Formation of intermediate phases during hydration of C3S

The described model concepts can be employed as the basis for the development of binding agents possessing a significantly lower energy content and thus generating lower specific carbon dioxide emissions.

1 Introduction

The setting of cement is an important technological process. Nowadays, more than 2 billion t of cement are manufactured and processed all around the world. In addition to the technological parameters of the produced cements, such as water demand, setting times and compressive strength development, the industry places very great importance on the environmental impact of the cement manufacturing process. The main focus is placed on carbon dioxide emissions and the consumption of thermal and electrical energy. It can be assumed that cement production capacities will continue to...

1 Introduction

The setting of cement is an important technological process. Nowadays, more than 2 billion t of cement are manufactured and processed all around the world. In addition to the technological parameters of the produced cements, such as water demand, setting times and compressive strength development, the industry places very great importance on the environmental impact of the cement manufacturing process. The main focus is placed on carbon dioxide emissions and the consumption of thermal and electrical energy. It can be assumed that cement production capacities will continue to increase in the coming decades. This will be accompanied by an increase in the environmental impact if no decisive measures are taken to reduce material-specific carbon dioxide emissions and material-specific energy consumption rates [1].

The substitution of Portland cement clinker with latent-hydraulic, inert and pozzolanic materials is an important element in current efforts to reduce the environmental impact. Nevertheless, Portland cement clinker still has an outstanding function in respect of the quantities produced and significance for the strength development. Particularly with regard to the production of cements with rapid strength development, it is not conceivable that the industry could dispense with Portland cement clinker.

Against this background, an understanding of the fundamental processes is necessary in order to assess possible alternatives to Portland cement clinker. In such analyses, tricalcium silicate (Ca3SiO5, C3S) is generally used because a form of this compound that is rich in other oxides (alite) is the main component of Portland cement clinker and is the most important factor for its hydraulic setting.

The reaction of C3S with water to form X-ray-amorphous C-S-H phases and calcium hydroxide has been studied for more than 100 years now. It is assumed that the initial substance dissociates in the mixing water or the pore solution to form calcium, silicate and hydroxide ions and that the reaction products precipitate out of the supersaturated solution. This is a continuous dissolution-precipitation process, conversion rates of which vary considerably over the entire course of the process. This can be particularly simply proven by measuring the heat of reaction. As a result of such measurements the process has been divided into different time stages (Fig. 1).

Following an initial release of heat in the “pre-induction period”, there is an apparent period of dormancy that is also referred to as the “induction period”. Generally, the heat release of the first few minutes is attributed to the slaking of free lime, the wetting of the solid material with water, the dissolution of a small quantity of C3S and the formation of the first hydrate phases, although the contributions of these individual reactions are difficult to quantify. The subsequent induction phase of the main hydration is very important from a technological point of view, as it governs the transportation, placing and compaction properties of the produced concrete. Experimental investigations have shown that the length of the induction period can vary greatly. The duration of this process stage is particularly influenced by the properties of the C3S, the reaction temperature and the addition of substances that accelerate or retard the process.

The reasons for the temporal delay of the main hydration due to the occurrence of an induction period are contentious. Early researchers assumed that the formation of a hydrate envelope around the C3S particles is responsible. They also came to the conclusion that the first hydration product is a metastable calcium silicate hydrate, which is transformed in a second step into C-S-H as a stable end product [2, 3]. However, at that time it was not possible to prove the formation of this intermediate product by experiment [4]. Later, various spectroscopic methods were employed in order to provide such proof [5-9]. These analyses revealed that various chemical and physical modifications take place on the surface. A particularly important discovery was that the ­primary hydrate phases contain uncondensed silicate tetrahedrons (monomers), while the stable ­C-S-H phases contain dimers and short chains, i.e. condensed silicate compounds. Although these studies succeeded in providing proof of an intermediate compound, they could not show that this covers the entire surface of the C3S. As a result, the formation of a complete envelope (Fig. 2) was not proven and it was also possible to alternatively explain the spectroscopic findings by the presence of clusters of the intermediate phase on the surface of the C3S (Fig. 3). For this reason, alternative mechanisms were proposed for the existence of the induction period. One model postulated the precipitation of nuclei of the stable C-S-H phases as early as the first minutes of the process. All further kinetic steps were attributed to modification of conversion rates of the solution-precipitation reaction due to the composition of the pore solution and the size of the available growth surface [10]. One other hypothesis holds that the reaction speed is dependent on the dissolution speed of the C3S, which is itself influenced by the density of defects in the crystal lattice of the C3S and by the composition of the solution [11].

This article describes experimental investigations aiming to prove the existence of an intermediate compound in the hydration of C3S. The method employed was to concentrate this phase and perform analysis by means of nuclear magnetic resonance spectroscopy. In a further investigation the surface of the C3S was studied during the hydration process by means of X‑ray photoelectron spectroscopy. This had the objective of ascertaining whether the entire surface of the C3S is really covered by an envelope of the intermediate product. The achieved results form the basis for discussion of the energetic fundamentals of C3S hydration.

2 Proof of an intermediate phase by means of nuclear

resonance spectroscopy [13]

The formation of an intermediate phase as a cover on the C3S particles is difficult to prove spectroscopically, as it only occurs in low concentrations. At a specific surface of 4000 cm²/g for the C3S and at an assumed layer thickness of 5 nm, an intermediate phase concentration of 0.5 % by mass would be expected in the total sample. If the surface is increased while the layer thickness remains the same, the concentration of the metastable intermediate product rises, making the intermediate product easier to verify. For this reason, a material with very large specific surface and thus very small particle size was produced prior to the in­vestigations.

For the investigations, pure C3S was ground in isopropanol to a fineness of approximately 21 m²/g (BET). The ground product contained particles with a diameter of between 50 and 200 nm. The formation of the intermediate phase was investigated after a very short hydration period. Due to the high fineness value, a water to solid ratio of 1.2 was needed for the production of a  workable paste. After a hydration period of 5 minutes the reaction was thermally halted. The hydrated sample and the non-hydrated sample were analysed using various methods, including thermal analysis, X-ray diffraction, nuclear resonance spectroscopy and electron microscopy [13]. This article is mainly concerned with the results of the nuclear magnetic resonance spectroscopy (NMR). Using 29Si MAS NMR, differences in the chemical environment of the silicon nucleus can be measured. The coordination, the degree of condensation and the mean Si-O distance influence (to various extents) the magnetic fields in the vicinity of the investigated nuclei and thus modify the chemical shifts in the NMR spectrum. The single pulse spectra were acquired at a magnetic field strength of 9.4 T (Varian INOVA-400) and a flip angle of 45° in rotors with a volume of 220 µl. The spectral width was reduced and rotation sidebands were avoided by rotating around the magic angle (MAS).

Figure 4 shows the results of the NMR ­investigations. The triclinic crystal structure of C3S contains 9 different silicon lattice sites, which normally lead to the detection of 8 NMR peaks, with one peak showing ­double the intensity of the others. By contrast, the NMR spectrum of the non-hydrated, finely ground C3S (Fig. 4, top) displays very broad resonances. It is impossible to distinguish the individual lattice sites. This is presumably due to the small particle sizes, which cause extreme structural disorder leading to different Si-O bond lengths. After a hydration period of 5 minutes, only slight changes in the single pulse spectrum can be observed (Fig. 4, centre). One particular feature is the absence of any indication for the presence of condensed silicon tetrahedrons (Q1 and Q2), which normally occur in C-S-H. The NMR investigation only verified the presence of non-condensed silicon species (Q0).

The additional recording of 29Si{1H} cross polarization (CP) spectra shows that a large proportion of the silicon tetrahedrons are in close contact to hydrogen nuclei, as direct transfer of the magnetization from 1H to 29Si is possible. This indicates that a high proportion of the silicon is already present in the form of calcium silicate hydrate. However, this phase is not the stable C-S-H with condensed silicon tetrahedrons, but of a phase containing silicon in monomer form (intermediate phase). The degree of hydration can be calculated from the CP spectrum after experimental determination of the CP gain factor under identical conditions in an ­inversion-recovery experiment. It was calculated with the aid of this value that after a hydration period of only 5 minutes the sample consisted of 79 % intermediate phase and 21 % C3S. In this sample, no stable C-S-H phases as end product of the reaction were detected. ­Additional analyses of other samples showed that in the further course of hydration a transformation of the intermediate product into C-S-H can be detected, indicating that it is really a metastable compound.

The described experiments proved that if the initial material has a very large surface, a large quantity of intermediate phase can be formed. However, it is not possible to conclude from these experiments whether the entire surface of cement particles of normal fineness is completely covered, or whether the formation of the intermediate phase is responsible for the reduction in reaction speed during the induction period.

3 Investigation of the degree of surface

covering by XPS [14]

X-ray photoelectron spectroscopy was employed on order to study the C3S-surface. This method involves exposing the sample to monochromatic X-ray radiation, which causes the generation of photoelectrons. Although the X-ray radiation penetrates relatively far into the sample, the method is surface sensitive, because the photo-electrons from depths greater than 10 nm are largely absorbed. The individual binding energy of the emitted electrons can be determined from the kinetic energy of the photoelectrons and the wave length of the employed X-ray radiation. The electron binding energy can be used for identifying the element and the electron shell. Moreover, it allows the derivation of information regarding the binding with neighbouring atoms.

It was already known from other investigations that the binding energy of Si2p electrons in C3S is approximately 100.8 eV [15]. After the transformation to C-S-H phases, Si2p binding energies of between 102.0 and 102.5 eV [16] were measured. These are relatively easy to distinguish from those of C3S. Furthermore, there were indications that the Si2p electrons in the intermediate phase also possess higher binding energies than those in C3S [16]. This experimental method has therefore been verified as both phase sensitive and surface sensitive, which makes it suitable for the investigation of the degree of covering of the C3S surface in the early stage of hydration.

The objective of the described investigations was to determine the proportion of the surface that is covered by the intermediate phase during the induction period. For this purpose, three samples were analysed - two reference samples (non-hydrated C3S, intermediate phase) and one sample from the early stage of the hydration process. To produce the non-hydrated reference, C3S was pressed into tablet form and thermally treated at 1500 °C prior to the analysis. The tablet was broken in the high vacuum of the XPS instrument in order to assure analysis of a fresh, non-hydrated surface. The intermediate phase (reference 2) was produced from nano-C3S analogously to the already described NMR analyses, as those analyses had shown that such samples consist almost completely of intermediate phase. For the actual sample, a C3S with a long induction period was selected (Fig. 1) and the hydration was terminated after 30 minutes by washing with isopropanol.

The XPS analyses were performed in a device (S-Probe) supplied by Surface Science Instruments, equipped with an Al X-ray tube. Different charges in the individual samples were corrected by referring the spectrum to the C1s binding energy of 248.80 eV.

The Si2p binding energies of the two reference samples are shown in Figure 5. It can be seen that the intermediate phase and the non-hydrated C3S display different Si2p binding energies. However, these partially overlap due to the relatively high half width. Correspondingly, a relatively wide signal is obtained for the actual sample. This signal can be split into the contributions of the two references (non-hydrated C3S, intermediate phase) (Fig. 6). From this, the proportions of C3S and intermediate phase in the analysed volume can be calculated. Three points of the sample were analysed. Mean contents of 56 % intermediate phase and 44 % C3S were determined. No indication of the presence of stable C-S-H phases was detected. In summary, a very high concentration of intermediate phase was detected on the surface of the C3S at a very low degree of hydration (less than1 % by mass). For evaluation of the experimental findings, various geometric situations which would lead to a concentration of 56 % intermediate phase and 44 % C3S in the analysed volume were taken into consideration (Fig. 7). The minimum degree of covering is 56 %, but in this case relatively high islands or clusters of intermediate phase should be visible on the C3S surface (Fig. 7B). Lower layer thicknesses would require a higher degree of covering (Figs. 7C-7E). A homogeneous layer thickness of approx. 2 nm and a complete covering layer would also produce the stated ratio of intermediate phase to C3S in the analysed volume (Fig. 7F). High-resolution scanning electron microscopy showed which of the possible geometric situations of Figure 7 is actually correct. Figure 8 shows a corresponding electron micrograph. It can be seen that the surface of the C3S does not show the humps or surface steps that were assumed in Figures 7B to 7E. The roughness of the surface shown in Figure 8 is less than 2 nm, which permits the assumption that not only a large proportion of the C3S surface is covered, but that there is in fact a complete covering layer of intermediate phase. This confirms earlier models [2, 3, 12] and the schematic representations based on them (Fig. 2).

4 Thermodynamic calculations for the hydration of C3S

With the aid of thermodynamic calculations it is possible to predict the driving force of a chemical reaction (change in Gibbs free energy) and the emitted or absorbed heat of reaction (change in enthalpy). These calculations reveal that C3S has a very high driving force (∆rG°=-84.4 kJ/mol) and a very high heat of reaction (∆rH°=-124.0 kJ/mol). These data are based on the assumption that the reaction takes place in a single step. However, the described experimental results prove that it is in fact a consecutive reaction. In the first step an intermediate phase is formed, and this is transformed in the second step into the stable end product. This means that the thermodynamic calculation has to be correspondingly modified so that the formation of the intermediate phase is also taken into consideration. Unfortunately, no reliable thermodynamic data are available for this (highly disordered) compound, so that such a calculation has to rely on solubility data from the literature (product B in [2], kinetic path in [4]). The results are presented in Figure 9. The reaction of C3S with water to form the intermediate phase proves to be by far the greatest contribution to the entire change in energy (> 90 %!). Compared to that, the second reaction makes a far smaller energetic contribution. This smaller energetic contribution is also associated with a slower reaction, as high-energy reactions generally proceed far quicker than low-energy reactions. Moreover, it can be deduced that the second reaction determines the speed of the C3S hydration, as the slowest kinetic step is decisive for the kinetics of the overall process. As a result, a major portion of the total energy cannot be used for the acceleration of the chemical reaction of C3S with water. The effects of this portion are restricted to a significant increase in the heat of reaction. This implies that it must be possible to produce reactive binding agents with significantly lower energy content. This applies, for instance, to the production of Celitement. During the production of this binding agent a crystalline calcium silicate hydrate is mechanically/thermally treated and thereby activated. Compared to C3S, hydration of this binding agent takes place at a substantially lower energy level.

5 Derivation of model concepts for C3S hydration

The reaction of C3S with water possesses a high driving force in the form of Gibbs free energy. This compound correspondingly displays a very high solubility in water. Moreover, the dissolution rate of the mineral is very high [19, 20]. As quickly as one second after mixing with water a supersaturation with respect to the C-S-H is reached, so that this phase should crystallize out of the pore solution. However, the formation of C-S-H demands condensation of the silicate tetrahedrons, which is a relatively slow process. For this reason, it is possible for the dissolution process to continue even beyond the solubility limit of C-S‑H, so that the ion concentrations in the pore solution continue to rise, resulting in the supersaturation with respect to other less stable calcium silicate hydrates. This also includes calcium silicate hydrates with non-condensed silicate tetrahedrons, which precipitate first for kinetic reasons. In accordance with Ostwald’s rule of stages, metastable compounds with a simple structure are formed first and are later transformed into the stable end products of complicated structure in a second step. The largest proportion of the Gibbs free energy is already consumed during the first partial reaction of C3S to a metastable calcium silicate hydrate (Fig. 9) and this step progresses very quickly. Clearly, a heterogeneous nucleation occurs on the surface during this process, and the intermediate phase preferably forms on the non-hydrated C3S. In the course of this, the C3S and the solution become completely separated by a thin layer of hydrate (approx. 2 nm) in a similar manner to the formation of a passivation layer observed on metals. Subsequently, the solution enters a state of thermodynamic equilibrium with the intermediate phase. There is a slight supersaturation with respect to the C-S-H. However, this supersaturation is so slight that no immediate formation of nuclei can take place and this is the reason for the observation of an induction period prior to the main hydration stage. The main hydration can only commence when nuclei of the stable ­C-S-H phases have formed. This process is principally dependent on the supersaturation, the temperature and the available amount of surface with a high affinity for heterogeneous nucleus formation [13]. The length of the induction period can be correspondingly shortened by adding suitable substances, increasing the temperature and the provision of other factors. Nucleation is followed by crystal growth, the speed of which is primarily influenced during the acceleration period by the specific surface and the addition of accelerating and retarding substances. This process also takes place on the surfaces of the particles. While C-S-H continues to grow, the rim of hydration products around the anhydrous cores of the C3S-particles becomes denser over time, causing retardation of the transformation of intermediate phases into C-S-H, i.e. delaying the second partial step of the process. This corresponds to the commencement of the deceleration period and has the result that larger particles still have an unreacted core after a long period of hydration.

6 Summary

The reaction of C3S with water is a high-energy process. This article presented experimental evidence for the formation of an intermediate compound with uncondensed silicate tetrahedrons during the hydration process. It also showed that the entire surface of the C3S is already covered by this intermediate phase shortly after contact with water. The hydration of C3S is thus demonstrated to be a consecutive reaction proceeding in two steps.

Due to the formation of an intermediate phase on the surface directly after mixing with water, an induction period (dormant period) is observed prior to the main hydration process. This induction period is terminated by the heterogeneous nucleation of the stable end product.

The first reaction already involves more than 90 % of the driving force of the overall reaction. A substantially lower change of energy is available for the second step, which therefore proceeds significantly more slowly.

The described model concepts can serve as the basis for the development of binding agents with a significantly lower energy content and consequently lower specific carbon dioxide emissions. Furthermore, the overall reaction of C3S with water can be accelerated by shifting the shares of energy between the two reactions.

7 Acknowledgements

The authors herewith express their gratitude to Prof. J. Skibsted (Aarhus, Denmark) for the performance of 29Si-NMR analyses. All electron micrographs were produced by Dr. B. Möser (Weimar). The XPS analyses were performed by A. Sidorenko and Dr. J. Meinhard of the Fraunhofer-Institut für Silikatforschung (Würz­burg).

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