sim\)0.5 M, the amount chloride in the clay is about seven times larger in Ca- as compared with Na-montmorillonite, which substantially reduces the required convergence time for the simulation.
These results also highlight the urgent need for empirical data. As I
pleaded for when
concluding the assessment of chloride equilibrium concentrations in Na-bentonite, labs all over the place should routinely produce and
publish ion equilibrium measurements. It is certainly a failure of the
bentonite research field that no published empirical data exists that
can be used to compare with these theoretical results. Indeed, as far
as I’m aware, no published systematic empirical data exists at all,
for anion equilibrium concentrations in calcium dominated
bentonite.6
Note that the implication of the results discussed here is not simply
some noted interesting difference in chloride equilibrium in different
types of montmorillonite. Rather, as the results indicate that
montmorillonite interlayers play by the rules of ordinary Donnan
equilibrium, they are an additional blow to the entire contemporary
multi-porous model description of compacted water saturated bentonite.
Footnotes
[1] As I often nag about on this blog, it is quite silly to use complete anion exclusion as a starting point when studying compacted bentonite, and then trying to “confirm” such a notion with e.g. MD simulations. There is no rationale for this assumption in the first place; as we have discussed earlier, the idea seems to have originated from misunderstanding the Poisson-Boltzmann equation. Moreover, there is solid empirical evidence for salt entering interlayers, in particular from measured swelling pressure response.
[2] Hsiao and Hedström (2022) call this ratio a partition
coefficient, which complies with the scientific literature on
e.g. polymer membranes. As I discussed
here, I have chosen to stick with some of my own terminology. I
hope this does not cause unnecessary confusion.
[4] That the activity coefficient ratios do not depend strongly on external concentration in this concentration interval is also compatible with the mean salt approach that I have suggested to use for compacted bentonite. For the external solutions, mean salt activities varies quite little in this concentration range, and since the interlayer concentrations only vary with a few percent, it make sense to assume that the interlayer activity coefficients basically remain constant. Hsiao and Hedström (2022) actually note that the undulation pattern in the potential of mean force in the direction of the reaction coordinate is essentially independent of the external solution, and conclude that the interlayer environment is essentially independent of external conditions.
[5] The nearly
identical profiles within each interlayer is also a confirmation
that these simulations are properly converged.
[6] An indication that CaCl2 in Ca-montmorillonite behaves as discussed is found here.
Over a long period on the blog, we have systematically examined studies on chloride equilibrium in sodium dominated bentonite. We have now individually assessed each study that was deemed to have potential to provide relevant information. In this blog post we make some overall conclusions and give an updated picture of what is actually known empirically regarding chloride equilibrium in bentonite.
The assessment included seven studies, which are summarized in the table below. The table also provides links to each individual assessment.
These studies are the only ones, to my knowledge, that meet the
following criteria:
They involve chloride
There are both theoretical and empirical arguments for that different anions may have different equilibrium concentrations (for otherwise similar conditions). In the assessment it has therefore been important to stick to one and the same type of equilibrating anion. Moreover, chloride is certainly the anion that has been studied the most within bentonite research, with iodide as its closest “competitor”.
They involve sodium dominated bentonite
This include commercial products, such as “MX-80”, “Kunigel V1” or “Kunipia F”, or materials that were intentionally prepared for the study (more or less pure Na-montorillonite).
Some studies exist where ion equilibrium is explored in other systems, e.g. claystone or bentonites dominated by divalent counter-ions. But, since we have every reason to belive that the conditions for ion equilbrium are different in such systems, as compared to Na-bentonite, we must be careful not to include them in the analysis. We shouldn’t compare apples and oranges.
They have a specified external sodium solution
Without some knowledge of the composition of the solution in contact with the sample, an evaluated chloride concentration cannot be related to any relevant equilibrium condition. Furthermore, if the water chemistry of the equilibrating solution is too complex (e.g. involving several cations), the equilibrium cannot in a reasonably straghtforward manner be related to chloride concentrations in a sodium dominated system.
They have a systematic variation of either density or external background concentration or both
My main motivation for making these assessments is for using equilibrium data to better understand salt exclusion in bentonite. This can reasonably only be achieved if density and/or background concentration has been systematically varied.
In the following we will refer to each study with the identifying
label listed in the table above.
Comments
Through-diffusion is unneccesary
A majority of the examined studies are
through-diffusion studies (Mu88, Mo03, Vl07, Is08, Gl10). A
through-diffusion test set-up is, in fact, much more complex than
required for only studying equilibrium quantities: it involves
monitoring the chemical evolution of the external solutions (often
using radiochemical methods), and the final state (steady-state)
concentration profile is often extracted, by meticulously sectioning
and analyzing the sample (studies where final state profiles were
extracted are indicated by a “p” in the above table).
Additionally, extracting relevant information from flux data requires fitting a two-parameter model. In all assessed diffusion studies, one parameter relates to mobility (either an “effective” or an “apparent” diffusion coefficient) and one to ion equilibrium (“effective porosity”, “anion-accessible porosity”, or a “capacity factor”).1 Consequently, through-diffusion tests, despite their complexity, only provide indirect estimates of equilibrium concentrations, and the accuracy of the estimated parameters naturally depends on details of the fitting procedure and the sampled data. In this regard, most of the studies we have examined report inferior fitting procedures and flux data, where the transient stage of the process has not been adequately sampled (the only exception being Gl10).2 Estimated “effective porosities” are therefore not very reliable. This imprecision can sometimes be mitigated by also using information on the final state concentration profile. But this part of the analysis then essentially corresponds to making a quite complicated equilibrium test. Two of the five diffusion studies — Mu88 and Mo03 — were discarded because evaluated parameters (and the underlying data) are too uncertain.
From an ion equilibrium perspective, through-diffusion tests are
consequently not very “economical”.
The obvious alternative are straightforward equilibrium
tests, where samples simply are equilibrated with specified external
solutions. This can in principle be done without monitoring, and only
requires the patience to wait long enough. The lack of any requirement
to monitor these types of tests also makes them suitable, I imagine,
for involving many samples without significantly increasing the
experimental workload.
Most equilibrium tests have not been adequately performed
Although they are conceptually much simpler, only two of the assessed
studies are pure equilibrium tests (Mu04 and Mu07).
A third (Vl07) performed explicit equilibrium measurements
as part of a diffusion study.
Essentially all studies in the assessment that have recorded concentration profiles show interface excess, i.e. an increased amount of ions near the edges as compared with the interior of the samples. As this effect seems to be universal,3 it must be accounted for when making equilibrium tests, or evaluated concentrations will be overestimated. Doing this should be quite straightforward, by, for example, quickly sectioning off the first few millimeters on both sides of the samples during dismantling. Unfortunately, this has not been done in the assessed equilibrium studies,4 which makes them unsuitable. Vl07, on the other hand, recorded full profiles, and the excess effect was accounted for.
Relevant parameter ranges
After discarding two diffusion studies and two equilibrium studies,
only three studies remain for which the evaluated equilibrium
concentrations are deemed sufficiently accurate: Vl07, Is08 and Gl10.
But we should also consider the relevance of the chosen density and background concentration ranges — something that has not been discussed to any greater extent in the individual assessments. My main motivation for performing this assessment is for using equilibrium concentration data for testing models for salt exclusion in compacted bentonite. A full understanding of ion equilibrium in such systems is crucial for e.g. a relevant chemical description of bentonite buffers in radioactive waste repositories. Therefore, a preferred effective montmorillonite density range is approximately 1.2 — 1.7 g/cm3, say.
With also this criteria in mind, we may therefore rule out two of the three remaining studies; Is08 treats low density systems (\(<\) 1.0 g/cm3), and Gl10 only considers an extremely high high density (1.9 g/cm3).5 This leaves us with a single study that passes both the test of providing accurate data on chloride equilibrium concentrations and being measured in relevant parameter ranges: Vl07. This study covers the approximate density range 1.15 — 1.75 g/cm3, and concentration range 0.01 — 1.0 M.
A single relevant study
On the one hand, it is great news that we have verified some data as
actually useful for evaluating salt exclusion in compacted
bentonite. On the other hand, it is very unfortunate that there only
is one single study!
Moreover, although the results of Vl07 most definitely are useful, they are not optimal. A more “pragmatic” problem with this study is that it reports whole sets of “Cl-accessible porosities”1 for each sample tested, together with an average value. But these different values simply reflect the uncertainty of the parameter for individual samples. If the study had no issues (experimental or modeling related), these values should all be the same, as they are evaluated from one and the same sample. In our assessment we identified that the major part of this uncertainty stems from evaluations from diffusion modeling, while estimations made from equilibrium considerations are more robust (total out-diffusion and stable chloride content). It is thus these estimations in Vl07 that are deemed useful, while the diffusion estimations should be discarded. Note that, since “Cl-accessible porosities” estimated from flux data are sub-optimal, so are the reported average values.
Unfortunately,
severalstudies have
used or
reported
the Vl07 data (as well as other data we have assessed) without
sufficient rigor when evaluating salt exclusion in compacted
bentonite. As a relatively recent example of this,
Gimmi and Alt-Epping (2018) compare two models for chloride exclusion with empirical data
in a figure that looks very similar to this6
In addition to the VL07 data, this plot also compare with data from Mu886 — a study that we have discarded. Taking the above plot at face value it is hard not to wonder what use the experimental data really has — the spread at certain places is almost an order of magnitude (indicated in the figure). You can basically fit any favorite model to this data (or rather, you can fit no model to this data). Gimmi and Alt-Epping (2018) anyway compare the data with two Donnan equilibrium models. One (“full Donnan”) is essentially equivalent to the homogeneous mixture model (all pore space is treated equally), while the other includes several specific additional model components (“free” porosity, exchange “sites”). Gimmi and Alt-Epping (2018) use this plot to argue for that these particular additional components become significant for bentonite at the lower density. But if we “clean up” the plot and only use data points that has passed the present assessment, the picture is instead this
With this version of the data we can at least convince ourselves that
it obeys the rules for Donnan equilibrium. But I mean that it is hard
to draw any more detailed conclusions than that. In particular, it is
a hard stretch to believe that the suggested more complex model has
any particular significance.7
The Vl07 data also has the more fundamental problem that the detailed ionic composition of the system is not fully controlled. This is actually the case for all assessed studies that use “natural” bentonite rather than specifically prepared homoionic clay, and relates to the presence of uncontrolled amounts of divalent cations.
Problems with ignoring the detailed equilibrium conditions
When “natural” bentonites — which generally contain more than one
type of cation — are contacted with a pure sodium solution, it is
inevitable that the material and the solution begin exchanging
cations. Furthermore, since these materials contain accessory
minerals, dissolution/precipitation processes are most probably also
initiated. Thus, at the time when the equilibrium concentration is
recorded, the exact chemical conditions are typically not known. In
particular, it is not clear exactly what e.g. the Na/Ca ratio is in
the clay. To make issues worse, the extent of this effect depends
significantly on the concentration of the external solution, where we
expect a purer sodium clay for higher external concentrations. Since
the external concentration is often varied by orders of magnitude in
these studies, this implies that quanities evaluated at different
concentrations most likely correspond to slightly different systems
(e.g. clay samples with different Na/Ca ratios). Thus, even if we have
taken measures when selecting studies to not compare apples and
oranges, this problem partly remains.
Relevant data for chloride equilibrium concentrations
Below is plotted the chloride equilibrium data that has been found
robust and relevant in the assessment (i.e. part of the data reported
in Vl07)
These values have been evaluated from the “Cl-accessible porosities” reported in table 6 in Vl07.8 The exact values of equilibrium concentration ratios and effective montmorillonite densities depend on adopted values for grain density and montmorillonite content. Here we have adopted \(\rho_s\) = 2800 kg/m3 and 80% montmorillonite. Note that equilibrium concentrations and densities are burdened with additional uncertainties that are not indicated in the above diagram. Note also that although most conditions in the above plot have two data points, these correspond to a single sample. For more details we refer to the individual assessment.
Comparing the above plot with
the one presented in the initial blog post on the assessment —
which included all available data — we note a considerably
less chaotic picture. At least, the robust Vl07 data gives evidence
for the two main features that we discussed in the initial blog post:
Chloride exclusion increases with increasing density at constant background concentration
Chloride exclusion decreases with increasing background concentration at constant density
It must be emphasized that the Vl07 data most probably has a
systematic “error”, in the sense that the data for lower background
concentrations (0.01 — 0.1 M) most probably is influenced by a
significant amount of divalent exchangable cations in the clay (Ca and
Mg). In contrast, for higher background concentrations (0.4 M, 1.0 M),
the clay is most probably in a purer sodium state.
A hundred labs should each make a hundred equilibrium tests!
After finishing this assessment the loudest question in my head is: why are not a hundred labs already on their way to each make a hundred equilibrium tests? Not only has the bentonite research sector failed when we must rely on a single soon 20-year-old study to have some idea of chloride equilibrium in sodium dominated bentonite. For other anions we essentially have no systematic data! As mentioned above, a general understanding of ion equilibrium is required in order to perform relevant chemical modeling of e.g. bentonite buffers in radioactive waste repositories.
[1] Here we do not discuss the
reasonability of these models and model parameters. I am, however,
arguing heavily in many
otherplaces on the blog that none of them are conceptually
sound. Here I have described how experimentally accessible equilibrium
concentrations can be extracted from “anion-accessible porosity”
parameters.
[2] This bad test design
isstillverycommon.
Through-diffusion tests should reasonably be designed so that the
outflux curve can be adequately sampled. As this curve behaves
drastically differently in the transient and in the steady-state
stages, the sampling frequency should reasonably be adapted.
As an example, if a lab has the capacity to make measurements at most every second day (as is done in e.g. Vl07), I suggest starting diffusion tests on a Friday and design them so that essentially no tracers reaches the target reservoir during the weekend. This can be achieved by aiming for a breakthrough time of about 20 days. The breakthrough time is related to diffusivity (\(D\)) and sample length (\(L\)) as \begin{equation*} t_\mathrm{bt} = \frac{L^2}{6D} \end{equation*} Consequently, to keep \(t_\mathrm{bt}\) relatively constant, sample lengths should be adjusted depending on the expected value of the diffusivity. For a breakthrough time of 20 days, \(D = 10^{-10}\) m2/s corresponds to \(L=32\) mm, and \(D = 10^{-11}\) m2/s to \(L=10\) mm.
With a breakthrough time of about 20 days, and tests started on
Fridays, I suggest the following measurement protocol
3 times a week the first 3 weeks (Monday, Wednesday, Friday)
2 times a week the following 3 weeks (Monday, Friday)
1 time a week the following 5 weeks (Friday)
This would give sampling at 20 occasions over about 80 days that
ideally corresponds to four times the breakthrough time, like this
However, I further argue for that through-diffusion tests generally
should be avoided. Diffusivities are more conveniently (and quickly)
measured in closed-cell tests. Likewise, for equilibrium properties
it is obviously better to perform equilibrium
tests. Through-diffusion tests, in my opinion, are only motivated
under
particular circumstances, e.g. for making several non-destructive
measurements in the same sample under various conditions.
[3] I am fully convinced that this is an effect due to swelling during sample dismantling. Molera et al. (2003) and Glaus et al. (2011) have presented other interpretations, which we have briefly discussed in the assessments. I intend to write a future separate blog post on this topic.
[4] Sample
information in Mu07 is sparse and it is not clear how dismantling
has been performed, but nothing suggests that interface excess has
neither been identified nor handled. In the individual assessment of
this study I came to the conclusion that this data after all can be
useful for evaluating models for salt exclusion. Here I anyway
discard the results, mainly due to the above mentioned lack of
information. This data should be kept in mind, however.
[5] Both Is08 and Gl10 provide interesting information,
which should not be completely forgotten. In particular, Is08 report
results for extremely high background concentrations (5.0 M). Gl10,
on the other hand, show a dependency on background concentration of
the diffusivity not seen in other tests. I was not able to rule out
this effect as an artifact and therefore encourage the bentonite
research community to help clarify what is occurring in these
specific systems.
[6] The reference for
the points labeled “M89” in
Gimmi and Alt-Epping (2018) is Muurinen et al. (1988), i.e. Mu88. I have not changed the label,
however, because the plot contains more data than what is reported
in Mu88. I have not been able to identify the source for this
additional data. We may also note that the Vl07 data reported here
appears to be quite randomly chosen; for some systems are chosen
data evaluated from diffusion, for others, data evaluated from
equilibrium measurements.
[7] On the contrary, there are many additional arguments for that sodium bentonite at 1.3 g/cm3 does not contain significant amounts of “free” porosity. Moreover, in my head, the procedure of treating ion exchange with both a Donnan equilibrium model and a surface site sorption model can only lead to overparameterization problems. It is also unreasonable in this context to add conceptually completely different features before the “full Donnan” model is treated in full, e.g. by including activity corrections.
[8] One entry in that table, for stable chloride at 1.9 g/cm3 and background concentration 0.01 M, has been discarded. The table also appears to contain a couple of typos, which have been corrected.
“Constitutive equations for diffusion in bulk, diffuse
layer, and interlayer water”
This section presents a mathematical formulation of ion diffusion in
bentonite,1
based on the material descriptions in the earlier sections. As we have
previously noted, these descriptions are fundamentally flawed in
several respects. In particular, compacted bentonite is presented as
consisting of
stacks (called “particles”), where it is supposed to make sense to
differ between external and internal interface water. TS15 also mean
that compacted bentonite (sometimes?) is supposed to contain a bulk
water phase.
As I have commented on in earlier parts, the only reason I can see to provide this nonsensical material description is as an attempt to to motivate a macroscopic, multi-porous model of bentonite. Here, TS15 make this claim quite explicit, as they write
Still it is possible to define three porosity domains, or water
domains, that can be handled separately: the bulk water, the diffuse
layer water and the interlayer water, the properties for which can
be each defined independently.
This is in essence what I have referred to as “the mainstream view” of bentonite. It is basically “possible” to define anything, but the real question is if provided definitions are relevant and useful. And, as we have already discussed in detail, there is no rationale for introducing these “porosity domains” when modeling water saturated, compacted bentonite.2
Here we will first comment on the conceptual aspects of the provided mathematical description. Thereafter, we will delve into the mathematical formulations, as I’m quite convinced that these are not correct. Unfortunately, this latter part will be quite burdened with equations and notation, but for the motivated reader I think it may be worth going through.
Conceptual aspects
TS15 choose the Nernst-Planck description of ion diffusion, and begin by commenting that this is more rigorous than using Fick’s law. I certainly agree with that a general description of ion diffusion in bentonite requires treating electrostatic couplings between the various system components (TOT-layers, ions). I don’t think, however, that putting up a massively complex description of multi-component diffusion in “three porosity domains” is the appropriate starting point for including such couplings. Since we have every reason to believe that e.g. no bulk water phase is present, I mean that this type of treatment only leads us astray from understanding the actual processes involved (we will return to this aspect in later parts of the review).
Also, as the “Fickian” aspect was the focus of the earlier section on diffusion, a reader of TS15 could here understandably get the impression that a Nernst-Planck treatment will “fix” the “issues” addressed there. But, as we have already discussed in some detail, the shortcomings of the traditional sorption-diffusion model are not solved by including multi-component diffusion in a bulk water phase. They are solved by removing the bulk water phase.
Although the above quotation states that the various “porosity domains” can be handled separately, and that their properties can be defined independently, this is not what is done in TS15. Rather, the treatment of any “porosity domain” assumes equilibrium with the corresponding bulk water phase. The entire description in TS15 is thus fully centered around the bulk water phase.
TS15 insist on treating their model quantities as functions of two spatial coordinates (\(x\) and \(y\)), in what they refer to as a “pseudo 2-D Cartesian system” (I don’t fully understand what that means). Diffusive flux is only assumed to take place in the \(x\)-direction, while the “\(y\)”-dimension is used for stacking the different “porosity domains”. The description can be schematically illustrated like this
Here we have for illustrative purposes discretized the various components in \(x\)- and \(y\)-directions. The bulk water domain is colored blue, the “interlayer” domain pink, and the “diffuse layer” domain green. For a given \(x\)-position, the “diffuse layer” and the “interlayer” domains are assumed to always be in equilibrium with the corresponding bulk water phase. TS15 nowhere consider the length scale in the \(y\)-direction (is it therefore the coordinate system is referred to as “pseudo 2-D”?), which in practice makes the model a collection of 1-dimensional domains that are in equilibrium locally. Note that even though diffusion only is accounted for in the \(x\)-direction, transport occurs also in the \(y\)-direction, as a consequence of equilibration between the “porosity domains”.
This description is exactly what we have investigated in the blog post on why multi-porous models cannot be taken seriously. To summarize what was said there, without properly defining the length scales, it makes no sense to “short-cut” the model in the \(y\)-direction (to assume equilibrium for all domains at the same \(x\) is in a sense equivalent to assuming infinitely high mobility of all components in the \(y\)-direction). And even if we assume that such an assumption is valid — which would mean that we consider a thin strip of stacked parallel domains, where the extension in \(y\) is negligible in comparison to the extension in \(x\) — the resulting model has really nothing to do with actual bentonite. As we concluded in the multi-porosity blog post, the only way to make sense of this type of description is as a set of macroscopic continua that are assumed to be locally in equilibrium. How this equilibrium is supposed to be maintained has never been suggested by any proponent of this description. Note that this description (in particular the existence of a bulk water phase in equilibrium) disqualifies the model for describing swelling and swelling pressure.
Incorrect application of the Nernst-Planck framework
While the presented model makes little sense conceptually, TS15 also
fail in applying the Nernst-Planck framework. The problem arises, as
far as I can see, from that they don’t fully recognize the role of the
electric potential.
As we now begin scrutinizing the details of the formulation, we will suppress the variables \(x\) and \(y\) in order to, hopefully, make the equations a little more readable. It should be understood that any quantity is evaluated for some specific value of \(x\), and that all “porosity domains” are supposed to be in equilibrium at the same value of \(x\).
The electro-chemical potential
In most standard thermodynamic text books we learn that the chemical potential governs the equilibrium associated with mass transfer. Just as e.g. pressure and temperature (which govern mechanical and thermal equilibrium, respectively), the chemical potential is defined by a specific derivative of a thermodynamic potential, e.g.3
where \(c\) is concentration, \(D\) the diffusion coefficient4,
and \(RT\) the usual absolute temperature factor. Here, and in the following, we use the
symbol \(\nabla\), which denotes the general
gradient operator, but
since the model is effectively one-dimensional, it can simply be seen
as a neat way of writing \(\partial/\partial x\).
For charged species, it is common to refer to the quantity defined in eq. 1 as the electro-chemical potential, and write it as composed of an “ordinary” and a purely “electrical” part
where \(z\) is the charge number of the considered species, \(F\) is the
Faraday constant and \(\Psi\) is the electric potential. The
“ordinary” chemical potential \(\mu\) (without bar) is, perhaps a bit
confusingly, also often referred to as the chemical potential. I will
here continue to refer to this part as “ordinary”. The “ordinary”
chemical potential is furthermore conventionally expressed in terms of
a reference potential (\(\mu^0\)) and an activity \(a\)
\begin{equation}
\mu = \mu^0 + RT\ln a \tag{4}
\end{equation}
A lot can be said about the decomposition in eq. 3, but it is clear that singling out an electric potential term is useful in e.g. electrochemistry or for describing charged clay. It should, however, be kept in mind that mass transfer is fundamentally governed by gradients in \(\bar{\mu}\); always keeping eqs. 1 and 2 in mind will avoid us from making mistakes, because the mass transfer rate relates to the “total” (i.e. electrochemical) potential, and for charge neutral species the description reduces to gradients in the “ordinary” chemical potential.
\begin{equation}
j = -cD\nabla \ln a -\frac{cDzF}{RT} \nabla \Psi
\end{equation}
Expressing the activity in terms of an activity coefficient, \(a = \gamma c\), the flux can also be written (TS15 are quite fond of including activity coefficients explicitly)
Considering an arbitrary set of diffusing charged species (using the
index \(i\)), and utilizing that the electric current is zero, lead to
an expression for the electric potential gradient
For the bulk water phase, TS15 indeed provide an expression for the flux that is essentially the same as eq. 6 (their eq. 37), and which they refer to as the Nernst-Planck equation. They claim, however, that the electrochemical potential in this case lack an electric potential term (my emphasis)5,6
In absence of an external electric potential, the electrochemical potential in the bulk water can be expressed as (Ben-Yaakov 1981; Lasaga 1981) \begin{equation} \bar{\mu}_\mathrm{bulk} = \mu^0+RT \ln a_\mathrm{bulk} \end{equation}
But even without an externally applied electric field,7 a zero bulk electric potential cannot be assumed, of course, if the goal is to treat individual ion mobilities; as just shown, the gradient in electric potential that appears in eq. 6 is a result of a corresponding term in the electrochemical potential (eq. 5). Oddly, TS15 seem to treat the electric potential term in the flux as a quantity unrelated to the electrochemical potential, giving it a separate symbol, \(^\mathrm{b}\Psi_\mathrm{diff}\), and writing
\(^\mathrm{b}\Psi_\mathrm{diff}\) is the diffusion potential that
arises because of the diffusion of charged species at different
rates.
It may be natural for a reader at this point to simply assume that
TS15 have missed writing out the term \(zF^\mathrm{b}\Psi_\mathrm{diff}\) when
stating the electrochemical potential. But this seems to be a genuine
misunderstanding rather than a mistake/typo, because the pattern
repeats in the derivation of the flux in the other “porosity
domains”.
For e.g. the “diffuse layer”,8 TS15 recognize the presence of an electric potential in the expression for the electrochemical potential, writing it (this is more awkwardly expressed in eq. 42 in TS15)
TS15 don’t further comment what \(^{\mathrm{DL}}\Psi_\mathrm{diff}\) is supposed to represent, but it must reasonably be understood as “the diffusion potential that arises because of the diffusion of charged species at different rates”, in analogy with what was claimed for the bulk water phase. Note that when eq. 8 is combined with eq. 9, the flux expression contains two different electric potential gradients! (TS15 never address this oddity.)
It is thus quite clear that TS15 misunderstand the function of the electric potential in the Nernst-Planck framework. When presenting the expression for the “diffuse layer” flux (eq. 9), they also refer to Appelo and Wersin (2007), who, in turn, express the misconception explicitly9
The gradient of the electrical potential [in the expression for the
flux] originates from different transport velocities of ions, which
creates charge and an associated potential. This electrical
potential may differ from the one used in [the expression for the
electro-chemical potential], which comes from a charged surface and
is fixed, without inducing electrical current.
I cannot understand this passage in any other way than that Appelo and
Wersin (2007) are under the impression that different electric
potentials can simultaneously act independently in a given point. And
it seems like TS15 are under some similar impression.
This ignorance leads to more errors in the description of the
“diffuse layer” in TS15. We should remember that the promoted model
requires the “diffuse layer” and bulk water domains to be in
equilibrium (for the same coordinate value \(x\)). When TS15 express
this condition, i.e.
\(\bar{\mu}_\mathrm{DL} = \bar{\mu}_\mathrm{bulk}\), they again leave
out the electric potential in the bulk water (eq. 42 in TS 15)
TS15 utilize a simplified version of eq. 11, expressed in terms of concentrations rather than activities, by assuming identical activity coefficients in the two domains10
Note that the exponential in eqs. 11 and 12 actually should contain the electric potential difference between “diffuse layer” and bulk (see below).
As TS15 have not included any electric potential in the bulk water phase, they continue by incorrectly substituting \(RT\nabla \ln a_\mathrm{bulk}\) for \(\nabla\bar{\mu}_\mathrm{DL}\) in eq. 9 (i.e. they use the incorrect relation in eq. 10), giving (TS15 eq. 47)
By substituting eq. 12 into this expression, we end up with the formula for the gradient of the mysterious potential \(^{\mathrm{DL}}\Psi_\mathrm{diff}\) (TS15 eq. 48)
At face value, eq. 15 is a quite weirdly looking equation, as it relates two electric potentials — \(^{\mathrm{DL}}\Psi_\mathrm{diff}\) and \(\Psi_\mathrm{DL}\) — that both are supposed to be associated with the “diffuse layer”. But, as we will see below, there is actually a way to make some sense of eq. 15, by completely reinterpreting what these potentials represent.
A “correct” formulation
Update (260803):The electrostatic potential within the homogeneous mixture model is treated here.
Most of the errors pointed out above are corrected by including the electric potential in the bulk water and writing the condition for equilibrium as (compare eq. 10)
But if we now plug in eq. 18 in eq. 19 we of course get
\begin{equation} j_\mathrm{DL} = -c_\mathrm{DL} D_\mathrm{DL} \nabla \ln a_\mathrm{bulk} + \frac{c_\mathrm{DL} D_\mathrm{DL} zF}{RT} \nabla \Psi^\star – \frac{c_\mathrm{DL} D_\mathrm{DL} zF}{RT} \nabla \Psi_\mathrm{DL}, \end{equation} which can be simplified to \begin{equation} j_\mathrm{DL} = -c_\mathrm{DL} D_\mathrm{DL} \nabla \ln a_\mathrm{bulk} – \frac{c_\mathrm{DL} D_\mathrm{DL} Fz}{RT} \nabla \Psi_\mathrm{bulk}, \tag{20} \end{equation} and, by identifying the electro-chemical potential in the bulk \begin{equation} j_\mathrm{DL} = -\frac{c_\mathrm{DL} D_\mathrm{DL}}{RT} \left ( RT \nabla \ln a_\mathrm{bulk} + Fz \nabla \Psi_\mathrm{bulk} \right ) = -\frac{c_\mathrm{DL} D_\mathrm{DL}}{RT} \nabla \bar{\mu}_\mathrm{bulk} \end{equation}
This whole “derivation” leads back to the rather trivial result that the flux in the diffuse layer is given by eq. 2, which we could have written down from the start! (because the model assumes \(\bar{\mu}_\mathrm{bulk} = \bar{\mu}_\mathrm{DL}\); eq. 16)
As TS15 have established the expression for the gradient of the electrochemical potential in the bulk water phase (which is implicit in their eq. 40), there should strictly be no need to consider a new expression for the same quantity in any other phase. Rather, they could simply have used the bulk water expression in all “porosity domains”, as a consequence of the assumption that these are all supposed to be in equilibrium. In a sense, this is actually what is done in TS15 — mainly by chance! — by establishing eq. 13 (their eq. 47).
Comparing with eq. 20, we see that the incorrect eq. 13 can be “saved” by reinterpreting \(^{\mathrm{DL}}\Psi_\mathrm{diff}\) as \(\Psi_\mathrm{bulk}\). Similarly, as TS15 assume the bulk electric potential to be zero, eq. 15 can be “saved” by also reinterpreting \(\Psi_\mathrm{DL}\) as \(\Psi^\star\) in that expression.12 I find this quite hilarious: By making several errors in its derivation, eq. 15 is in a sense a correct expression for the electric potential gradient in the bulk water — a potential that TS15 has put identically equal to zero.
But even if the total flux in the “diffuse layer” is correctly given by combining eqs. 12, 13 and 15 (and by completely ignoring what TS15 mean \(\Psi_\mathrm{DL}\) and \(^{\mathrm{DL}}\Psi_\mathrm{diff}\) represent), TS15 continue by defining the separate terms in eq. 13 as contributions from the “concentration gradient”, and the “diffusion potential”. As we will explore next, this interpretation fails miserably.
“Relative contributions of concentration, activity coefficient and
diffusion potential gradients to total flux”
According to TS15, the “concentration gradient” and the “diffusion potential” contributions to the “diffuse layer” flux are given by, respectively (TS15 eq. 50 and below)
Here we use the index “conc” for the “concentration gradient” contribution, and “E” for the “diffusion potential” contribution. \(A\) is referred to as a “DL enrichment factor”, and is essentially defined as the concentration ratio \(c_\mathrm{DL}/c_\mathrm{bulk}\). Using the incorrect relation in eq. 12, TS15 write these as \(A = e^{-\frac{zF}{RT}\Psi_\mathrm{DL}}\), but, as we see from eq. 18, they are really given by13 (we continue assuming identical activity coefficients in the two domains)
\begin{equation}
A = e^{-\frac{zF}{RT}\Psi^\star} \tag{23}
\end{equation}
TS15 also define a third contribution, related to the gradient of the bulk water activity coefficient. Here we will not further discuss this contribution, as it does not give any additional insight. Moreover, since TS15 anyway derive their model under the unjustified assumption that activity coefficients in the “diffuse layer” and the bulk water are identical, I cannot see the use of including their spatial variation in the description.14 (TS15 spend a couple of pages on activity coefficient models that we will ignore.)
Examples
To explore the various couplings in the presented model, TS15 apply
the Nernst-Planck framework in three examples. We can see immediately
from the presented graphs that their partitioning of the total flux in
“concentration gradient” and “diffusion potential” contributions
makes no sense.
“Example 2” imposes constant concentration gradients in the bulk water of NaCl and corresponding \(^{22}\mathrm{Na}^+\) and \(^{36}\mathrm{Cl}^-\) tracers; the NaCl concentration drops from 0.1 M to 0.001 M, and the tracer concentrations drop from 10-9 M to 10-11 M (domain length is 10 mm).
The corresponding sodium and chloride tracer concentrations in the “diffuse layer” look like this15
These profiles make sense: bulk water ionic strength decreases with distance, but so do the tracer concentrations. For the process of accumulating \(^{22}\mathrm{Na}^+\) in the diffuse layer, these two effects oppose each other, resulting in a quite flat profile. We thus expect the corresponding “concentration gradient” contribution to the flux to be quite moderate, and to fall off with distance (as the profile flattens with distances). The corresponding flux graph presented in TS15, however, looks completely different16
This plot makes no sense: The “concentration gradient” contribution is seen to increase quite dramatically with distance, rather than falling off. The value of this contribution is also orders of magnitude too large, given the imposed sodium diffusion coefficient of 1.33⋅10-10 m2/s. Moreover, the “concentration gradient” contribution is “compensated” by an equally nonsensical “diffusion potential” contribution. Note, for instance, that the “diffusion potential” contribution is negative, which implies that the corresponding electric field is supposed to be directed towards higher concentrations. This can certainly not be the case, as the electric potential gradient is caused by the negative ion having higher mobility than the positive ion (chloride diffusivity is set to 2.03⋅10-10 m2/s).
In “example 3”, the tracer concentrations in the bulk is set to a constant value (1⋅10-9 M), while the same concentration gradient as in “example 2” is maintained for the main NaCl electrolyte (from 0.1 M to 0.001 M). We thereby expect the corresponding \(^{22}\mathrm{Na}^+\) concentration in the “diffuse layer” to strongly increase with distance, which is also what is presented in TS15
while the corresponding flux plot looks like this16
This plot is almost comically absurd. According to TS15, the highly skewed concentration profile above is supposed to give no (zero, nil, 0) contribution to the flux (we see from eq. 21 that this is a consequence of that this “contribution” is directly proportional to the concentration gradient in the bulk). Instead, the huge flux is supposed to be caused entirely by an electric field that has the wrong direction! I can’t even really begin to imagine how these two plots have ended up next to each other in a peer-reviewed published article.
Note that the flux associated with a concentration gradient is what we may reasonably call a “Fickian” contribution. If TS15 mean (and they do) that these examples demonstrate how ion diffusion in bentonite works, we can understand the focus on the “Fickian” aspect at the beginning of the article (covered here). But the only reasonable response to these outlandish results is that they demonstrate that the definitions of eqs. 21 and 22 simply make no sense.
The real concentration gradient and electric field contributions
The only reasonable way to define “concentration gradient” and “diffusion potential” contributions to the “diffuse layer” flux is as the two terms in eq. 19, respectively. To rewrite these, we utilize eq. 16 (or 18), giving for the “concentration gradient” contribution (we continue ignoring activity coefficients)
where we have utilized that \(\nabla \Psi_\mathrm{bulk}\) is actually what is expressed in eq. 15 (where \(\Psi_\mathrm{DL}\) should be replaced by \(\Psi^\star\)).
We note that, to compensate the nonsensical expressions given in TS15, we should add the term \(j^\star\) (eq. 25) to the “concentration concentration” contribution (eq. 21), and subtract the same term from the “diffusion potential” contribution (eq. 22). Making these corrections gives the following components of the tracer fluxes in “example 2”
This is an infinitely more reasonable situation than what is depicted in TS15. Although the sodium flux has a non-negligible contribution from the electric field, the larger contribution is still from the concentration gradient (and none of these are gigantic terms that cancel). The concentration contribution also falls off with distance, in accordance with the shape of the concentration profile.
For chloride, the field contribution to the flux is negligible, i.e. this flux is essentially fully governed by the concentration gradient. The electric field contributions for both ions are also seen to have the correct signs: the electric field is directed from high to low concentration, and mainly functions to boost the sodium transport, in order to “keep up” with the faster chloride ions.
For “example 3” we get the following picture
The corrected \(^{22}\mathrm{Na}^+\) flux is essentially fully due to the concentration gradient, in absolute contrast to what is concluded in TS15, who mean that this flux is completely governed by an electric field in the wrong direction. Also the \(^{36}\mathrm{Cl}^-\) transport is basically solely governed by the concentration gradient, rather than by an incorrectly directed electric field (as stated in TS15). In conclusion, most of the “diffuse layer” diffusion in these examples can actually be classified as “Fickian”.
We may also investigate the electric potential profile in the
“diffuse layer” in both of these examples (this is the same in the
two cases, as the main electrolyte distribution does not change)
Here we have chosen the reference \(\Psi_\mathrm{DL}(0) = 0\). The total potential drop is only about 1 mV. Such a relatively small drop is reasonable because the denominator in the Nernst-Planck expression for the electric potential gradient (eq. 7) will always be large due to the ever-present counter-ions in the “diffuse layer”. The electric potential gradient — and thus the corresponding electric potential drop — is therefore suppressed. Physically, this means that since many (equally charged) charge carriers are always present, smaller potential differences are required to cancel electric currents caused by differences in mobility (a “diffuse layer” is a quite good conductor).
Even worse problems?
Even though some sense can be made out of the derived expression for the flux in the “diffuse layer” domain — by completely reinterpreting the electric potentials involved — it seems as the overall model is too constrained. Specifically, for an imposed set of concentration profiles in one domain it is not possible, as far as I can see, to simultaneously have zero current in all domains, while also maintaining (Donnan) equilibrium. As this blog post is already quite massive, I will elaborate on this point in the next part of the review.
Summary
Here is an attempt to sum up the main messages of this blog post.
Conceptually, the clay model presented in TS15 is exactly what was discussed in the blog post on multi-porous models, and the same issues that are identified there are present here. In particular, no attention is paid to length scales (perhaps that is why TS15 call the coordinate system “pseudo-2D”…), and no mechanism whatsoever is suggested for how the different diffusing domains are supposed to maintain equilibrium.
Mathematically (or perhaps physically), the presented Nernst-Planck flux expressions are incorrectly derived. The source of the error, as far as I can see, appears to be a misunderstanding of how electric potentials function.
TS15 define “contributions” to the “diffuse layer” flux, claimed to be related to the concentration gradient and the “diffusion potential” (i.e. the electric field), respectively. It is, however, quite obvious that these “contributions” are completely nonsensical: highly skewed concentration profiles are claimed to not have any concentration gradient contributions, and several “diffusion potential” “contributions” have the electric field in the wrong direction. We have shown that these “contributions” can be corrected, where the correction term involves the gradient of the Donnan potential. With these corrections, fluxes in the provided examples must be interpreted completely differently (they’re basically “Fickian”).
As far as I can see, the proposed model has even larger problems, related to the imposed Donnan equilibrium. We will address this issue in the next part.
Update (260526): Part V of this review is found here.
Update (260922): The full Nernst-Planck framework is treated within the homogeneous mixture model here.
Footnotes
[1] As I have commented in the earlier parts: TS15 are
fond of using the general terms “clays” and “clay minerals”, while
it is clear that the publication mainly focus on systems with
substantial ion exchange capacity and swelling properties. Here we
will continue to use the term “bentonite” for these systems, and
ignore the frequent references in TS15 to more general terms.
[2] It is of course crucial to include a component that represents compartments where the exchangeable ions reside. This is done in the TS15 model by both the “diffuse layer water” and the “interlayer water” domains. But the distinction made between these domains is based on the flawed “stack” concept.
[3] This equation assumes a single component. The
formulation of the Nernst-Planck framework naturally involves
several different charged species. When several species are
involved, we will indicate this with an index \(i\) in the equations.
[4] In some of their equations, TS15 use (electrical) mobility, \(u\), rather than diffusivity, \(D\). These quantities are related via the Einstein relation \(D = uRT/(F|z|)\). I don’t see the point in involving \(u\), as it typically makes expressions even more cluttered, and since we here ultimately are interested in diffusion coefficients anyway.
[5] In order to not cause too much confusion,
and to try to simplify a bit, I use slightly different mathematical
notation than what is actually used in the quotation. In particular,
I use the notation \(\bar{\mu}\) for the electro-chemical potential,
while TS15 don’t use a bar (\(\mu\)). I also try to avoid the index
\(i\) as much as possible.
[7] I
whined about electrostatics being poorly understood in the
bentonite research field in an earlier part of this review, but here
is more fuel for my argument. The statement “absence of an
[external] potential” has no physical meaning, as we are free to
choose the reference point (the absolute value of a potential has no
physical meaning). What TS15 must mean in the quote is “the absence
of an external electric field”. The electric field relates to the
potential as \(E = -\nabla \Psi\). Thus, all gradients of electric
potentials that occur in this text are synonymous with electric
fields (electric fields drive electric currents).
[8] This post focus almost
entirely on the “diffuse layer” domain, but a similar analysis can
be made for the “interlayer” domain. This is left as an exercise
for the reader.
[9] It should of course also rather read “…which creates a charge separation and an associated potential gradient.”, or simply “…which induces an electric field.” (showing that this part of the sentence is redundant). See also footnote 7.
[10] TS15 write cryptically that
equating the activity coefficients (and the reference potentials) in
bulk and “diffuse layer” is assumed “by following the [Modified
Gouy-Chapman] model”. But I don’t see why this model has to be
alluded to here, these assumptions can just be made.
[11] Yes, this is a Donnan potential. We will discuss this more in the next part part of the review. Update (260526): Part V of this review is found here.
[12] Again, this is related to Donnan equilibrium between the bulk and “diffuse layer” domains, that we will discuss further in the next part. Update (260526): Part V of this review is found here.
[13] This is \(f_D^{-z} \), where \(f_D\) is the Donnan factor.
[14] Rather, I would argue for that
the activity coefficients in a “diffuse layer” domain will be
quite insensitive to the imposed external (bulk) concentration, for
details see Birgersson (2017).
[15] In producing these graphs we have used the Donnan equilibrium framework to calculate the “diffuse layer” concentrations. These are given from eq. 23, where \(\Psi^\star\) is calculated from
where \(q\) is a measure of the structural charge in the “diffuse layer”, in the examples set to \(q\) = 0.33 M.
[16] Note that I have not included activity coefficient gradients when producing the plots in this section. They may therefore differ slightly from the published plots. This does not in any way influence the conclusions drawn here.
Reading Gl10 gives the impression that the study consists solely of through-diffusion tests of a set of different tracers (HTO, sodium, chloride), in a set of different materials (Kaolinite, “Na-Illite”, Na-montmorillonite), at nominal density 1.9 g/cm3. A lot of additional information, however, is published in a later, completely separate publication: Glaus et al. (2011), which we will refer to as Gl11. Needless to say, this is a quite peculiar way of reporting a study. For instance, Gl10 do not provide any geometrical information about the samples (!), but this is found in Gl11; Gl11 also report corresponding out-diffusion measurements that apparently were made.1
Even with the combined sources of Gl10 and Gl11, information is not
entirely complete. For example, tests have been carried out in
duplicates, but evaluated diffusion parameters are only reported as
averages (table 2 in Gl10). Furthermore, the sources give
contradictory information in some instances (this is further discussed
below). Scraping both sources for information, these are the tests
that have been performed, as far as I understand:
Through-diffusion
In total 8 separate tests were performed, with NaClO4 background concentrations of 0.1 M, 0.5 M, 1.0 M and 2.0 M. These were performed in sequence in four different tests cells. Thus, two tests at 1.0 M background concentration were first performed in two different samples; thereafter, the same two samples were used for two additional tests at 2.0 M. Similarly, in two other samples, two 0.5 M tests were followed by two 0.1 M tests. The steady-state concentration profile in the clay was measured in one single test, performed at 0.1 M background concentration.
In this assessment we will also make use of the results from through-diffusion of water (HTO). These were made at background concentrations 0.1 M and 1.0 M. We will return to the question of whether they were carried out in the same samples as used for the chloride-diffusion experiments.
Out-diffusion
Most of the through-diffusion tests were followed by out-diffusion tests: after steady-state was reached, the external reservoirs were exchanged for tracer free solutions, and diffusion of chloride out of the sample was recorded.
Out-diffusion was tested on all samples at background concentrations 0.5 M and 2.0 M, and on one sample at background concentration 0.1 M.
Sorption
The montmorillonite material was tested for sorption of chloride, in suspensions with background concentrations of either perchlorate or chloride (at 0.5 M).
Equilibrium tests
At least one test was conducted to investigate the amount of ClO4 in the clay after the sample was equilibrated with a specified external concentration.
Investigation of swelling during dismantling.
The samples were cylindrical with diameter 2.54 cm, and with slightly different lengths, close to 1.0 cm. The sample volume is thus roughly 5 cm3.
In the following, we mainly refer to the chloride diffusion tests in
montmorillonite. Although the diffusion parameters are only reported
as averages, each individual parameter is actually found in a single
plot in Gl10 (“Fig. 6”). From this plot we can extract results from
each individual through-diffusion test (see below).
In Gl10 are also presented breakthrough curves (flux vs. time) for four tests, one for each different background concentration. Similarly, in Gl11 are presented three flux-vs.-time plots for out-diffusion. As will be further discussed below, we have to do some combined guess- and detective work in order to identify these flux evolution curves with specific samples.
Material
The material is referred to as montmorillonite “from Milos”, and was prepared specifically for the study. Bentonite from Milos (Greece), purchased from Süd-Chemie (now Clariant), was repeatedly washed in strong NaCl solutions to remove most of the accessory minerals and to convert the clay to essentially pure sodium-form. Excess NaCl was subsequently removed from the clay by dialysis. Gl10 present analyses of the chemical composition of both the used materials, as well as of a further purified 0.5 \(\mu\)m fraction of the montmorillonite material. From these analyses it is concluded that the used montmorillonite still contains some silica accessory minerals (3 — 4%), as well as some carbonate (calcite). We may thus assume a montmorillonite content of around 95%.
Concerning the cation population, Gl10 assert that the detected calcium is “most probably” present as CaCO3 rather than being part of the exchangeable cations. However, as the purification procedure used here is quite similar to that used in Muurinen et al. (2004) — that we have assessed earlier — we may expect some influence of calcium on the exchangeable cations. Muurinen et al. (2004) measured a Na/Ca-ratio of approximately 90/10 in their material, which also contained some carbonate (as well as sulfate). Here we assume that the used Na-montmorillonite is basically a pure sodium system, but should keep in mind that the presence of calcium may somewhat influence the results, especially since the different samples are exposed to very different external sodium concentrations.
Sample density
The nominal density for all samples appears to be 1.9 g/cm3, but actual sample densities are not reported (in Gl10, it is even hard to find information on nominal density). However, results of HTO diffusion in four tests (at 0.1 M and 1.0 M background concentration) indicate a considerably lower density. Porosities inferred from the breakthrough curves for these tests range between approximately 0.35 — 0.42. As is further discussed below, we here choose a range for the porosity of 0.321 — 0.394. Assuming a grain density of \(\rho_s\) = 2.8 g/cm3, this corresponds to a density range of 1.9 g/cm3 — 1.7 g/cm3 (effective montmorillonite density 1.87 g/cm3 — 1.66 g/cm3).
Uncertainty of external solutions
We have no reason to doubt the validity of the solutions used, and
will assume no uncertainty here.
Evaluations from the diffusion tests
The chloride diffusion data in Gl10 and Gl11 is essentially analyzed in terms of the effective porosity model, although the fitted parameters are the “effective diffusivity” (\(D_e\)) and the “rock capacity factor” (\(\alpha\)). But for chloride, Gl10 use \(\alpha\) and \(\epsilon_\mathrm{eff}\) (the “effective porosity”) interchangeably.2 To avoid confusion, we will only use the notation \(\epsilon_\mathrm{eff}\).
As mentioned, Gl10 only tabulate the mean values of \(D_e\) and \(\epsilon_\mathrm{eff}\) for each background concentration, but we can extract each individual parameter graphically. The extracted \(D_e\) and \(\epsilon_\mathrm{eff}\) are listed here.3
With a single exception, the averages are identical with what is listed in table 2 in Gl10, which confirms the accuracy of the extracted parameters (for 1.0 M background concentration, the average \(\epsilon_\mathrm{eff}\) is 0.050 rather than the tabulated value 0.051). In the above table are also listed the corresponding pore diffusivities, evaluated as
From the flux and profile data found in Gl10 and Gl11, we can also
evaluate several pore diffusivites ourselves. Such values are
presented in the fifth column in the above table, and corresponding
steady-state fluxes are found in the sixth column. Below is compared
various flux vs. time data with my own simulations.
Regarding the breakthrough curves, the test design is here much better
than what we have encountered in earlier assessments; the transient
stage is properly sampled rather than that the data mainly represents
a sequence of steady-state measurements.4 This makes the inference of diffusion parameters
quite easy and robust.
Comparing the through-diffusion and out-diffusion results we can conclude that the data presented in Gl10 and Gl11 for background concentration 0.1 M most probably is for the same sample. Although the fitted parameters differ somewhat, the text of Gl11 states a steady state flux of 1.8⋅10-13 mol/s/m2 for the other 0.1 M sample, which was subsequently sectioned. As the presented through-diffusion flux is considerably smaller we may conclude that this is the same sample for which out-diffusion subsequently was conducted.
For the 0.5 M data, we can instead conclude that the two data sets must stem from two different samples, as the steady-state fluxes differ by roughly a factor of 2. For the 2.0 M data, the fitted parameters are very similar for the two test phases, which may indicate that they were measured in the same sample. However, the parameters are also very similar for the other test. The same is true for 1.0 M data (for which no out-diffusion was performed).
From steady-state fluxes and reported values of \(D_e\), we can calculate the corresponding tracer concentration in the source reservoir as
where \(L\) is sample length.5 Source tracer concentrations evaluated in this
way are presented in the last column in the above table (source
concentration is only reported for a single test, in Gl11).
Finally, we can also look at the presented tracer profile at
termination, which was determined in a single case,6 for one of the 0.1 M tests.
We note — as does Gl11 — that the concentration profile shows quite extensive interface excess, a topic that we have discussed in a separate blog post. The main focus of Gl11 is actually a modeling treatment of these regions, but here we focus on the linear interior part of the profile.7 Fitting a line to this part (see figure) we extract a slope of -22.0 nmol/g/m. Gl11 do not report the corresponding density profile (that most certainly was measured), but using the nominal density (1.9 g/cm3), gives a corresponding clay concentration gradient of \(\nabla c_\mathrm{ss} = -0.0418\) mol/m4. Combining this value with the steady-state flux (1.8⋅10-13 mol/m2/s; reported in the text in Gl11), we can independently evaluate the pore diffusivity
This is in reasonable agreement with the value evaluated from \(D_e\) and \(\epsilon_\mathrm{eff}\).
In conclusion, even though crucial information is missing in Gl10, the re-evaluations made here, with help from information in Gl11, confirm the adequacy of the reported parameters \(D_e\) and \(\epsilon_\mathrm{eff}\). A perhaps single conspicuous detail is that the source concentration in one of the 0.5 M tests appears to have been about twice as large as for any of the other tests. There may, of course, be a reasonable explanation for this.
Evaluating chloride equilibrium concentrations
As noted in earlier assessments, the convenient quantity expressing the chloride equilibrium in through-diffusion tests is the ratio \(\bar{c}(0) / c^\mathrm{source}\), where \(\bar{c}(0)\) denotes the tracer concentration within the clay, at the interface to the source reservoir (for details, see here).
From the reported values of \(\epsilon_\mathrm{eff}\), the most
straightforward way to evaluate the chloride equilibrium
concentrations is
where \(\phi\) is the (physical) porosity. Gl10 (or Gl11) don’t provide information on actual measured densities, leaving us little choice but to use the nominal density in order to get a value for \(\phi\) in eq. 3. However, Gl10 also provide data for corresponding water (HTO) diffusion measurements. As mentioned above, these measurements indicate densities significantly lower than the nominal value. The (graphically extracted) values for \(D_e\) and \(\epsilon_\mathrm{eff}\) for HTO are
For water, the effective porosity parameter is really an estimate of
the physical porosity, and we can thus use this value to calculate a
corresponding density, which is presented in the last column in the
table.
Gl10 state
The diffusion of the various radioactive tracers (HTO, 22Na, 36Cl) was measured in sequence, each new tracer run was started after the out-diffusion of the previous tracer had been completed.
which is hard to interpret in any other way than that the above HTO parameters have been evaluated in the same samples in which chloride diffusion was tested. However, the protocol presented in Gl11 does not include any HTO diffusion “measured in sequence” (see above for information on the test protocol). The two sources evidently contain some contradictory information.8 Under any circumstance, as water diffusivity is claimed to be measured in samples with the same nominal density, we must assume a quite substantial uncertainty of the actual sample densities. In evaluating the chloride equilibrium concentrations, we therefore choose a porosity interval between the nominal value and the average given from the water parameters: \(\phi\sim\) 0.321 — 0.394. The table below lists the corresponding intervals for the chloride equilibrium concentrations
From the out-diffusion tests we can also evaluate the equilibrium concentrations “independently”, by integrating the flux. As discussed in the assessment of Van Loon et al. (2007), this integral (multiplied by sample area) gives one third of the total amount of tracers present in the clay at the start of the out-diffusion phase (these quantities are labelled “Acc.” in the above diagrams). With an estimate of the tracer concentration in the source reservoir, the equilibrium chloride concentration can thus be evaluated as
where \(N_\mathrm{right}\) denotes the final amount of tracers in the target reservoir. The corresponding chloride equilibrium concentrations are listed in the last column in the above table.
Finally, we also look at the 0.1 M test for which the steady-state tracer concentration profile was recorded. Extrapolating the linear part to the clay/source interface, gives a chloride content of 0.282 nmol/g, which corresponds to a clay concentration interval of 5.37⋅10-4 — 4.80⋅10-4 mol/m3, using the porosity interval defined above.9 Given the source concentration (0.024 mol/m3), these values correspond to a chloride equilibrium concentration ratio in the range 0.051 — 0.071.
The different ways of estimating chloride equilibrium concentrations provide a quite consistent picture (see above table). Although the information has been difficult to extract, it may thus seem that, in the end, all is good and well. However, we should note that the evaluated pore diffusivities show a quite peculiar dependency on background concentration.
Such a dependency, which has not been observed in earlier assessed studies, directly influence the evaluated equilibrium concentrations. As the breakthrough curves are so well sampled in the present study, this result can hardly be attributed to uncertainty in the values of \(D_p\). While Gl10 don’t explicitly identify this behavior (they do not evaluate \(D_p\)), a main focus of the study is actually to account for it, by means of “Archie’s law”, i.e. by suggesting a non-linear functional relationship between \(D_e\) and \(\epsilon_\mathrm{eff}\). I am strongly critical of such a treatment, but will refrain from discussing it here, as the focus of this assessment is the data itself rather than its interpretation (we have discussed this issue in a previous blog post).
An obvious alternative interpretation of this behavior is that chloride adsorbs on some system component, in the sense of becoming immobilized (what I have earlier dubbed true sorption). Gl11 test this hypothesis by performing additional batch sorption tests on the montmorillonite, in background solutions of NaCl and NaClO4 (0.5 M) at various pH. Although they cannot exclude a “\(R_d\)” value of the order of 10-4 m3/kg, they ultimately conclude that chloride do not sorb to any significant extent in these systems (and continues with “explaining” the behavior as resulting from other mechanisms).
I mean, however, that some experimental observations suggest that a sorption mechanism may be active. In addition to the above limit for the \(“R_d”\) value, we may note significant chloride sorption in the kaolinite samples, which were also studied in Gl10. There may of course be a reasonable explanation for why chloride sorption is observed in kaolinite, while it is not active in montmorillonite, but this issue is not really discussed in Gl10. Also, the recorded steady-state chloride content profile suggests a non-zero value at the interface to the target reservoir. This could, reasonably, indicate that some chloride is immobilized.
Perchlorate equilibrum concentrations
On the other hand, an additional argument against chloride sorption is that equilibrium perchlorate concentrations seem to be comparable with those evaluated for chloride. Gl11 don’t report perchlorate content directly, and we have to do some work to extract the corresponding equilibrium concentration in the 0.1 M sample that was sectioned. Gl11 plot the chloride tracer content for this sample together with “the concentration in the anion-accessible volume”, labelled \(c_\mathrm{acc}\).
\(c_\mathrm{acc}\) is, unsurprisingly, not a directly measured chloride concentration, but a quite elaborate interpretation of the data. From the unreported ClO4 content, an “anion-accessible porosity” variable has been calculated, by simply multiplying the physical porosity by the ratio between internal and external ClO4 concentrations. \(c_\mathrm{acc}\) is, in turn, defined as the actual measured chloride content distributed in a volume that corresponds to this “anion-accessible porosity”. By combining the reported chloride content (let’s call it \(\bar{n}_\mathrm{Cl}\)) and \(c_\mathrm{acc}\), we can thus de-derive the perchlorate equilibrium concentration as
Using this formula for the inner “linear” part of the profile (2 — 8 mm) gives the values 0.060, 0.059, 0.061 and 0.062, assuming nominal density. For porosity 0.394 the corresponding values are 0.044, 0.043, 0.044, and 0.045. We note that a range 0.043 — 0.062 for the equilibrium concentration ratio at 0.1 M background is in line with the previous evaluations. It should be noted, though, that this evaluation is for perchlorate, which not necessarily has the same equilibrium concentration as chloride. Nonetheless, this evaluation shows a similar, relatively high, equilibrium concentration also for this ion.
In fact, Gl11 provide results from yet another test where the focus is the perchlorate equilibrium,10 this time at a background concentration of 0.5 M. The results are reported as physical and “anion-accessible” porosities, evaluated from measuring water and perchlorate content.11
We note that also this sample shows substantial interface excess, but here we focus on the inner, relatively flat part (marked points in figure). From values of physical and effective porosity, we can directly calculate an equilibrium concentration in accordance with eq. 3. In this case the equilibrium concentration can also be related to a measured density. Using the average values gives a perchlorate equilibrium concentration ratio of \(\bar{c}_\mathrm{ClO_4}/0.5\; \mathrm{M} = 0.150\). Note that this value should be associated with density of 2.05 g/cm3 (the average porosity for the inner points is 0.259). This perchlorate equilibrium concentration ratio is nevertheless considerably larger than what was evaluated for chloride at (nominal) density 1.9 g/cm3 (0.11). This may indicate that perchlorate has a larger preference for the clay than chloride in these systems, but, as 2.05 g/cm3 is remarkably high, I suspect that measured water contents in this test have been systematically underestimated.
Summary and verdict
With only the information given in Gl10, I would judge the provided
information too uncertain to be used for quantitative process
understanding of chloride equilibrium in bentonite. With the
additional information provided in Gl11, however, we have seen that
the diffusion parameters — and consequently the equlibrium
concentrations that can be inferred — can be assessed to have been
quite robustly evaluated. Needless to say, access to a
completely separate publication should not be needed in order to make
this type of assessment. Nevertheless, my choice is to keep this data
to use for evaluating e.g. performance of models for salt exclusion.
A remaining uncertainty is the actual density of the tested samples. Results from corresponding water tracer tests suggest densities considerably lower than the nominal density. It not fully clear, however, if these water diffusion tests were conducted with separate samples or with the same samples as for the chloride diffusion tests.
Finally, these results complicate the picture of chloride equilibrium
concentrations in bentonite, as they do not fully comply with earlier
ones. In particular, here is observed a dependency of the pore
diffusivity on the background concentration, and chloride contents,
which are not seen in other studies. For anyone that is truly
interested in how salts distribute in bentonite, it should be a
priority to understand how the present results can be reconciled with
other chloride equilibirum results.12
Below is plotted the chloride equilibrium concentrations evaluated
from this study. For each background concentration is drawn an
“uncertainty box”, that takes into account the uncertainty in
density, as discussed above, and the corresponding interval in
equlilibrium concentration ratio. The corresponding points have been
arbitrarily put in the middle of these “uncertainty boxes”. The
effective montmorillonite density has been calculated assuming a
montmorillonite content of 95%.
To compare the present results with others, we have also plotted some chloride equilibrium concentration evaluated from Van Loon et al. (2007), that we have assessed previously.
[1] To be fair, reading Gl10 carefully, out-diffusion is briefly mentioned a couple of times.
[2] Gl10 rather use the term “accessible porosity”, and symbol \(\epsilon_\mathrm{acc}\), but we stick with the terminology that we have used in thepreviousassessments. Also, a critique of mixing the effective porosity model (that involves \(\epsilon_\mathrm{eff}\)) and the traditional diffusion-sorption model (that involves \(\alpha\)) is found here.
[3] For background concentration 0.5 M it is difficult to resolve if the diagram in Gl10 has a single point, or if there are two points on top of each other. As Gl10 claim that duplicates were made at all concentrations, here we have assumed two different samples with identical parameters.
[4] The
through-diffusion flux evolution for background concentration 0.1 M
plotted in Gl10 seems not to be complete: the diagram shows data
points up until day 160, but Gl11 state that the test was conducted
for 229 days.
[5] The simulations presented here use \(L\) = 9.75 mm for the samples with background concentration 2.0 M, and \(L\) = 10.25 mm for the samples with background concentrations 0.1 M and 0.5 M. These are average values from the sample lenghts reported in Gl11.
Tracer profiles of 36Cl in Na–mom were found to be in qualitative agreement with those found by Molera et al. (2003) and exhibited two distinct linear regions with different slopes. In contrast to Molera et al. (2003) we interpret the 36Cl profiles in terms of heterogeneities of compaction in the boundary zones of the clays and not as the result of two diffusion processes. In view of these ambiguities, tracer profiles were generally used as a consistency test and not for the calculation of \(D_e\) values.
At least to me, this way of writing gives the impression that
profiles were recorded for most of the tests. In Gl11, however, we
learn that only a single profile was recorded.
[7] Gl11 argue for that the non-linear
parts of the profile actually reflect the state of the sample during
steady-state, rather than being an effect of dismantling. I am
strongly critical to their arguments, and plan to comment on this in
a separate blog post.
[8] For the sodium measurements in montmorillonite, it is certain that the above statement is false. Most of these were made in 5.4 mm samples, and they were all sectioned. Morover, these were reported in a much earlier publication: Glaus et al. (2007).
[9] The clay concentration is calculated as \(\bar{c} = \bar{n} \cdot \rho_d/\phi\), where \(\bar{n}\) denotes the chloride concentration as amount per dry mass.
[10] The main focus in Gl11 is
actually the density distribution in the interface regions of the
sample, but this is a straightforward perchlorate equilibrium test.
[11] The data in
this plot has been “de-scaled”, as it was measured in a 5.4 mm
sample, but then “recalculated” (!?) for a 10 mm sample in Gl11.
[12] I intend to write a
follow-up blog post discussing these issues.
The subsection we focus on here, “Adsorption processes in clays”,
contains very little descriptions of fundamental properties of
bentonite, and is instead almost exclusively devoted to detailed
discussions on various models. As an example, already in the
first paragraph the text digresses into dealing with the problem of
defining “surface species activity” in the “DDL”2 model…
TS15 discuss adsorption separately on “outer basal surfaces”, “interlayer basal surfaces”, and “edge surfaces”. Note that the distinction between “outer” and “interlayer” basal surfaces requires that we view the compacted bentonite as composed of stacks (referred to as “particles” in TS15). But this idea is just fantasy, as we have discussed in the previous part and in a separate blog post. Moreover, central to the description of adsorption processes in TS15 is the idea of a Stern layer. This concept was briefly introduced in the previous subsection (“Electrostatic properties, high surface area, and anion exclusion”)
The [electrical double layer] can be conceptually subdivided into a Stern layer containing inner- and outer-sphere surface complexes […] and a diffuse layer (DL) containing ions that interact with the surface through long-range electrostatics […].
The next time this concept is brought up is at the beginning of the
discussion on adsorption on “outer basal surfaces”
The high specific basal surface area and their electrostatic properties give rise to adsorption processes in the diffuse layer, but also in the Stern layer.
I have written a separate blog post arguing for that the idea of Stern layers on montmorillonite basal surfaces is unjustified. Note that the notion of Stern layers on montmorillonite basal surfaces in the contemporary bentonite literature de facto means that these surfaces are supposed to be full-fledged chemical systems. In particular, the basal surface is supposed to contain localized “sites” that interact generally with ions to form surface complexes and that can involve covalent bonding.
Note further that the Stern layer was originally introduced as a model (or a model component) that extends the Gouy-Chapman description of the electric double layer. TS15, on the other hand, use the term “Stern layer” to refer to an actual physical structural component. And just as in the case of several other “components” that has been introduced in the article (“particles”, “inter-particle water”, “free or bulk water”, “aggregates”…), the existence of a Stern layer is just declared rather than argued for. And just like with the other components, these are not universally adopted. I don’t think it is appropriate to include Stern layers in this way in a review article when established parts of the colloid science community refer to them as an “intellectual cul de sac”.
So in order to even begin to criticize what TS15 actually write about adsorption processes here, one has to accept both the flawed idea of stacks as fundamental structural units and the far from universally accepted idea of Stern layers on montmorillonite basal surfaces. I will therefore refrain from doing that, and simply proclaim that I don’t accept the premises. (I believe I will have reasons to return to the models presented here when reviewing later sections of TS15.)
Additional remarks
But I think it is worth reminding ourselves that at the end of the previous section (covered in part I) we were promised that this section should qualitatively link “fundamental properties of the clay minerals” to the diffusional behavior of compacted bentonite. A reader of TS15 will thus expect this section to contain, in particular, a reasonable description and discussion on how compacted montmorillonite works. Instead a very specific (and flawed) model is imposed on the reader: the first subsection (covered in part II), introduced the fictional stack concept, and gave a confused and irrelevant explanation of anion exclusion; the presently discussed subsection is centered around Stern layers.
If the authors truly did what they claimed, in this section they should have addressed the consequences of montmorillonite TOT-layers being charged — a universally accepted fact — without introducing further assumptions. This would naturally lead to a discussion on osmosis, swelling, swelling pressure and semi-permeable boundary conditions (all simple empirical facts). These topics, in turn, should lead to considerations of e.g. ionmobility and chemical interface equilibrium. Not a single one of these topics are, in any meaningful sense, actually addressed in this section.
Before ending this part of the review, I also would like to focus on what is being said about “interlayers”. We should keep in mind that TS15 — together with a large part of the contemporary bentonite research community — assume “interlayers” to be something different than simply the space between adjacent basal surfaces: these are supposed to be internal to the fantasy construct of a stack. When discussing adsorption in these presumed compartments they write
The interlayer space can be seen as an extreme case where the
diffuse layer vanishes leaving only the Stern layer of the adjacent
basal surfaces.
Of everything I’ve read in the bentonite literature, this is the closest I’ve come to see some actual description of what the fundamental difference between an “outer basal surface” and an “interlayer” is supposed to be. But let’s think this through. TS15 have claimed that an electric double layer is composed of a Stern layer and a diffuse layer, and we have vaugley been told that ions in the Stern layer are immobile. The above quotation thus implicitly says that that “interlayer” ions are not mobile, and that diffuse layers are only supposed to exist on “outer basal surfaces” (which, remember, is a fantasy component). But — disregarding that the stack-internal “interlayer” also is a fantasy concept — it is an indisputable experimental fact that has been known for a longtime that interlayers provide the only relevant transport mechanism in compacted bentonite.
Thus, either TS15 here provide us with yet another incorrect description of the behavior of compacted bentonite (that “interlayer” ions are immobile) or they are claiming, somewhat contradictorily, that Stern layer ions are mobile after all. But if Stern layer ions diffuse, such a structural component could reasonably not have been singled out in the first place! (The diffuse layer is supposed to have “vanished”.) As with many other issues in TS15, this question is left vague and unanswered.3 The continuation of the text does not make things clearer
For this reason, the interlayer space is often considered to be
completely free of anions (Tournassat and Appelo 2011), although
this hypothesis is still controversial (Rotenberg et al. 2007c;
Birgersson and Karnland 2009).
An interlayer completely devoid of anions certainly play by other rules than an “ordinary” electric double layer. Does this mean that TS15 assume “interlayer” ions to be immobile?4 Anyway, it is an indisputableexperimental fact that anions occupy interlayers, and I find it quite bizarre to find myself referenced in connection with the “controversial hypothesis”. The idea of compartments completely devoid of anions is widespread in the contemporary bentonite research community, but no one has ever suggested a mechanism for how such an exclusion is supposed to work; here, it apparently should be related to “Stern layers” in some (unexplained) manner. At the same time, the simplest application of Donnan equilibrium principally explains e.g. the behavior of the steady-state flux in anion tracer through-diffusion tests.
The agreement between [Poisson-Boltzmann] calculations and MD
simulation predictions was somewhat worse in the case of the
\(\mathrm{Cl^-}\) concentration profiles than in the case of the
\(\mathrm{Na^+}\) profiles (Figure 3), perhaps reflecting the poorer
statistics for interlayer Cl concentrations or the influence of
short-range ion-ion interactions (and possibly ion- water
interactions, as noted above) that are not accounted for in the
[Poisson-Boltzmann] equation. Nevertheless, reasonable quantitative
agreement was found (Table 2).
Here they acknowledge not only that anions do occupy interlayers, but also that the interlayer plays by the same rules as the “ordinary” electric double layer (“Poisson-Boltzmann calculations”). What happened to the “vanishing” diffuse layer, and to “considering” the interlayer to be “completely free of anions”? I find it quite outrageous that they fail to acknowledge these blatantly mixed messages with so much as a single word.
Update (251106): Part IV of this review is found here.
Footnotes
[1] As I have commented in the
earlier parts: TS15 are fond of using the very general terms
“clays” and “clay minerals”, while it is clear that the
publication mainly focus on systems with substantial ion exchange
capacity and swelling properties. Here we will continue to use the
term “bentonite” for these systems, and ignore the frequent
references in TS15 to more general terms.
[2] For some
reason, “DDL” is short for (the very generically sounding) “double
layer model”. Why not “DLM”?
[3] Spoiler: in later sections describing models, TS15 allow for the possibility of transport in “interlayers”.
[4] Questions like these can often not be answered because so many statements in TS15 are vague and ambiguous. In this discussion we have to refer to statements such as (my emphasis)
“The EDL can be subdivided into a Stern layer […] and a diffuse layer […].”
“The interlayer can be seen as an extreme case where the diffuse layer vanishes […]”
“The interlayer space is often considered to be completely free of anions […]”
I get annoyed by too much of such language in scientific
publications.
I argue that the only significant pore type in water saturated compacted bentonite is interlayers, by which I mean pores where the exchangeable cations reside (together with any other dissolved species). From this perspective it naturally follows that a homogeneous view is a suitable starting point for modeling compacted bentonite. I have presented, used, and discussed the homogeneous mixture model in many places on the blog, the main sources being
For reasons I can’t get my head around, a homogeneous view of
compacted bentonite is not the mainstream in contemporary
bentonite research. Instead we are stuck with
“the mainstream view”, which postulates several distinctly
different pore structures within the bentonite; in particular, the
mainstream view uses a bulk water phase as a starting point and also
distinguishes between “outer” and “inner” basal surfaces. Electric
double layers are assumed to only exist on “outer” surfaces, while
the function of the “inner” basal surfaces is mostly shrouded in
mystery.
On the blog I have also presented plenty of experimental support for a
homogeneous view. A main argument is that the conditions for swelling
pressure — the most profound feature of bentonite in equilibrium with an external solution — are essentially fulfilled automatically in the
homogeneous mixture model. The mainstream view, in contrast, requires
handling of the seemingly contradictory situation of having swelling
pressure while the water chemical potential is supposedly restored
without pressurization. Proponents of the mainstream view often deal
with this by simply ignoring swelling phenomena altogether.
I have also on the blog dissected several studies that argue for a
non-homogeneous view, but that actually provide evidence for the
opposite when examined more carefully. Consider in particular:
By systematically varying background concentration, material, and diffusing tracer, Glaus et al. (2007) clearly demonstrate, not only that the exchangeable cations are mobile, but that they dominate the flux in through-diffusion tests in highly compacted montmorillonite. While this certainly is an argument for that compacted bentonite is homogeneously structured, Glaus et al. (2007) still analyze their results from the perspective of the mainstream view, and do not — in my view — fully conclude what their results imply.
In particular they postulate the presence of an interlayer domain and a “free pore water” domain, and write for the “total” flux1 (their eq. 3)
where \(J_\mathrm{il}\) is a presumed diffusive flux in the interlayer domain and \(J_\mathrm{pw}\) is the presumed diffusive flux in the “free pore water” domain.
Their subsequent analysis shows that the measured flux in montmorillonite scales as
where \(C_\mathrm{bkg.}\) is the concentration of the background electrolyte (NaClO4), and \(Z\) is the charge number of the diffusing tracer (\(Z = 1\) for sodium and \(Z=2\) for strontium). Moreover, by considering ion exchange equilibrium, Glaus et al. (2007) show that also \(J_\mathrm{il}\) is expected to scale according to eq. 2. As they also confirm that this scaling behavior is not observed in systems without interlayer pores (kaolinite), they could have confidently concluded that their results imply that interlayers are the only significant pore structure in montmorillonite at these densities (as the title suggests).
Unfortunately, the discussion part of the article is considerably more tentative, focusing mainly on “interpretations” of the resulting flux
The present work shows that the interpretation of cation diffusion experiments in highly compacted swelling clays in terms of the concentration gradient in the aqueous phase may result in a nonsensical dependence of the effective diffusion coefficients on the salt concentration in the external aqueous phase. An alternative interpretation using an effective diffusion coefficient in the interlayer water (\(D_\mathrm{il}\)), being independent of the external salt concentration, with a corresponding concentration gradient in the interlayer water is more consistent with the experimental observations.
and the article ends on a quite apologetic note
The proposed interpretation should in turn not be blindly applied to
other experimental conditions. Diffusion of cations via the free
pore water may become increasingly important in swelling clays with
lower degrees of compaction or in clays in which the interlayer gel
pores are not that adjacent as they are in compacted
montmorillonite. In such cases, the assumption of
\(J_\mathrm{tot} \cong J_\mathrm{il}\) may no longer hold, and a
double-porous diffusion model would have to be applied in such
cases. The present concept may also reach its limits when dealing
with cations that rather sorb by surface complexation than by ion
exchange. Further work is therefore planned to extend the
investigations to such systems.
Given that the mainstream view to this day continues to be the default approach, one may think that this “further work” did show some convincing evidence for e.g. “diffusion of cations via the free pore water” at lower density. But what has actually been shown is that the “assumption of \(J_\mathrm{tot} \cong J_\mathrm{il}\)“ continues to be true for lower density!
Before we look at the additional results, we summarize the findings of
Glaus et al. (2007).
Findings in Glaus et al. (2007)
In the following we will consider the so-called “effective diffusion
coefficient”, here strictly defined as the experimental parameter
where \(j_\mathrm{ss}\) denotes the steady-state flux when an external
tracer concentration difference \(\Delta c^\mathrm{ext}\) is maintained
across a bentonite sample of length \(L\). We have
discussed through-diffusion and
the role of \(D_e\) in
many places on the blog, but in the present discussion we simply
view \(D_e\) as a normalized version the steady-state flux.
Note that we are required to compare diffusive fluxes in
different montmorillonite samples (an alternative test protocol
is suggested below). \(D_e\) varies both due to varying background
concentration (which is our object of study) and due to the variation
of different samples. It is thus crucial to minimize the latter type
of variation. This should be done (I suppose) by employing as
identical preparation protocols as possible. We will get back to this
complication of sorting out signal from noise as we comment the
results.
Glaus et al. (2007) present their results in diagrams where the logarithm of the evaluated quantities (diffusion parameters) is plotted against background concentration. This is of course convenient, as e.g. \(D_e\) can be expected to vary by two orders of magnitude as the background concentration is varied between 0.01 M and 1.0 M. But to remind ourselves what the actual dependency looks like between the normalized steady-state flux and background concentration, I will here insist on plotting the results in lin-lin diagrams.
The results for sodium in Glaus et al. (2007) plotted in lin-lin
diagrams, look like this (the data is the same in these three
diagrams)
We see that the data complies with the scaling law (eq. 2) and is quite well constrained (click on pictures to enlarge). \(D_e\) is evaluated in two ways in Glaus et al. (2007): by examining the breakthrough curve, and by examining the internal tracer profile at test termination. These methods of evaluation give more or less identical results, with the exception of the test performed at 0.01 M background concentration. In this low concentration limit, the confining filters increasingly restrict the flux, making it difficult to extract actual clay transport parameters. We have discussed this issue (and this particular study) at length in a previous blog post.
Even with the problem of accurately measuring \(D_e\) at the lowest background concentration, the results clearly demonstrate the behavior of a homogeneous system (eq. 2): e.g., \(D_e\) undoubtedly increases by a factor of approximately 10 when the background concentration is lowered from 1.0 M to 0.1 M.
The data for strontium in Glaus et al. (2007) only covers the
background concentration interval 0.5 M — 1.0 M, and is consequently
less constrained, as seen here
This data also has the peculiarity that the diffusivity of samples of length 5.4 mm is almost twice as large as for samples of length 10.4 mm. This clearly demonstrates how sample preparation becomes crucial when conducting these types of tests. In the plots above, I have allowed myself to treat samples of different length separately (Glaus et al. (2007) use average values). It is clear from the data, that also strontium is compatible with the scaling law of eq. 2. In particular, it can be distinguished that sodium and strontium have different dependencies.
The take away message from these results is clear: montmorillonite at this density (1950 kg/m3) behaves as a homogeneous system and shows no indication of containing additional pore structures.
Glaus et al. (2013) and NTB-17-12
After the publication of Glaus et al. (2007), corresponding results for lower densities has been presented. Glaus et al. (2013) — which is mostly recognized for demonstrating the seeming “uphill” diffusion effect — also contains measured \(D_e\) of sodium as a function of background concentration in conventional through-diffusion tests, both for density 1600 kg/m3 and 1300 kg/m3. These results are also published in more detail,2 together with new strontium results, in the NAGRA technical report NTB-17-12. We therefore look at these two publications together.
The additional data for sodium is here compared with the results from
Glaus et al. (2007)
For some of the additional tests, both through- and out-diffusion were performed. These points are labelled “TD” and “OD”, respectively, in the diagrams. We see that even for density as low as 1300 kg/m3, the data complies with the behavior of a homogeneous system (eq. 2) and is quite well constrained; in particular, there is nothing in the data for 1300 kg/m3 that suggests that these systems behave principally different than the 1950 kg/m3 samples.
For the system at 1300 kg/m3 and background concentration 0.1 M, two different values of \(D_e\) are presented in NTB-17-12. Only the lower of these values (\(7.0\cdot 10^{-10}\) m2/s) was published in Glaus et al. (2013), but NTB-17-12 presents a continued analysis that includes filter resistance, giving the value of \(D_e\) presented in the diagram. I think this is quite interesting, as the tests made at 0.1 M used “flushed” filters in order to minimize filter resistance. Apparently, filter resistance is still influential and it is not that easy to “design away” this problem.
NTB-17-12 also presents measured values of \(D_e\) for strontium under similar conditions (1300 — 1900 kg/m3, 0.1 — 1.0 M NaClO4 background), and are here compared with the earlier results
Although it naturally contains some scatter, we note that the additional data for ~1900 kg/m3 strengthens the earlier conclusion that also strontium scales in accordance with eq. 2. And just as for sodium, we see that the behavior does not qualitatively change, even for densities as low as 1300 kg/m3.
In the above diagrams are plotted single values for \(D_e\) for strontium at the lowest background concentration (0.1 M). It should be noted that these are burdened with large uncertainties as the transport restriction of the confining filters is severe; in NTB-17-12 are presented a whole set of simulations of the underlying flux evolution and concentration profiles with variations of the filter transport parameters. It is thus very clear that the problem of eliminating transport restrictions at the sample interfaces are not easy to completely eliminate. This is not surprising, as the theory suggests that \(D_e\) increases without limit with decreasing background concentration. Note that this behavior is strongly enhanced for divalent strontium; the measured values are many times larger than the corresponding diffusivity in bulk water (\(0.79\cdot 10^{-9}\) m2/s).
Even if the value of \(D_e\) is quite uncertain at the lowest background concentration, the mere observation that filter diffusivity strongly influence the process is, in a sense, itself a confirmation that the system still is governed by the behavior of interlayers.
The picture is quite clear from these findings: the combined results of Glaus et al. (2007), Glaus et al. (2013) and NTB-17-12 validates a homogeneous view of compacted bentonite, at essentially any relevant density!
The curious case of Bestel et al. (2018)
Bestel et al. (2018) further examine how \(D_e\) for sodium varies with background concentration. This publication shares some of the same authors with the previous studies, and presents additional measurements of \(D_e\) for sodium in essentially identical systems (similar preparation protocols, “Milos” montmorillonite, NaClO4 background electrolyte, flushed filters). Given the substantial evidence for homogeneous behavior collected in the publications discussed above, I find the conclusions of Bestel et al. (2018) rather odd.
Bestel et al. (2018) perform subsequent measurements of the steady-state flux in the same samples at different temperatures. The dependency of \(D_e\) on background concentration, however, looks essentially the same for each temperature, and — just as Bestel et al. (2018) — we here focus mainly on the results for 25 \(^\circ\mathrm{C}\). This data looks like this3
In their analysis, Bestel et al. (2018) include the results from Glaus et al. (2007) and Glaus et al. (2013), but treat them separately. They consequently conclude implicitly that, although the earlier studies found that \(D_e\) depends on background concentration in accordance with eq. 2, the new results show a different behavior. Specifically, they conclude that \(D_e\) scale with background concentration as \(C_\mathrm{bkg}^{-0.52}\) for density 1300 kg/m3 and as \(C_\mathrm{bkg}^{-0.76}\) for density 1600 kg/m3. Bestel et al. (2018) write
The results obtained in the present work for a broad variety of bulk
dry densities of Na-montmorillonite and concentrations of the
background electrolyte, give clear evidence that the equilibrium
distribution of cations between the clay phase and the external
aqueous phase is the main parameter influencing the observed overall
diffusive fluxes of cations. Whether the observed overall diffusive
fluxes are described by a physical subdivision of the pore space
into domains containing different species (e.g. the model proposed
in Appelo and Wersin (2007) or Bourg et al. (2007)), or whether
they are the result of the concentration gradients of such species
in a single type of pore (e.g. the model proposed by Birgersson and
Karnland (2009)), cannot be decided unambiguously from the available
data — notably because of the wide similarity of the model
predictions and because of some internal inconsistencies in the
experimental data. Both types of models would require some
adjustments in order to fully match the data. The diffusion data of
\(^{22}\mathrm{Na}^+\) can equally be described by a surface diffusion
model with a reduced, but non-zero mobility of sorbed cations,
similar to the median value determined in Gimmi and Kosakowski
(2011).
I think this is a problematic way of arguing and presenting data.
The data obviously has scatter
To begin with, why are the results from this study and the ones from Glaus et al. (2007) and Glaus et al. (2013) treated separately? When treated separately — according to Bestel et al. (2018) — these results are vaguely supposed to be incompatible: the dependence of \(D_e\) either comply with eq. 2 or it does not. I think that the appropriate thing to do is to discuss possible causes for why the new results supposedly differ from the earlier ones. As we have made clear above, all factors that determine \(D_e\) are not fully controlled in tests like these (e.g, what causes the difference in diffusivity for strontium in 5.4 mm and 10.4 mm samples, respectively, in Glaus et al. (2007)?). We have also seen that it is difficult to make accurate measurements at low enough background concentration, even with flushed filters.
Look e.g. at the specific values of \(D_e\) at background concentrations 1.0 and 0.1 M, respectively, in NTB-17-12 and Bestel et al. (2018) (unit is m2/s).
Under ideal conditions, these values would not differ for the same conditions in the two studies. The scatter of these values is moreover quite random, e.g. one study does not have values that are systematically larger than in the other. In Bestel et al. (2018) we also see that the mere disturbance of a sample in form of a temperature pulse may alter the diffusivity significantly (temperature is first increased in steps from 25 \(^\circ\mathrm{C}\) to 80 \(^\circ\mathrm{C}\), then decreased in steps to 0 \(^\circ\mathrm{C}\), and finally increased again to 25 \(^\circ\mathrm{C}\)). In e.g. one sample of density 1600 kg/m3 and background concentration 0.1 M is reported \(D_e = 3.4\cdot 10^{-10}\) m2/s at 25 \(^\circ\mathrm{C}\) before the conducted temperature changes, and \(2.3\cdot 10^{-10}\) m2/s after. One should also consider that the samples are not prepared equally, as they are saturated directly with the corresponding background solution. (This is also true for the previous studies.) Could this cause differences in diffusivity?
Bestel et al. (2018) should thus either argue for why the new results
are more accurate (or why the results of Glaus et al. (2007, 2013)
are less accurate) or treat the data from all studies in accumulation
and admit substantial experimental uncertainty. My impression is that
Bestel et al. (2018) make a little of both.
The data still complies with a homogeneous view
Looking at the aggregated sodium data, a somewhat different picture
emerges
Here is also included a model labelled “Full Donnan”, which takes into account the excess salt that is expected to enter the interlayers. For all other samples we have discussed, this contribution is only minor and can be neglected, and this assumption underlies eq. 2. For the sample of density 1300 kg/m3 with background concentration 5.0 M, however, the excess salt is not negligible and must be included in the analysis of the behavior of a homogeneous system (the deviation from eq. 2 is seen to become significant around 1.0 M background concentration). Bestel et al. (2018) actually present a full Donnan calculation for the excess salt, but, for unknown reasons, do not compare it directly with the experimental results (it is plotted in a separate diagram next to the data).
For 1300 kg/m3, I would claim that the “Full Donnan” model fits better to the accumulated data than the scaling law suggested in Bestel et al. (2018) (exponent \(-0.52\)). For 1600 kg/m3, the suggested scaling law (exponent \(-0.76\)) indeed fits better to the data than eq. 2, but the data is not that well constrained. To use this singular result to argue for a non-homogeneous bentonite structure basically boils down to claiming that the values measured at 0.1 M — a concentration range that is documented to be difficult to measure accurately — could not possibly be underestimated by, say, 50% (while also ignoring all other results).
If we also consider the results for strontium presented in NTB-17-12, I mean that the only reasonable conclusion that Bestel et al. (2018) can draw is that the results comply with a homogeneous bentonite structure.
Additional model components should not be motivated
solely by the ability of a model to be fitted to some arbitrary
data
A major motivation for measuring how \(D_e\) depends on background concentration at lower densities, according to Glaus (2007), is that “the assumption of \(J_\mathrm{tot} \cong J_\mathrm{il}\) may no longer hold”. What (I mean) has been demonstrated in the subsequent studies is that this assumption actually does hold. In particular, from the aggregated data it is not possible to claim that the behavior of \(D_e\) is qualitatively different at 1950 kg/m3 and 1300 kg/m3. Thus, there is no valid justification for introducing more complex model components. Moreover, introducing e.g. a bulk water phase causes fundamental conflicts with the description of other well-established properties of these systems, particularly swelling pressure. Adding such components merely to improve agreement with a specific dataset, while ignoring their broader implications, undermines the model’s overall coherence and validity. The data cannot“equally be described by a surface diffusion model”.
What does some alternative model actually predict?
Eq. 2 (or a full Donnan calculation) is a clean statement of the expected behavior of a homogeneous system (based on how interlayers function). If actual deviations from this behavior could be established we may conclude that a homogeneous description is not sufficient. However, any arbitrary deviation from eq. 2 does not automatically validate any specific alternative model. Validating a model requires that we can experimentally reproduce some of its non-trivial predictions. Bestel et al. (2018) don’t discuss what the exponents \(-0.52\) and \(-0.76\) are suppose to represent.
Note also that the arbitrary exponent \(-0.52\) is inferred by fitting to the data at 5.0 M background concentration. But we saw above that a full Donnan calculation within the homogeneous view actually explains the behavior in this concentration limit (Bestel et al. (2018) show this!). We have thus every reason to believe that the exponent \(-0.52\) is just spurious and do not represent some actual physical mechanisms.
A suggestion for how to preferably conduct these types of tests
The discussed studies are enough to convince me that cation tracer
diffusion behave in accordance with a homogeneous bentonite view at
any relevant density.
It is however also clear that the full variation of \(D_e\) in these
tests is caused by more factors than just background concentration and
density. To eliminate as much as possible of this scatter — and thus
to more accurately determine the dependence of background
concentration on \(D_e\) — I suggest the following test protocol.
Measure tracer flux at several background concentrations in the same sample.
This would eliminate both the unavoidable (small) variation in density between different samples as well as several unknown factors that determine the exact value of diffusivity (these may e.g. be related to variation in material or equipment and to sample handling)
Prepare samples by saturating them all with the same low concentration solution (e.g. 0.05 M).
To me it seems reasonable that the way samples saturate may influence the resulting detailed structure and thus the diffusivity. Saturating all samples in the same manner with the same solution will minimize variations from such effects.
Keep temperature constant.
I don’t think this is a crucial factor, but we see in Bestel et al. (2018) that larger temperature pulses may significantly alter the diffusivity.
Increase background concentration in steps and record the steady-state flux at each concentration.
I think a good range may be between 0.2 M and 1.0 M. For a homogeneous system, this corresponds to a variation in \(D_e\) by a factor 5 for monovalent and 25 for divalent cations.5 At the same time, the problem of filter transport resistance can hopefully be kept under control.
Decrease the background concentration (perhaps in steps) back to the first concentration where steady-state flux was measured.
Measure steady-state flux again and assert that no significant change in \(D_e\) has occurred as a consequence of the disturbance introduced by the background concentration pulse.
Final thoughts
The only reasonable conclusion to draw from the studies we have looked
at is that the behavior of cation tracer diffusion indicates a
relatively homogeneous structure, dominated by interlayers, in any
relevant bentonite system. Despite this, the contemporary scientific
bentonite literature is crammed with non-homogeneous descriptions of
compacted bentonite, centered around a bulk water phase (the
“mainstream view”). As we have seen here, this can even be the case
for studies that provide evidence for homogeneity.
What I find most frustrating is that interlayer effects often are viewed as some additional feature to be handled in specific cases. In reality, virtually all experimental findings (diffusion, swelling pressure, temperature response, Donnan effects, fluid flow, hyperfiltration, …) indicate that the behavior of compacted bentonite is fully governed by interlayers. The question is not if a presumed bulk water phase may dominate under certain conditions, but if such a phase is at all relevant. I want to emphasize this point: up until this day, no convincing evidence has ever been presented that compacted bentonite contains significant amounts of bulk water.
Even if the structure becomes more complex at lower densities, a
homogeneous model centered around interlayers guarantees to cover at
least some aspects of the system. On the contrary — if the goal is
process understanding — most experimental evidence rules out
bentonite models that assume a bulk water phase.
[2] As
far as I can see, these tests were done in duplicates for Na
diffusion with background concentrations 0.5 M and 1.0 M, and the
the numbers reported in Glaus et al. (2013) are averages.
[3] Bestel et
al. (2018) use a normalization scheme in their analysis that
involves corresponding measured water diffusivities and parameters
from “Archie’s law” (note, it is the
quotation marks version of the law). I think this handling makes
the presented results less transparent, and here we use the actual
reported values of \(D_e\).
[4] These are only values from the first phase at 25 \(^\circ\mathrm{C}\).
[5] I assume that measurements are being made in pure Na-montmorillonite.