Minjun
Yang‡
a,
Ling
Tan‡
a,
Christopher
Batchelor-McAuley
b and
Richard G.
Compton
*a
aPhysical and Theoretical Chemistry Laboratory, Department of Chemistry, University of Oxford, South Parks Road, Oxford, UK. E-mail: Richard.Compton@chem.ox.ac.uk
bThe School of Chemistry, Trinity College Dublin, The University of Dublin. College Green, Dublin 2, Ireland
First published on 10th January 2024
Quantification of calcite dissolution underpins climate and oceanographic modelling. We report the factors controlling the rate at which individual crystals of calcite dissolved. Clear, generic criteria based on the change of calcite particle dimensions measured microscopically with time are established to indicate if dissolution occurs under kinetic or thermodynamic control. The dissolution of calcite crystals into water is unambiguously revealed to be under thermodynamic control such that the rate at which the crystal dissolved is controlled by the rate of diffusion of ions from a saturated surface layer adjacent to the calcite surface. As such the dissolution rate is controlled by the true stoichiometric solubility product which is inferred from the microscopic measurement as a function of the concentration of NaCl. Comparison with accepted literature values shows that the role of ion pairing at high ionic strengths as in seawater, specifically that of CaCO3 and other ion pairs, exerts a significant influence since these equilibria control the amount of dissolved calcium and carbonate ions in the later of solution immediately adjacent to the solid.
The saturation state of calcite depends on a knowledge of the true solubility product defined in terms of the activities of the ions. However, in the case of seawater it has been usual to work with the stoichiometric solubility constant defined by
K0sp = [Ca2+][CO32−] | (1) |
K0sp,apparent = ∑[Ca2+]∑[CO32−] | (2) |
The stoichiometric solubility product controls the maximum rate at which calcite can dissolve since this corresponds to the rate at which ions diffuse into bulk solution from the solid–liquid interface under conditions where the interfacial concentration is pinned at the maximum level consistent with the value of K0sp. Under other conditions, notably for ultra-small particles the rate can be slower and reflects a surface kinetic controlled dissolution.1 Other than particle size,12 the pH and salinity of seawater,13 and the adsorption of surface-active components in seawater, notably magnesium ions,14–16 are thought to impact the rate of calcite dissolution.
Typical seawater contains a total calcium (∑[Ca2+]) concentration of approximately 10 mM, a total carbonate ions (∑[CO32−]) of 0.2 mM and a total magnesium concentration at a relatively large excess of 55 mM.9,17 Under seawater conditions carbonate ion is known to form ion pairs18 most notably with Mg, Ca and Na cations,17,19 resulting in merely 8% of the total carbonate existing as free ions.17 It is evident that the ionic composition of seawater plays an integral role in the calcium carbonate chemistry not only at the heterogeneous calcite–water interface20,21 but also chemically in the solution phase. Note that more recent studies observed the recession/growth of pristine surface and kink sites of calcite surfaces using atomic force microscopes allows mechanistic insights into particle dissolution/crystallisation at the nanoscale level with or without calcite dissolution/growth inhibitors to be inferred.15,22–27 Most notably, the dissolution step velocities of obtuse 〈48〉 and acute 〈
41〉 sites on a pristine (104) calcite surface were found to reduced by 97% and 18% with the addition of 0.8 mM Mg2+, respectively.15
In contrast the work in this paper concerns the overall rate of macroscopic dissolution of micron-sized calcite crystals as entire single entities. This is different to atomic force microscope studies where the latter necessarily focuses on the evolving recess of surfaces, steps and kink sites on pristine crystalline facets. The rate of dissolution of the crystal (particle) as a holistic entity is perplexed by the intertwined effect of the surface kinetics and rate of mass-transport of solute to and from the crystal surfaces. In the limiting cases, the overall rate of particle dissolution can either be limited by the rate of surface processes (surface kinetics) or the rate of mass-transport of materials (thermodynamic dissolution). Note that the intertwined effects of surface kinetics and mass-transport are commonly seen in reaction kinetics at interfaces such as, but not limited to, crystal precipitation28 and dissolution,29 biosensors30 and electrochemistry.31,32
A discussion of the limiting cases is given in ESI Section 3† and below where it is shown that the variation of the particle dimensions with time shows generically different behavior for the two cases reflecting either a constant flux of dissolving solid (surface kinetic control) or dissolution controlled by the rate of diffusion of the dissolved solid away from the crystal as happens when the concentration local to the dissolving surface is pinned, for example by the solubility of the solid, in which case the solubility product controls the local concentration and hence indirectly the rate of dissolution. In the following we exploit the generic probe for fingerprinting and hence resolving the two kinetic limits of surface and thermodynamic control. In the thermodynamic limit it should be stressed that the physical process controlling the rate is that of diffusion of dissolved solid into the bulk of solution but that this reflects the prevailing concentration gradients adjacent to the solid and these in turn reflect the pinned concentration(s) at the surface as dictated by the solubility product. In this limit the rate at which dissolved solute diffuses into bulk is matched by an equal (net) rate of dissolution of the crystal so maintaining the saturated layer at the dissolving interface.
The distinction between surface and thermodynamic dissolution in the context of calcite dissolution has proved challenging with a diversity of views expressed.1 The terms “surface kinetics” and “thermodynamic dissolution” in the context of this work are discussed in ESI Section 3.† In our opinion this partly arises since the approaches used have been to monitor the net release/consumption of calcium and/or carbonate ions in the solution phase – an inherently indirect method. Driven by the need for unambiguous mechanistic distinction coupled with the fact that the dissolution/precipitation process is intimately linked to the evaluation of K0sp, in this paper we use a direct method for measuring the dissolution rate and show that the rate of change of the size of calcite particles with time inferred microscopically via recording the rate of recession of the particle interface gives the sought clear, unambiguous mechanistic distinction and allows the quantification of the real, stoichiometric K0sp of calcite prompting reconsideration of Mucci's approach. The method is extended to consider retarded dissolution in the presence of Mg2+ ions at concentrations similar to those encountered in seawater with a simple model used to explain all observations.19
![]() | (3) |
![]() | (4) |
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Fig. 1 Single particle dissolution. (A) An illustration of the dissolution of a single calcite particle on a plate and the observed projection area of the particle as a function of time viewed top-down. (B) Optical images of the dissolution of a representative calcite particle. The top row shows raw images and the bottom row shows the same images after thresholding. (C) Projected areas, A, and (D) particle lengths, L, of three calcite particles are plotted as a function of time in a solution containing 0.7 M NaCl. The particle length was calculated from ![]() |
Note that, in the limiting case of thermodynamic dissolution, which is discussed in detail in more ESI Section 3,† the interfacial concentration of the solute is a constant pinned by the thermodynamic solubility. A revaluation of the right-hand side of eqn (3) and (4) reveals that, under thermodynamic dissolution, is a constant whereas
becomes increasingly more negative as the particle size reduces during dissolution. Note that the opposite is true if the dissolution is limited by the surface kinetics. The dissolution pattern as described by eqn (3) and (4) provides a generic mechanistic distinction for the dissolution of calcite single-particles analysed first in the absence of inhibitors and, second, with sea-level quantities of Mg2+.
Fig. 1C shows that the rate of change in the projection area, A, displays a strong linear dependency on time (gradient = −2.1 × 10−14 m2 s−1, Parson's R = −0.99), which is not the case for particle length (Fig. 1D). ESI Section 4† shows more examples of transients analysed in ionic strengths ranging from 0 mM to 1 M NaCl(aq) with similar observations in respect of the variation of length and area with time. This strongly evidences calcite dissolution occurring at the thermodynamic limit; the rate of calcite dissolution and precipitation at the particle–solution interface is fast allowing local equilibrium and the overall rate of dissolution is dictated by how quickly the diffusion-limiting Ca2+ flux can diffuse down the concentration gradient away from the particle–solution interface into the bulk solution.
Fig. 2A shows the dissolution rate, , of calcite single-particles measured experimentally in aqueous solutions containing exclusively NaCl(aq) reported by Fan et al.33 As can be seen, by increasing the overall ionic strength of the solution by 3 orders of magnitude, from 0.1 mM to 1 M, the rate of particle dissolution was seen to increase ca. three-fold from 1.6 × 10−14 m2 s−1 to 4.5 × 10−14 m2 s−1. At low ionic strengths, I < 10 mM, the data reported by Fan et al. agrees with the predicted thermodynamic rate of calcite dissolution using values reported by Mucci(6) but at higher ionic strengths, I > 10 mM, significant deviations were seen.33 Below we show this apparent paradox arises because of the neglect of ion pairing.
The calcite dissolution equilibrium is expressed in terms of free ions in solution and ion pairs, CaCO30(aq) and CaHCO3+(aq)
![]() | (5) |
![]() | (6) |
![]() | (7) |
Noting that the stoichiometric ion pair association constants defined herein, Kip,1 and Kip,2, are in terms of concentration, not activities. As the ionic strength of an aqueous medium increases, the effect of the ion pairing effect between calcium and carbonate ions becomes non-negligible.19 Separate from the calcite dissolution equilibrium, calcium binds with hydroxide to form
![]() | (8) |
At 0.7 M ionic strength, the stoichiometric ion pair association constants, Kip,1 and Kip,2 has a reported value of 162 M−1 and 1.96 M−1, respectively.17 A Kip,3 value of 3.3 M−1 was calculated using the PHREEQC software36 by accounting for the activity coefficients of species involved at 0.7 M ionic strength via the Davies equation. In the next section we first calculate the effect of ion pairings in the calcite single-particle experiments before discussing the extent of ion pairings in Mucci's experiments.
c = ∑[Ca2+]0 = [Ca2+]0 + [CaCO30]0 + [CaHCO3+]0 + [CaOH+]0 | (9) |
Using the experimentally determined ∑[Ca2+]0, the apparent stoichiometric solubility product is inferred via modelling (K0sp,apparent = ∑[Ca2+]∑[CO32−]) and ∑[CO32−] are obtained and shown in Table 1 by solving the CaCO3 and carbonate equilibrium for the given ionic strength and temperature recognising that the solid CaCO3 dissolution releases both calcium and carbonate ions in equal amounts.33 Separately, to investigate the effects of ion pairing, the CaCO3 and carbonate equilibrium, fully described in ESI section 5,† is solved simultaneously additionally with the above ion pairing equilibria (eqn (5), (6) and (8)) to infer the fraction of the total dissolved solute existing as free ions, Ca2+(aq), CO32−(aq), and ion pairs assuming that the ion-pairing equilibria are fast and not rate determining.
Ionic strength (mM) | K0sp,apparent (M2) | Total concentrations (including ion pairing, M) | Concentrations of free ions and ion pairs (M) | |||||
---|---|---|---|---|---|---|---|---|
∑[Ca2+]0 | ∑[CO32−]0 | [Ca2+]0 | [CO32−]0 | [CaCO30]0 | [CaHCO3+]0 | [CaOH+]0 | ||
0.1 | 3.9 × 10−9 | 1.3 × 10−4 | 2.9 × 10−5 | 1.2 × 10−4 | 2.9 × 10−5 | 5.7 × 10−7 | 2.6 × 10−8 | 1.0 × 10−5 |
160 | 2.6 × 10−8 | 2.2 × 10−4 | 1.2 × 10−4 | 2.0 × 10−4 | 1.2 × 10−4 | 3.7 × 10−6 | 4.0 × 10−8 | 1.6 × 10−5 |
300 | 3.0 × 10−8 | 2.3 × 10−4 | 1.3 × 10−4 | 2.1 × 10−4 | 1.3 × 10−4 | 4.4 × 10−6 | 4.2 × 10−8 | 1.6 × 10−5 |
684.5 | 3.4 × 10−8 | 2.4 × 10−4 | 1.4 × 10−4 | 2.2 × 10−4 | 1.4 × 10−4 | 4.9 × 10−6 | 4.3 × 10−8 | 1.7 × 10−5 |
1000 | 8.5 × 10−8 | 3.5 × 10−4 | 2.4 × 10−4 | 3.2 × 10−4 | 2.3 × 10−4 | 1.2 × 10−5 | 7.0 × 10−8 | 2.9 × 10−5 |
The right-hand side of Table 1 tabulates the concentrations of the ions that exist as free ions and as ion pairs where
∑[CO32−]0 = [CO32−]0 + [CaCO30]0 | (10) |
It is evident from Table 1 that the extent of ion pairing in the calcite single-particle dissolution experiment reported by Fan et al. is negligible. This is because the bulk solution contains only NaCl ions but no calcium other than that resulting from calcite dissolution. Fig. 2B plots the values of K0sp,apparent and K0sp values of calcite inferred from data reported by Fan et al. As can be seen, the effect of ion pairing can be essentially ignored in those experiments since K0sp,apparent ≈ K0sp. Next, we turn to investigate the extent of ion pairing in Mucci's ‘long-term’ calcite equilibrium experiments in natural seawater and we will discuss how this might affect the true stoichiometric solubility product of calcite, K0sp.
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Fig. 2 Dissolution of calcite single-particles. (A) Experimentally measured rate of change in the projection area of CaCO3 microparticles with time using aqueous solutions containing variable concentrations of NaCl. Data is obtained from ref. 33, an open-access article in ACS Measurement Science Au. (B) The stoichiometric solubility product of calcite as a function of ionic strength in NaCl solution and in seawater, with and without ion pair correction. Black squares shows the calcite solubility product in NaCl solutions using data reported by Fan et al.33 (no ion pair correction). Blue triangles shows the true calcite solubility product in NaCl after ion pair correction (reanalysed in this work). Green rhombus is the calcite solubility product reported by Mucci in seawater (without ion pair correction). Red cross is the true stoichiometric solubility product of calcite in seawater after ion pair correction (reanalysed in this work). (C) Pie charts showing the calculation of the percentage of the speciation of (i) Ca2+ and (ii) CO32− in natural seawater as inferred by the analysis (see text) of the data reported by Mucci. |
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![]() | (12) |
![]() | (13) |
![]() | (14) |
Heretofore, the results hint at the importance of considering, and the need to correct for ion-pairing since any changes in the chemical composition, in seawater or other media, will have an impact on the value of K0sp,apparent. Using the ion-pair corrected true stoichiometric of calcite in seawater calculated in this study (5.4 × 10−8 M2) and assuming that the concentration of Ca2+ is in large excess (10 mM in surface waters) the concentration of CO32− free ions needed to reach saturation (Ω = 1) is 5.4 μM. In natural seawater the total carbonate concentration is reported to be in the range of 50–250 μmol kg−1,39,40 the carbonate free ions in seawater, however, is approximately 7.99% of the total concentration17,38 which gives rise to a range of 4–20 μmol kg−1. This is entirely consistent with the claim that the surface of our ocean is saturated/supersaturated with respect to calcite, however, we note the literature is often unclear if free or total ion concentrations are used in the calculation.40–45
Further, we recognised that the true saturation of calcium carbonate can rigorously only be asserted relative to a true stoichiometric solubility product, in seawater or in a well-defined NaCl aqueous solution, or anything in between. Of the many components in seawater, however, one of considerable impact is Mg2+ cations where it is important to note that in a sample of solid CaCO3 particles equilibrated with seawater-type media, significant amounts of magnesite (MgCO3) have been detected even after just 7 days of exposure.46 Clearly assertions of ‘supersaturation’ require a precise knowledge of the composition of the solid phase controlling the equilibrium! Given the apparent role of Mg2+, in the following, we explore the role of this ion in the dissolution of CaCO3.
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Fig. 3 Calcite dissolution in the presence of magnesium. (A) Projected area and (B) side length of 5 different dissolving calcite particles plotted against time. The calcite particles were exposed to 10 mM Mg(NO3)2·6H2O solution to which. KNO3 was added to make the total ionic strength of the solution equal to 0.3 M. Different colours relate to different particles. (C) The average rate of dissolution of calcite as a function of magnesium concentration. The overall ionic strength of the aqueous solution is 0.3 M with the addition of a suitable amounts of KNO3. The dashed red line corresponds to the value in the absence of magnesium. (D) Plot of apparent stoichiometric solubility product inferred from single particle dissolution measurements against ![]() |
Fig. 3C shows the average rate of change in projection area, , of calcite particles measured at different concentrations of Mg2+. The rate is reduced by approximately 6-fold with the addition of Mg2+ from 2.9 × 10−14 m2 s−1 to a limiting value of approximately 6.5 × 10−15 m2 s−1 at [Mg2+] of 25–100 mM. Interestingly, the fact that the rate does not decrease to zero but, rather, to a non-zero plateau suggests that the different calcite sites are affected differently by the magnesium adsorption as suggested elsewhere.15 An examination of the particle-size evolution of the calcite particles, the transients of which are shown in ESI Section 7,† reveals that
remains linear with time whilst
becomes increasingly non-linear and more steep over the dissolution duration (ca. ∼100 minutes). This indicates that, despite the presence of Mg2+ showing an unambiguous sign of rate reduction, the dissolution remains to proceed at the limit corresponding to a fixed surface concentration rather than a constant surface flux. This is a strong indication, as discussed above, that the rate-determining step is the diffusion of ions away from the crystal. The overall rate of the dissolution of the crystal is thus controlled by the constant composition in the adjacent layer.
The dotted line in Fig. 3C shows the dissolution rate of calcite particles, in the form of , reported separately by Fan et al. in 0.3 M NaCl solutions. However, increasing the concentration of magnesium ions from 0 to 53 mM is reported to increase the apparent solubility product of calcite (∑[Ca2+]∑[CO32−]) by ca. a factor of 1.5.47 This is due to the formation of magnesium (bi)carbonate ion pairs which encourages calcite dissolution. Therefore, the effect of magnesium adsorption has on slowing the rate of calcite dissolution may be slightly larger than that appears when referenced against the rate at 0.3 M NaCl solution (absent of Mg2+) as shown in Fig. 3C. Note that the variation of the error bars shown in Fig. 3C is likely due to an intertwined effect of the slight changes of particle geometry from particle to particle along with a slow drift in the optical focus away of the particle plane as the particle shrinks. A periodic readjustment of optical focus is usually required during the experiment.
Hereto, it is clear that the auto dissolution of micron sized calcite particles, in 0.3 M ionic strength aqueous solutions both in the absence of, and in the presence of, Mg2+, occurs under conditions where the concentration of the dissolved material at the solid surface is constant, at least for most of the duration of dissolution. Accordingly, the question arises as to what is the interfacial equilibrium concentration of Ca2+ on the CaCO3(s) surface in the presence of Mg2+? And why might this be fixed? In the absence of Mg2+ we interpreted this above as indicating that the surface concentration is pinned by the solubility product of pure calcite.
Noting literature reports of significant Mg2+ adsorption on calcite surfaces and that this is approximately Langmuirian14 we suggest that the net interfacial dissolution rate can be described by the rate equation
flux (mol cm−2 s−1) = kf(1 − θMg) − kb[Ca2+][CO32−] | (15) |
At steady-state, eqn (15) can be rearranged to give an effective stoichiometric solubility product of calcite as a function of magnesium coverage
![]() | (16) |
Note that is different to the stoichiometric solubility constant, K0sp, defined in eqn (1) since a coverage of magnesium on calcite surfaces gives rise to a lower effective stoichiometric solubility product of calcite.
The average surface coverage of magnesium, θMg2+, is given by the Langmuirian adsorption isotherm48,49
![]() | (17) |
Substituting eqn (17) into eqn (16) shows
![]() | (18) |
Fig. 3D shows a plot of versus (1 + KMg[Mg2+])−1, where KMg is the adsorption constant of magnesium on Iceland Spar (230 ± 60 M−1) reported by Compton and Brown14 and
was inferred from the experimental measurements of
and by solving the CaCO3 and carbonate equilibrium shown in ESI Section 7.†
As can be seen in Fig. 3D, the experimentally inferred as a function of magnesium concentration is in good agreement with the simple model using a magnesium adsorption constant derived from independent measurements.14 At high magnesium concentrations where
is close to zero the experimental data can be seen to deviate from the simple model. This is likely due to the presence of multiple sites available for adsorption on calcite surfaces as suggested by AFM studies.15 Finally, we note that the idea of a ‘partially blocked’ surface leading to a reduced average surface concentration is well established in the electrochemical literature (as summarised in ESI Section 9†,50–52) where the scale of the heterogeneity is small compared to diffusional lengths leads to a uniform, average surface concentration reflecting a balance of independent kinetic contributions. We accordingly view the calcite surface as a ‘partially blocked’ surface where the total macroscopic surface concentration is a sum of contributions by the ‘blocked’ and ‘unblocked’ zones:
![]() | (19) |
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3sc04063a |
‡ These authors contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2024 |