Cement and Concrete Research 42 (2012) 1157–1165 Contents lists available at SciVerse ScienceDirect Cement and Concrete Research journal homepage: http://ees.elsevier.com/CEMCON/default.asp Uptake of chloride and carbonate ions by calcium monosulfoaluminate hydrate Adel Mesbah a, b, Céline Cau-dit-Coumes a,⁎, Guillaume Renaudin b, d, Fabien Frizon a, Fabrice Leroux c, d a Commissariat à l'Energie Atomique et aux Energies Alternatives, CEA DEN/DTCD/SPDE, F-30207 Bagnols sur Cèze, France Clermont Université, ENSCCF, Laboratoire des Matériaux Inorganiques, BP 10448, F-63000 Clermont-Ferrand, France c Clermont Université, Université Blaise Pascal, Laboratoire des Matériaux Inorganiques, BP 10448, F-63000 Clermont-Ferrand, France d CNRS, UMR 6002, F-63177 Aubière, France b a r t i c l e i n f o Article history: Received 14 February 2012 Accepted 16 May 2012 Keywords: Waste management (E) Monosulfate (D) Chloride (D) Carbonation (C) X-ray diffraction (B) a b s t r a c t Decommissioning of old nuclear reactors may produce waste streams containing chlorides and carbonates, including radioactive 36Cl − and 14CO32−. Their insolubilization by calcium monosulfoaluminate hydrate was investigated. Carbonates were readily depleted from the solution, giving at thermodynamic equilibrium monocarboaluminate, monocarboaluminate + calcite, or calcite only, depending on the initial ratio between the anion and calcium monosulfoaluminate hydrate. Chloride ions reacted more slowly and were precipitated as Kuzel's salt, Kuzel's and Friedel's salts, or Friedel's salt only. Rietveld refinement of X-Ray powder diffraction patterns was successfully used to quantify the phase distributions, which were compared to thermodynamic calculations. Moreover, analysing the lattice parameters of Kuzel's salt as a function of its chloride content showed the occurrence of a restricted solid solution towards the sulfate side with general formula 3CaO·Al2O3·xCaCl2·(1 − x)CaSO4·(12 − 2x)·H2O (0.36 ≤ x ≤ 0.50). © 2012 Elsevier Ltd. All rights reserved. 1. Introduction Calcium sulfoaluminate (CSA) cements may have a good potential to stabilize hazardous wastes such as heavy metals [1–7], ion exchange resins [8], aluminum-containing wastes [9] or radioactive streams containing high amounts of borate and sulfate ions [10]. Unlike Portland cement, hydration of CSA cement leads to the formation of two principal hydrates: calcium monosulfoaluminate hydrate [11] and ettringite [12] with general formula 3CaO·Al2O3·CaSO4·12H2O and 3CaO·Al2O3·3CaSO4·32H2O, respectively. Their contents are very sensitive to the amount of added sulfate: the former dominates in a gypsum-deficient environment, whereas the latter tends to increase in a gypsum-rich system [13]. Both ettringite and calcium monosulfoaluminate hydrate have a flexible structure and can admit various substitutions on their cationic or anionic positions [14–18]. In this study, the focus is placed on chloride and carbonate anions, which may contain long-lived radioactive isotopes 36Cl and 14C, in waste streams produced during the decommissioning of old nuclear reactors (UNGG-type, graphite moderated, cooled by carbon dioxide, and fuelled with natural uranium metal). In the literature, AFm phases are considered as good candidates to bind chloride anions contrarily to AFt phases [15,19,20]. Two Cl-containing AFm phases are involved: Kuzel's salt 3CaO·Al2O3·1/2CaSO4·1/2CaCl2·11H2O, a crystallized compound containing ordered chloride and sulfate anions, and Friedel's salt 3CaO·Al2O3·CaCl2·10H2O, a phase containing chloride anions only. Moreover, it is well known that cement-based materials can be easily carbonated, leading to the formation of calcium hemicarboaluminate hydrate 3.5CaO·Al2O3·1/2CaCO3·12H2O, calcium monocarboaluminate hydrate 3CaO·Al2O3·CaCO3·11H2O and/or calcite [21–26]. The AFm phases belong to the lamellar double hydroxide (LDH) large family. Their structure is composed of positively charged main layers [Ca2Al(OH)6] + and negatively charged interlayers [X·nH2O] −, where X is one monovalent anion or half a divalent anion. The following general formulae 3CaO∙Al2O3∙CaX2∙nH2O for a monovalent anion, or 3CaO∙Al2O3∙CaX∙nH2O for a divalent anion, are generally used in cement chemistry. Several structural studies have been performed on AFm compounds incorporating one type of anion only in the interlayer: SO42− [11], Cl − [27–29], CO32− [30,31], NO3− [32,33], I − [34,35] and Br − [34,35]. Others studies were devoted to bi anionic-AFm compounds formed by Cl −\Br − [35], CO32−\OH − [36], CO32−\Cl − [37–39] or SO42−\Cl − permutation [40]. The present study was undertaken within a project aiming at assessing the binding capacities of chloride and carbonate anions by hydrated CSA cements. The first step was to investigate the uptake of Cl − and CO32− by calcium monosulfoaluminate hydrate. 2. Experimental section 2.1. Samples preparation ⁎ Corresponding author. Tel.: + 33 4 66 39 74 50; fax: + 33 4 66 33 90 37. E-mail address: [email protected] (C. Cau-dit-Coumes). 0008-8846/$ – see front matter © 2012 Elsevier Ltd. All rights reserved. doi:10.1016/j.cemconres.2012.05.012 Calcium monosulfoaluminate hydrate with general formula 3CaO∙Al2O3∙CaSO4∙12H2O was synthesized in aqueous solution. The 1158 A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 starting reagents, tricalcium aluminate (Ca3Al2O6) and gypsum (CaSO4∙2H2O), were mixed in decarbonated water (boiled during 1 h and cooled under nitrogen atmosphere) to reach a final water/ solid mass ratio of 50. The suspension was introduced in a Teflon reactor and stirred continuously at 80 °C during three weeks. The temperature was chosen to avoid the formation of ettringite, which is unstable over ~70 °C under these conditions [41]. Then, the suspension was filtered twice using pure water and finally rinsed with isopropanol. The precipitates were subsequently dried in a desiccator over potassium acetate (≈20% r.h.) at room temperature. Sorption tests were carried out by adding 0.5 g (8.03 × 10 − 4 mole) of calcium monosulfoaluminate hydrate to 10 mL of sodium chloride (NaCl) or sodium carbonate (Na2CO3) solutions. The suspensions were kept under stirring at 20 °C. Two series of sorption tests were performed, firstly to study the exchange rate between sulfate and chloride or carbonate, and secondly to investigate the influence of the initial concentration of chloride or carbonate on this exchange. In the first series of experiments, the Cl −/monosulfoaluminate and CO32−/monosulfoaluminate molar ratios were fixed to 2 and 1 respectively, and the stirring time varied from 1 to 28 days. The second series of experiments lasted for 28 days. The Cl -/monosulfoaluminate molar ratios were fixed to n = 0.2, 0.5, 1, 1.5, 2, 5 and the CO32−/ monosulfoaluminate ratios to 0.25, 0.75, 1, 2, 3.5 and 5. At the end of an experiment, the suspension was filtered at 0.45 μm. The solid fraction was analyzed by X-ray powder diffraction and thermogravimetry. The anion concentrations in the solution were determined by ion chromatography and total inorganic carbon analysis. 2.3. Solution analysis Chloride and sulfate anions were analyzed using ionic chromatography (Dionex DX 500 equipped with AS9 HC analytical column and AG9 HC guard column, injection volume = 100 μL, eluent = Na2CO3 9 mmol/L, flow rate = 1 mL/min, detection = suppressed conductivity (ASRS 300 suppressor in the autosuppression recycle mode)). Carbonates were analyzed using a total organic carbon analyzer from Shimadzu (TOC V-VPN). The quantification limits were 0.5 mg/L for chloride, 1 mg/L for sulfate, and 0.1 mg/L for carbonates. Concentrations were measured with ±5% accuracy. 2.4. Thermodynamic modelling Thermodynamic calculations were carried out using the CHESS software [46]. The solubility constants of the selected cement phases were taken from the CEMDATA 07 database [47], and from [20] for Kuzel's salt. 3. The CaO\Al2O3\CaSO4\CaCl2\H2O system Details of the X-ray powder patterns corresponding to the chloride sorption tests are presented in Fig. 1. a K E 2.2. Solid characterization Thermogravimetric analyses were carried out under nitrogen on 50 ± 2 mg of sample using a TGA/DSC Netzsch STA409 PC instrument at 10 °C/min up to 1000 °C. X-ray powder diffraction (XRPD) patterns were recorded on a Bruker D8 diffractometer, equipped with a “Lynx eye” detector, using Cu Kα radiation (λ = 1.54184 Å). XRPD patterns were recorded at room temperature within the interval 4° b 2θ b 120°, with a step size Δ2θ = 0.011° and a total counting time of 8 h for each sample. The measurements were carried out with the Debye Scherrer geometry (capillary) to reduce the preferred orientation effect. Quantitative phase analysis was performed using Rietveld method with the FullProf_Suite program [42]. All refinements used the Thomson–Cox–Hastings Pseudo Voigt convoluted with an axial divergence asymmetry function [43]. The instrumental function was extracted from pure silicon measured under the same conditions. Rietveld refinement were performed considering the structural models described by Allmann for monosulfoaluminate [11], Rapin et al. for Friedel's salt [28], Mesbah et al. for Kuzel's salt [40], GoetzNeunhoeffer and Neubauer for ettringite [44], François et al. for monocarboaluminate [30] and for calcite [45]. Rietveld treatments were used to characterize the mineralogical composition of the samples after contact with chloride and carbonate solutions (quantitative analyses), and to characterize the restricted Kuzel's salt solid solution (lattice parameters and anionic contents in the interlayer regions). Concerning the refinements involving the restricted Kuzel's salt solid solution, the following three constraints were applied: 1) full occupancy of the anionic 3a and 3b sites by considering the presence of water molecule with XCl + XOw =1 in chloride interlayer and XS + XOw =1 in sulfate interlayer (X is an occupancy parameter, the corresponding atom being given in subscript), 2) XCl + 2 XS = 1 to respect electroneutrality of the crystal, and 3) XOs1 = XS and XOs2 =3 XS to respect the sulfate geometry (Os1 and Os2 are the apical and basal oxygen atoms of the sulfate anion, respectively). For more details, see the complete structural description of Kuzel's salt recently reported [40]. Ms E b K E Ms E F Fig. 1. XRPD patterns recorded after sorption tests with chloride anions (zoom on (00l) reflexions). Influence of the reaction time (a) and of the initial chloride concentration (b) on the phase assemblage. Hydrates are labelled: Ms (calcium monosulfoaluminate hydrate), K (Kuzel's salt), E (ettringite) and F (Friedel's salt). n indicates the initial chloride/monosulfoaluminate molar ratio. The time series was performed at n = 2. A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 1159 DTG (%/°C) Ms K Temperature(°C) Fig. 2. DTG curves of the phase assemblage obtained after sorption tests (calcium monosulfoaluminate hydrates + NaCl): influence of contact time (Ms: calcium monosulfoaluminate hydrate, E: ettringite, K: Kuzel's salt) (n = initial chloride/ monosulfoaluminate ratio = 2). 3.1. Investigating the exchange rate between sulfate and chloride anions Five sorption tests were performed with a Cl−/monosulfoaluminate molar ratio of 2, and increasing contact times of 1, 4, 7, 14 and 28 days. The corresponding X-ray patterns showed the presence of three hydrates. Precipitation of Kuzel's salt and ettringite was already observed after one day. From 4 days, the peak intensity of calcium monosulfoaluminate hydrate decreased significantly, while the relative intensities of the two other hydrates increased. After 28 days, calcium monosulfoaluminate hydrate was fully depleted. The diffraction peak close to 2θ = 10° with weak intensity corresponded to ettringite (Fig. 1). Thermogravimetry analysis (Fig. 2) confirmed the precipitation of ettringite and Kuzel's salt. The weight amounts of each crystallized phase were determined by Rietveld refinement. Their equivalent molar amounts are reported in Table 1 and presented in Fig. 3-a. The results confirmed the previous qualitative observations. At 28 days, calcium monosulfoaluminate hydrate was converted to Kuzel's salt and ettringite in 77:23 molar ratio, not far from balance equation (Eq. (1)) − ð1Þ 9 ½3CaO ˙ Al2 O3 ˙ CaSO4 ˙ 12H2 O þ 6 Cl þ 28 H2 O→ 6 ½3CaO ˙ Al2 O3 ˙ 1=2CaSO4 ˙ 1=2CaCl2 ˙ 11H2 O þ 2 ½3CaO ˙ Al2 O3 ˙ 3CaSO4 ˙ 32H2 O þ 2 − Al2 O3 ˙ 3H2 O þ 6 OH Fig. 3. Refined molar amounts of hydrates at the end of the sorption tests (calcium monosulfoaluminate hydrate + NaCl): influence of contact time (a) and initial chloride concentration (b). n indicates the initial chloride/monosulfoaluminate ratio (n = 2 for the time series). (Eq. (1)) assumed the precipitation of aluminum hydroxide. This phase, which can be poorly crystallized, was not detected by XRD. However, even on the TGA diagrams (Fig. 2), we did not observe any characteristic weight loss near 250 °C, due to the dehydration of AH3. This result could be explained by the small amount of AH3 formed, below the detection limit of the method. For instance, after 28 days, the AH3 amount should represent 0.9 wt.%, versus 59.0% for Kuzel's salt, and 40.1% for ettringite (Table 1) according to the stoichiometry of (Eq. (1)). Table 1 Influence of reaction time on the phase assemblage formed by mixing calcium monosulfoaluminate hydrate with NaCl solution (n = initial chloride/monosulfoaluminate molar ratio = 2). Indicated errors correspond to standard deviation extracted from Rietveld refinements. Calculated amounts (μmol)a Time (days) Refined molar amounts (%) Monosulfoaluminate (x) Kuzel's salt (y) Ettringite (z) Monosulfoaluminate Kuzel's salt Ettringite Aluminum hydroxide 0 1 4 7 14 28 100 43.4 ± 0.8 20.5 ± 0.8 11.0 ± 0.6 7.4 ± 0.6 0 0 43.4 ± 0.8 62.9 ± 1.0 64.5 ± 0.8 71.7 ± 0.8 77.1 ± 0.6 0 13.2 ± 0.5 16.7 ± 1.0 24.5 ± 0.6 20.8 ± 0.6 23.0 ± 0.5 803 327 152 79 54 0 0 326 466 461 522 515 0 100 124 175 152 165 0 50 62 88 76 83 Calculated residual chloride amount (mmol) Measured residual chloride amount (mmol)b 1.61 1.28 1.14 1.15 1.09 1.05 – 1.18 1.22 1.22 1.20 1.09 a Calculation performed by assuming the balance equation: [3CaO·Al2O3·CaSO4·12H2O]+ α Cl− + β H2O → γ [3CaO·Al2O3·1/2CaSO4·1/2CaCl2·11H2O]+ δ [3CaO·Al2O3·3CaSO4·32H2O]+ ε Al2O3·3H2O + μ OH−, stoichiometric coefficients calculated from the Rietveld refinement results and conservation of matter: z 1z γ ¼ μ ¼ α ¼ 1þ13z, δ ¼ 1þy 3z, ε ¼ 1þ2y3z, β ¼ 2y 2y 2y 31z 1 2 y−2 1þ32yz yþ3z where y and z are the refined molar amounts of Kuzel's salt and ettringite.The depleted mol number of monosulfate is given by a ¼ a0 1þ21z 2 (where a0 stands for the initial mol number of monosulfoaluminate), and the precipitated mol numbers of Kuzel's salt, ettringite and aluminum hydroxide are γ·a, δ·a and ε·a respectively. b Amount derived from the measured concentration, by taking into account the volume decrease of the aqueous phase due to consumption of water. 1160 A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 1.8E+00 1.7E+00 1.6E+00 1.5E+00 1.4E+00 1.3E+00 1.2E+00 1.1E+00 1.0E+00 8.5E-03 8.0E-03 7.5E-03 7.0E-03 6.5E-03 6.0E-03 5.5E-03 5.0E-03 4.5E-03 4.0E-03 Chloride Sulfate 0 5 10 15 20 25 Released Sulfate (mmol) Residual chloride (mmol) a 30 Time (days) Chloride 0.025 Sulfate 0.02 2.5 0.015 2 1.5 0.01 1 0.005 0.5 0 0 0 1 2 3 4 5 Residual sulfate (mmol) Residual chloride (mmol) 0.03 4 3 Depleted Actual Corresponding Predicted amounts (μmol) chloride na time Monosulfoaluminate Kuzel's Ettringite Gibbsite amount (d) salt (mmol) 0.433 0.388 0.394 0.426 0.536 0.539 0.484 0.490 0.530 0.667 1 4 7 14 28 485 522 519 491 401 190 165 167 186 248 68 60 61 67 86 66 61 61 65 78 a Molar ratio between depleted chloride and initial calcium sulfoaluminate hydrate amounts. b 3.5 Table 2 Reaction of calcium monosulfoaluminate hydrate with chloride anions. Predicted phase assemblage composition at thermodynamic equilibrium. 6 concentration in the thermodynamic model was corrected by substracting the residual concentration measured experimentally in solution from the initial concentration, the calculated phase assemblage was significantly different from that observed, with lower contents of Kuzel's salt and ettringite (Tables 1 and 2). The system was far from thermodynamic equilibrium, apparently because of a delay in the precipitation of Friedel's salt which should involve the solubilisation of Kuzel's salt. n Fig. 4. Investigation of the chloride uptake by calcium monosulfoaluminate hydrate— evolution of the chloride and sulfate amounts in solution versus time (n = 2) (a) or versus initial Cl−/monosulfoaluminate molar ratio (n = 0.1 to 5) after 28 days of reaction (b). Relative amount of solid (% mol) Analysing the solutions for chloride and sulfate anions showed a rapid decrease, by a factor 1.4, of the residual chloride concentration during the first day (Fig. 4-a). Then, depletion of chloride strongly slowed down, and, after 28 days, the residual fraction still reached 66%. On the contrary, only very small amounts of sulfate were detected, irrespectively of the contact time, due to ettringite precipitation. The consistency between the refined data on the solid phase assemblages and the solution analyses was checked by calculating the mol number of Kuzel's salt formed versus time, and the resulting residual chloride concentration was compared with that determined by ion chromatography. The deviation between the two results was less than 10% (Table 1). Kuzel's salt was the only chloride-containing AFm phase. Friedel's salt was not observed under our conditions, unlike Hirao et al. [19] who detected it directly after 2 days of experiment. Thermodynamic calculations predicted the precipitation of Kuzel's salt, Friedel's salt, gibbsite and ettringite (Fig. 5). Even when the reacting chloride 100 Monosulfo Kuzel Friedel Ettringite Gibbsite 90 80 70 3.2. Investigating the influence of the chloride concentration Calcium monosulfoaluminate hydrate was mixed with solutions of increasing chloride concentration, corresponding to n ratios of 0.2, 0.5, 1, 1.5, 2 and 5. After 28 days, the crystallized phases identified by X-ray diffraction were calcium monosulfoaluminate hydrate, Kuzel's salt, ettringite, and Friedel's salt. Their respective proportions were quantified as a function of n by Rietveld refinement (Fig. 3-b, Table 3). At low chloride concentrations (0 b n ≤ 1), residual calcium monosulfoaluminate hydrate dominated over Kuzel's salt and ettringite. The proportions of these two phases increased however with n. At intermediate chloride concentrations (1 b n ≤ 2), calcium monosulfoaluminate hydrate was fully converted into Kuzel's salt and ettringite. At higher chloride concentrations (n = 5), Friedel's salt additionally precipitated. The chloride and sulfate concentrations in solution after 28 days increased almost linearly versus n (Fig. 4-b). Chlorides always remained in great excess over sulfates. The different systems were far from equilibrium after 28 days of reaction. Thermodynamic modelling predicted indeed the depletion of calcium monosulfoaluminate hydrate from n = 1.3, the precipitation of Friedel's salt from n = 1.65, and the depletion of Kuzel's salt from n = 2.35 (Fig. 5). This showed again that the restricting parameter was the transformation of Kuzel's salt into Friedel's salt. Qualitative analysis of the X-ray patterns presented in Fig. 1 showed a shift of the (003) reflexion of the Kuzel's salt (towards Table 3 Influence of the initial chloride concentration on the phase assemblage formed by mixing calcium monosulfoaluminate hydrate with NaCl solution (t = 28 days). Indicated errors correspond to standard deviation extracted from Rietveld refinements. 60 50 40 30 na 20 Refined molar fraction (%) Monosulfoaluminate 10 0 0 1 2 3 4 5 6 n Fig. 5. Thermodynamic modelling of the phase assemblage formed in the calcium sulfoaluminate hydrate–NaCl system as a function of n (initial chloride/ monosulfoaluminate molar ratio). 0.2 0.5 1 1.5 2 5 a 87.5 ± 0.8 74.0 ± 0.8 50.4 ± 0.8 0 0 0 Kuzel's salt 6.7 ± 0.2 17.2 ± 0.4 35.6 ± 0.6 77.1 ± 0.8 77.1 ± 0.6 65.3 ± 1.0 Ettringite 5.8 ± 0.2 8.8 ± 0.4 14.1 ± 0.4 22.9 ± 0.6 23.0 ± 0.5 25.6 ± 0.7 n = initial chloride/monosulfoaluminate molar ratio. Friedel's salt 0 0 0 0 0 9.1 ± 0.8 A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 Table 4 Refined lattice parameters of Kuzel's salt obtained after reaction of calcium monosulfoaluminate hydrate with chloride anions with general formula of 3CaO·Al2O3· xCaCl2·(1 − x)CaSO4·(12 − 2x)H2O. Standard deviations are indicated in parentheses. na Time (days) a (Å) c (Å) Unit cell volume Refined x Cl2 2 2 2 2 2 0.2 0.5 1 2 1.5 5 1 4 7 14 28 28 28 28 28 28 28 5.7599(1) 5.7568(1) 5.7559(1) 5.7562(1) 5.7538(1) 5.7667(1) 5.7659(1) 5.7600(1) 5.7563(1) 5.7538(1) 5.7504(1) 50.6259(11) 50.5862(10) 50.5119(9) 50.5009(8) 50.4588(9) 50.7721(52) 50.6873(27) 50.6276(17) 50.5185(10) 50.4588(9) 50.3278(11) 1454.59(4) 1451.89(2) 1449.31(3) 1449.12(3) 1446.69(3) 1462.23(15) 1459.37(8) 1454.67(6) 1449.68(2) 1446.69(3) 1441.23(3) 0.40(1) 0.43(1) 0.44(1) 0.44(1) 0.46(2) 0.36(1) 0.38(1) 0.41(1) 0.43(1) 0.46(1) 0.49(1) a n = initial chloride/monosulfoaluminate molar ratio. 1161 interlayers: one composed of chloride and the other composed of sulfate anions. The evolution of the solid solution could be explained assuming the substitution of one chloride anion by one water molecule in the chloride interlayer, and the insertion of ½SO4 in the sulfate interlayer space with the departure of two water molecules. The sulfate insertion into the sulfate interlayer region was allowed by the statistic distribution between one sulfate anion and two water molecules in Kuzel's salt structure [40]. The full occupancy of the chloride site in the Kuzel's salt structure (chloride interlayer region fully occupied with Cl − anions [40]) prevented the extension of the Kuzel's salt solid solution towards the chloride side (i.e. with x > 0.50). Fig. 7 shows a projection along [100] of Kuzel's salt and of a solid solution obtained by replacing 2 chloride ions by 2 water molecules in the chloride interlayer, and 2 water molecules by 1 sulfate ion in the adjacent sulfate interlayer. 4. CaO\Al2O3\CaSO4\CaCO3\H2O system smaller interlayer distance when increasing time of contact or increasing n), which could indicate the existence of a solid solution between chloride and sulfate ions in the interlayer space of the AFm phase, as already postulated by Glasser et al. [15]. This was confirmed by the Rietveld refinement results (Table 4, Fig. 6). The lattice parameters (a, b and unit cell volume) decreased linearly when the chloride content increased, following a Vegard's law. The decrease could be explained by the smaller size of chloride (anionic radius = 1.67 Å) compared to sulfate (around 2.4 Å). The chloride amount in the interlayer space varied between 0.36(1) ≤ x ≤ 0.50(1), giving general formula 3CaO·Al2O3·xCaCl2·(1 − x)CaSO4·(12 − 2x)H2O. The solid solution between sulfate and chloride had a restricted range, which could be linked to the structural properties of Kuzel's salt [40]. This AFm phase is a two-stage layered compound with two distinct To investigate the possible exchange between sulfates and carbonates, calcium monosulfoaluminate hydrate was mixed with solutions of sodium carbonate. The X-ray diffraction patterns recorded on the solid phases after increasing contact times or carbonate concentrations are shown in Fig. 8. 4.1. Investigating the exchange rate between sulfate and carbonate ions Five experiments were performed with a CO32−/monosulfoaluminate molar ratio of 1, and contact times increasing from 1 to 28 days. Up to 7 days, only two crystallized phases were detected: calcium monosulfoaluminate hydrate and calcite. Their molar fractions were estimated (during the first week) to be 36 ±1 and 64±1% respectively by Rietveld Fig. 6. Evolution of the lattice parameters of Kuzel's salt versus its chloride content (assessed from Rietveld refinement) with general formula of 3CaO·Al2O3·xCaCl2·(1 − x) CaSO4·(12 − 2x)H2O. Triangles correspond to the experiments aiming at investigating the contact time between chlorides and sulfates, and squares to the experiments on the influence of n (initial chloride/monosulfoaluminate molar ratio). 1162 A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 Fig. 7. Structure of Kuzel's salt (a) and of Kuzel's salt enriched in sulphate (solid solution) (b) represented along [100]. For clarity reasons, distribution between one sulfate group and two water molecules, and orientation disorder of sulfate groups (up and down) were ordered. refinement (Table 5, Fig. 9-a). A balance equation such as (Eq. (2)) would lead to a maximum calcite fraction of 57.1% (and to a minimum monosulfoaluminate fraction of 42.9%) assuming the consumption of all carbonate ions, which is lower than the Rietveld estimation. 2 2 75:25 ½3CaO ˙ Al2 O3 ˙ CaSO4 ˙ 12H2 O þ 79CO3 þ 254:5H2 O→32 ð3Þ ½3CaO ˙ Al2 O3 ˙ CaCO3 ˙ 11H2 O þ 21 ½3CaO ˙ Al2 O3 ˙ 3CaSO4 ˙ 32H2 O þ 47 CaCO3 þ 22:25 2 − ½Al2 O3 ˙ 3H2 O þ 12:25 SO4 þ 133:5 OH 2 ½3CaO ˙ Al2 O3 ˙ CaSO4 ˙ 12H2 O þ 4 CO3 →4 CaCO3 þ SO4 þ ½Al2 O3 ˙ 3H2 O þ 6 OH þ H2 O the investigated systems. The Rietveld analysis suggested a balance equation such as (Eq. (3)). ð2Þ Additional information was provided by the analysis of the aqueous fractions (Table 6). Given the residual concentration of carbonates and the released concentration of sulfates, the molar ratio between calcium monosulfoaluminate hydrate and calcite should be equal to 0.726, which corresponds to relative fractions of 57.9% and 42.1% for the two phases, and agrees well with balance equation (Eq. (2)) given measurement errors. The Rietveld analysis thus slightly overestimated calcite, and/or underestimated calcium monosulfoaluminate hydrate. This could result from very different crystallinities of the two phases. After 7 days, the calcite content decreased while calcium monocarboaluminate hydrate and ettringite precipitated. At 28 days, calcium monosulfoaluminate hydrate was almost fully depleted, and the phase assemblage comprised ettringite, calcium monocarboaluminate hydrate, and calcite in respective proportions of 32/21/47 according to Rietveld refinement. Calcium hemicarboaluminate hydrate was never observed, which could be explained by the absence of portlandite in Given the residual carbonate concentration measured in the aqueous fraction (Table 6), the sulfate amount theoretically released according to (Eq. (3)) was calculated to be 0.120 mmol, in rather good agreement with the experimental determination (0.140 ± 0.010 mol). However, under these conditions, the residual amount of calcium monosulfoaluminante hydrate should be slightly higher than that estimated by Rietveld refinement (monosulfoaluminate/ monocarboaluminate/ettringite/calcite in 6/30/20/44 molar proportions, instead of 0.4/31.7/20.7/47.2). Once again, the Rietveld analysis seemed to overestimate slightly calcite and/or underestimate calcium monosulfoaluminate hydrate. The broadening of the diffraction peaks of calcium monosulfoaluminate hydrate probably affected the quality of the quantification. The phase assemblage was close to thermodynamic equilibrium (Fig. 10). Calculations predicted the complete depletion of calcium monosulfoaluminate hydrate, and the precipitation of gibbsite, calcium monocarboaluminate hydrate, ettringite and calcite, with 35/22/43 proportions for monocarboaluminate, ettringite and calcite, respectively. A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 Fig. 8. XRPD patterns recorded after sorption tests with carbonate anions (zoom on (00l) reflexions). Influence of the reaction time (a) and the initial carbonate concentration (b) on the phase assemblage. Hydrates are labelled: Ms (calcium monosulfoaluminate hydrate), Mc (calcium monocarboaluminate hydrate), E (ettringite) and C (calcite). n indicates the initial carbonate/monosulfoaluminate molar ratio. The time series was performed at n = 1. 4.2. Investigating the influence of the carbonate concentration Calcium monosulfoaluminate hydrate was mixed for 28 days with solutions containing increasing carbonate concentrations, giving n ratios of 0.25, 0.75, 1, 2, 3.5 and 5. The evolution of the respective 1163 Fig. 9. Refined molar amounts of hydrates at the end of the sorption tests (calcium monosulfoaluminate hydrate + Na2CO3); influence of contact time (a) and initial carbonate concentration (b). n indicates the initial carbonate/monosulfoaluminate molar ratio. The time series was performed at n = 1. proportions of calcium monosulfoaluminate hydrate, ettringite, calcite and monocarboaluminate, estimated from Rietveld refinement, is shown in Fig. 9-b. At low carbonate concentration (n = 0.25), calcium monosulfoaluminate hydrate was partly converted into ettringite and calcium monocarboaluminate hydrate, according to mass balance equation (Eq. (4)). 2 Table 5 Influence of reaction time and initial carbonate concentration on the phase assemblage formed by mixing calcium monosulfoaluminate hydrate with Na2CO3 solution. Indicated errors correspond to standard deviation extracted from Rietveld refinements. n a 1 1 1 1 1 0.25 0.75 2 3.5 5 a t (days) 1 4 7 14 28 28 28 28 28 28 Refined molar fraction (%) Monosulfoaluminate Ettringite Monocarboaluminate Calcite 36.5 ± 0.7 36.5 ± 0.7 35.3 ± 0.8 31.3 ± 0.7 0.4 ± 0.1 64.7 ± 0.8 5.4 ± 0.6 7.9 ± 1.0 1.2 ± 0.6 0 0 0 0 2.4 ± 0.4 20.8 ± 1.2 23.9 ± 0.6 24.2 ± 1.1 0 0 0 0 0 0 0.9 ± 0.4 31.7 ± 0.3 11.4 ± 0.4 32.1 ± 1.6 11.7 ± 1.5 3.5 ± 1 0 63.5 ± 0.4 63.5 ± 0.4 64.7 ± 0.4 65.5 ± 0.4 47.2 ± 0.8 0 38.4 ± 0.4 80.4 ± 0.8 95.3 ± 0.8 100 n = initial carbonate/monosulfoaluminate molar ratio. 7=2 ½3CaO ˙ Al2 O3 ˙ CaSO4 ˙ 12H2 O þ 2 CO3 þ 15 H2 O→2 ½3CaO ˙ Al2 O3 ˙ CaCO3 ˙ 11H2 O þ 2− − ½3CaO ˙ Al2 O3 ˙ 3CaSO4 ˙ 32H2 O þ 1=2 ½Al2 O3 ˙ 3H2 O þ 1=2 SO4 þ 3 OH ð4Þ According to this equation, the expected sulfate and carbonate amounts in the aqueous phase would be 0.045 mmol and 0.019 mmol, Table 6 Amounts (mmol) of carbonates and sulfates in the aqueous fractions at the end of the sorption tests (initial calcium monosulfoaluminate hydrate amount = 0.803 mmol). na t (days) SO42− CO32− 1 1 1 1 1 0.25 2 5 1 4 7 14 28 28 28 28 0.239 0.244 Not measured 0.220 0.141 0.044 0.547 0.800 0.025 0.032 0.026 0.033 0.028 0.012 0.045 0.724 a n = initial carbonate/monosulfoaluminate molar ratio. 1164 Relative amout of solid (mol%) a A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 100 90 80 70 60 50 40 30 20 10 0 Monosulfo Calcite Monocarbo Ettringite Gibbsite 0 1 2 3 4 5 6 n Relative amout of solid (mol%) b 100 90 80 70 60 50 40 30 20 10 0 Monosulfo Calcite Monocarbo Ettringite exp Monosulfo exp Monocarbo exp Ettringite exp Calcite 0 1 2 3 4 5 6 n Fig. 10. (a) Thermodynamic modelling of the phase assemblage formed in the calcium sulfoaluminate hydrate–Na2CO3 system as a function of n (initial carbonate/ monosulfoaluminate molar ratio). (b) Comparison with experimental results at 28 days (gibbsite excluded). given the depleted amount of calcium monosulfoaluminate hydrate assessed from Rietveld analysis (0.317 mmol). This was in rather good agreement with the analyses of solution (0.044 mmol of sulfates, and 0.012 mmol of carbonates—Table 6). Increasing n led to the additional precipitation of calcite. Calcium monosulfoaluminate hydrate was almost fully depleted at n = 1 but, quite unexpectedly, was detected again at n = 2 and 3.5. From n = 2, ettringite was not observed any longer. The fraction of calcium monocarboaluminate hydrate decreased when n increased beyond 1, while that of calcite went on increasing. At n = 5, calcite was the sole detected crystallized phase. These results, as well as the sulfate amount measured in solution (0.800 mmol), were consistent with mass balance equation (Eq. (5)). 2− 2− − ½3CaO ˙ Al2 O3 ˙ CaSO4 ˙ 12H2 O þ 4 CO3 →4 CaCO3 þ SO4 þ ½Al2 O3 ˙ 3H2 O þ 6 OH þ 6 H2 O ð5Þ Comparing the experimental results with the phase assemblage evolution predicted by thermodynamics showed two main differences (Fig. 10-b) the persistence of calcium monosulfoaluminate hydrate at n = 2 and 3.5, and the early disappearance of ettringite (from n = 2 instead of 3.1 for the model). Thermodynamic modelling was also performed by considering amorphous Al(OH)3 instead of less soluble gibbsite in the database. In that case, ettringite disappeared for n = 2.9, a value still significantly higher than the experimental one. Thus, the type of AH3 selected in the database could not explain the deviation between the modelled and experimental data at high n (n ≥ 2). It seems likely that the corresponding samples were not at thermodynamic equilibrium after 28 days. 5. Conclusion These results show that calcium monosulfoaluminate hydrate has a better potential for insolubilizing carbonates than chlorides. When equimolar amounts of calcium monosulfoaluminate hydrate and carbonates or chloride are made to react (0.803 mmol under the investigated conditions), the residual concentrations at thermodynamic equilibrium are calculated to be 32 times smaller for carbonates than for chloride (12.59 μmol against 402.6 μmol). Moreover, carbonates are much more readily insolubilized. Under the same experimental conditions, the aqueous concentration of carbonates is reduced by a factor 32 after one day for carbonates, and that of chlorides by a factor 1.26 only. Carbonates are rapidly depleted to form calcium monocarboaluminate hydrate (nb 0.5), calcium monocarboaluminate hydrate and calcite (0.5≤n≤4.3), or calcite only (n>4.3) at thermodynamic equilibrium. At n=1, the reaction occurs by the precipitation of calcite which is later partly destabilized into calcium monocarboaluminate hydrate. Chloride ions react more slowly. Under the investigated experimental conditions, thermodynamic equilibrium is not achieved after 28 days at ambient temperature. The final chloride-containing products are Kuzel's salt (0.2 ≤ n b 1.65), Kuzel's and Friedel's salts (1.65 ≤ n ≤ 2.35), and Friedel's salt only at higher n. The reaction proceeds by the transient precipitation of Kuzel's salt which is later converted into Friedel's salt. Rietveld analysis was successfully used for a quantitative analysis of the solid phase distribution. The lattice parameters of Kuzel's salt were shown to decrease linearly when the chloride concentration increased, which clearly demonstrates the occurrence of a solid solution between sulphate and chloride within a restricted range of compositions 3CaO·Al2O3·xCaCl2·(1 − x)CaSO4·(12 − 2x)H2O with 0.36 ≤ x ≤ 0.50, towards the sulfate side. Acknowledgments The authors are grateful to Pascal Antonucci for his help on the synthesis experiments. Laurent Petit, from Electricité de France, is deeply acknowledged for his support on the study. References [1] R. Berardi, R. Cioffi, L. Santoro, Chemical effects of heavy metals on the hydration of calcium sulphoaluminate 4CaO·3Al2O3·SO3, J. Therm. Anal. Calorim. 50 (1997) 393–400. [2] S. Berger, C. Cau Dit Coumes, P. Le Bescop, D. Damidot, Hydration of calcium sulfoaluminate cement by a ZnCl2 solution: investigation at early age, Cem. Concr. Res. 39 (2009) 1180–1187. [3] C.A. Luz, J. Pera, M. Cheriaf, J.C. Rocha, Behaviour of calcium sulfoaluminate cement in presence of high concentrations of chromium salts, Cem. Concr. Res. 37 (2007) 624–629. [4] C.A. Luz, J.C. Rocha, M. Cheriaf, J. Pera, Use of sulfoaluminate cement and bottom ash in the solidification/stabilization of galvanic sludge, J. Hazard. Mater. 136 (2006) 837–845. [5] C.A. Luz, J.C. Rocha, M. Cheriaf, J. Pera, Valorization of galvanic sludge in sulfoaluminate cement, Constr. Build. Mater. 23 (2009) 595–601. [6] J. Péra, J. Ambroise, M. Chabannet, Valorization of automotive shredder residue in building materials, Cem. Concr. Res. 34 (2004) 557–562. [7] S. Peysson, J. Péra, M. Chabannet, Immobilization of heavy metals by calcium sulfoaluminate cement, Cem. Concr. Res. 35 (2005) 2261–2270. [8] J. Li, J. Wang, Advances in cement solidification technology for waste radioactive ion exchange resins: a review, J. Hazard. Mater. 135 (2006) 443–448. [9] Q. Zhou, N.B. Milestone, M. Hayes, An alternative to Portland cement for waste encapsulation—the calcium sulfoaluminate cement system, J. Hazard. Mater. 136 (2006) 120–129. [10] C. Cau Dit Coumes, S. Courtois, S. Peysson, J. Ambroise, J. Pera, Calcium sulfoaluminate cement blended with OPC: a potential binder to encapsulate low-level radioactive slurries of complex chemistry, Cem. Concr. Res. 39 (2009) 740–747. [11] R. Allmann, Refinement of the hybrid layer structure hexahyd-roxoaluminodicalcium hemisulfate trihydrate [Ca2Al (OH)6] [1/2SO4·3H2O], Neues Jb Mineralog. Monatsh. 3 (1977) 136–144. [12] A.E. Moore, H.F.W. Taylor, Crystal structure of ettringite, Acta Cryst. B 26 (1970) 386–393. [13] F.P. Glasser, L. Zhang, Calculation of chemical water demand for hydration of calcium sulfoaluminate cement, Proceedings of the 4th International Symposium on Cement and Concrete, Shanghai, 1998, pp. 38–44. [14] M. Chrysochoou, D. Dermatas, Evaluation of ettringite and hydrocalumite formation for heavy metal immobilization: literature review and experimental study, J. Hazard. Mater. 136 (2006) 20–33. [15] F.P. Glasser, A. Kindness, S.A. Stronach, Stability and solubility relationships in AFm phases: part I. chloride, sulfate and hydroxide, Cem. Concr. Res. 29 (1999) 861–866. A. Mesbah et al. / Cement and Concrete Research 42 (2012) 1157–1165 [16] M.L.D. Gougar, B.E. Scheetz, D.M. Roy, Ettringite and C-S-H Portland cement phases for waste ion immobilization: a review, Waste Manage. 16 (1996) 295–303. [17] P. Kumarathasan, G.J. Mccarthy, D.J. Hassett, D. Pflughoefthasset, Oxyanion substituted ettringites: synthesis and characterization; and their potential role in immobilization of As, B, Cr, Se and V, Proceedings of the Materials Research Society Symposium, 1990, pp. 83–104. [18] G.J. Mccarthy, D.J. Hassett, J.A. Bender, Synthesis, crystal chemistry and stability of ettringite, a material with potential applications in hazardous waste immobilization, Proceedings of the Materials Research Society Symposium, 1992, pp. 129–140. [19] H. Hirao, K. Yamada, H. Takahashi, H. Zibara, Chloride binding of cement estimated by binding isotherms of hydrates, J. Adv. Concr. Technol. 3 (2005) 77–84. [20] M. Balonis, B. Lothenbach, G. Le Saout, F.P. Glasser, Impact of chloride on the mineralogy of hydrated Portland cement systems, Cem. Concr. Res. 40 (2010) 1009–1022. [21] U.A. Birnin-Yauri, F.P. Glasser, Friedel's salt, Ca2Al(OH)6(Cl, OH)·2H2O: its solid solutions and their role in chloride binding, Cem. Concr. Res. 28 (1998) 1713–1723. [22] P. Brown, J. Bothe, The system CaO\Al2O3\CaCl2\H2O at 23 ± 2 °C and the mechanisms of chloride binding in concrete, Cem. Concr. Res. 34 (2004) 1549–1553. [23] M.R. Jones, D.E. Macphee, J.A. Chudek, G. Hunter, R. Lannegrand, R. Talero, S.N. Scrimgeour, Studies using 27Al MAS NMR of AFm and AFt phases and the formation of Friedel's salt, Cem. Concr. Res. 33 (2003) 177–182. [24] E.P. Nielsen, D. Herfort, M.R. Geiker, Binding of chloride and alkalis in Portland cement systems, Cem. Concr. Res. 35 (2005) 117–123. [25] T. Matschei, B. Lothenbach, F.P. Glasser, The AFm phase in Portland cement, Cem. Concr. Res. 37 (2007) 118–130. [26] B.Z. Dilnesa, B. Lothenbach, G. Le Saout, G. Renaudin, A. Mesbah, Y. Filinchuk, A. Wichser, E. Wieland, Iron in carbonate containing AFm phases, Cem. Concr. Res. 41 (2011) 311–323. [27] A. Terzis, S. Filippakis, H.J. Kuzel, H. Burzlaff, The crystal structure of Ca2Al(OH)6 Cl·2H 2 O, Z. Kristallogr. 181 (1987) 29. [28] J.P. Rapin, G. Renaudin, E. Elkaim, M. Francois, Structural transition of Friedel's salt 3CaO·Al2O3·CaCl2·10H2O studied by synchrotron powder diffraction, Cem. Concr. Res. 32 (2002) 513–519. [29] G. Renaudin, F. Kubel, J.P. Rivera, M. François, Structural phase transition and high temperature phase structure of Friedel's salt, 3CaO·Al2O3·CaCl2·10H2O, Cem. Concr. Res. 29 (1999) 1937–1942. [30] M. François, G. Renaudin, O. Evrard, A cementitious compound with composition 3CaO·Al2O3·CaCO3·11H2O, Acta Cryst. C 54 (1998) 1214–1217. [31] G. Renaudin, M. François, O. Evrard, Order and disorder in the lamellar hydrated tetracalcium monocarboaluminate compound, Cem. Concr. Res. 29 (1999) 63–69. 1165 [32] G. Renaudin, M. François, The lamellar double-hydroxide (LDH) compound with composition 3CaO·Al2O3·Ca(NO3)2·10H2O, Acta Cryst. C 55 (1999) 835–838. [33] G. Renaudin, J.P. Rapin, B. Humbert, M. François, Thermal behaviour of the nitrated AFm phase Ca4Al2(OH)12(NO3)2·4H2O and structure determination of the intermediate hydrate Ca4Al2(OH)12(NO3)2·2H2O, Cem. Concr. Res. 30 (2000) 307–314. [34] J.P. Rapin, A. Walcarius, G. Lefevre, M. François, A double-layered hydroxide, 3CaO·Al2O3·CaI2·10H2O, Acta Cryst. C 55 (1999) 1957–1959. [35] G. Renaudin, J.P. Rapin, E. Elkaim, M. François, Polytypes and polymorphs in the related Friedel's salt [Ca2Al(OH)6]+·[X·2H2O]− halide series, Cem. Concr. Res. 34 (2004) 1845–1852. [36] R. Fischer, H.J. Kuzel, Reinvestigation of the system C4A·nH2O\C4A·CO2·nH2O, Cem. Concr. Res. 12 (1982) 517–526. [37] A. Mesbah, C. Cau Dit Coumes, F. Frizon, F. Leroux, J. Ravaux, G. Renaudin, A new investigation of the Cl−\CO32− substitution in AFm phases, J. Am. Ceram. Soc. 94 (2011) 1901–1910. [38] A. Mesbah, J.P. Rapin, M. François, C. Cau-dit-Coumes, F. Frizon, F. Leroux, G. Renaudin, Crystal structures and phase transition of cementitious bi-anionic AFm-(Cl−, CO32 −) compounds, J. Am. Ceram. Soc. 94 (2011) 262–269. [39] M. Sacerdoti, E. Passaglia, Hydrocalumite from Latium, Italy: its crystal structure and relationship with related synthetic phases, Neues Jb Mineralog. Monatsh. 10 (1988) 462–475. [40] A. Mesbah, M. François, C. Cau-Dit-Coumes, F. Frizon, Y. Filinchuk, F. Leroux, J. Ravaux, G. Renaudin, Crystal structure of Kuzel's salt 3CaO·Al2O3·1/2CaSO4·1/2CaCl2·11H2O determined by synchrotron powder diffraction, Cem. Concr. Res. 41 (2011) 504–509. [41] D. Damidot, F.P. Glasser, Thermodynamic investigation of the CaO\Al2O3\CaSO4\H2O system at 50 °C and 85 °C, Cem. Concr. Res. 22 (1992) 1179–1191. [42] T. Roisnel, J. Rodriguez-Carvajal, WinPLOTR: a Windows tool for powder diffraction pattern analysis, Mater. Sci. Forum 378–381 (2001) 118–123. [43] L.W. Finger, D.E. Cox, A.P. Jephcoat, Correction for powder diffraction peak asymmetry due to axial divergence, J. Appl. Cryst. 27 (1994) 892–900. [44] F. Goetz-Neunhoeffer, J. Neubauer, Refined ettringite (Ca6Al2(SO4)3(OH)12·26H2O) structure for quantitative X-ray diffraction analysis, J. Powder Diffr. 21 (2006) 4–11. [45] J. Terada, Crystal structure of the Ba, Sr and Ca triple carbonate, J. Phys. Soc. Jpn 8 (1953) 158–164. [46] J. Van der lee, Thermodynamic and mathematical concepts of CHESS, Technical report LHM/RD/98/39, 1998, p. 99. [47] T. Matschei, B. Lothenbach, F.P. Glasser, Thermodynamic properties of Portland cement hydrates in the system CaO\Al2O3\SiO2\CaSO4\CaCO3\H2O, Cem. Concr. Res. 37 (2007) 1379–1410.
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