The Effect of Vibro-Activation Time on the Properties of Highly Active Calcium Hydroxide

The results of studying the effect of the vibration processing time on the size of calcium hydroxide particles are given. The physicochemical processes affecting the size and morphology of calcium hydroxide particles have been studied. A stage-by-stage mechanism of the process of the carbonation of lime, depending on its specific surface, is established. The results show that the optimal period for the vibration treatment of lime to obtain the most active material is 20 min. A longer period of vibration results in the merging of particles into larger agglomerates.

Nanoparticles of hydrated lime have specific properties and, above all, a high rate of carbonation. During the treatment of cracks and damages in rocks with nano-lime suspension, a protective dense layer of calcium carbonate and portlandite is formed, increasing in volume, which contributes to the filling of free space and increasing of the strength of the stone [12]. The adhesion of the layer of the carbonized lime to the surface of the material increases as the process of carbonation develops [13]. At the same time, it should mentioned that the content of calcium hydroxide particles with sizes less than 100 nm in nano-lime is small, and therefore, the special properties of Ca(OH) 2 nanoparticles are not being fully exploited.
The technology for obtaining calcium hydroxide with particle sizes less than 100 nm is complex and characterized by high energy costs, which significantly restrains the widespread use of such lime. Research in this direction has been conducted by scientists from India, Italy, France, Canada, China, Spain, Iran, Malaysia and Qatar [2,[14][15][16][17][18][19][20][21][22][23][24][25][26] and aimed i.a. at studying the influence of the hydration environment on the characteristics of Ca(OH) 2 obtained. It has been found out that the most effective way to obtain Ca(OH) 2 particles with dimensions of 50-400 nm is the reaction between CaCl 2 and NaOH in the environment of ethylene glycol, polyoxyethylene, 1,2-propanol and 2-propanol [2,18]. When NaOH and Ca(NO 3 ) 2 ·2H 2 O interact in an aquatic environment at a temperature of 30 • C, it is possible to obtain nanoparticles of lime with sizes up to 200 nm [2]. It is claimed that in aqueous solutions, nanoparticles of lime are unstable, because they consolidate to form aggregates with sizes of up to 1-2 microns [27]. To stabilize the water suspensions of Ca(OH) 2 , it is recommended to introduce a certain amount of finely dispersed CaCO 3 . In this case, there is a physical and chemical interaction between the components, there is a change in the ζ-potential of calcium hydroxide, and the stability of the system increases.
The purpose of this work is to study the effects of the duration of vibro-treatment on the process of lime carbonation and study the physical and chemical processes that affect the size and morphology of Ca(OH) 2 particles.

Materials and Methods
In this work, hydrated lime was obtained by slaking the ground quicklime of the company Lhoist (Poland), type CL 90-Q, at a CaO/H 2 O ratio of 1:1. The contents of basic oxides in quicklime in % were as follows: CaO-91.9, MgO-1.6, the sum of active CaO+MgO-89.6, CO 2 -1.4 and SO 3 -0.2. The obtained paste-like mass of hydrated lime with a water content of 600 g in 1 kg of ready mixture was subjected to vibro-treatment with the use of a toroidal type vibro-activator operating in resonance mode. The frequency of fluctuations of the working chamber with blades was 25 Hz, and the amplitude of the fluctuations was 1.00-1.75 mm. The vibration processing time for different samples was changed from 10 to 45 min.
The granulometry of the original quicklime, its hydration products, and hydrated lime particles after vibrating treatment were studied with the Mastersizer 3000 laser diffraction particle size analyzer. The suspension used in granulometric studies was obtained by the dispersion of the obtained products in ethanol (98%) with the help of the ultrasonic processor VCX500 by SONIKS. The power of the processor was 150 W; the resonance frequency, 20-50 kHz; and the diameter of the conical generating nozzle, 6 mm. The processing time was changed from 1 to 5 min.
The BIOLAR-EPI optical microscope was used to study the results of processes occurring during the vibro-treatment of lime suspensions, to determine the size and shape of Ca(OH) 2 particles and to determine the crystallographic characteristics of crystals. To prepare samples for optical microscopy, lime suspension was prepared in ethyl alcohol (98%) or glycerol using an ultrasonic microwell nozzle with a diameter of 2 mm and a processing time of 30 s. The structure and morphology of portlandite crystals were also studied using the scanning electron microscope JSM-6010PLUS/LA InTouchScope.
The quicklime used in the work has a particle size of CaO from 100 nm to 500 microns. The number of CaO particles with sizes from 45 to 200 microns was the largest and was up to 55%. The number of CaO particles with sizes from 100 nm to 32 microns was much smaller-up to 28% (Table 1). When quicklime was slaked, the specific surface area almost doubled, and the largest number of formed particles were those with sizes of 0.1-32 microns. The study of the process of the carbonation of hydrated lime and the influence of the vibro-activation time on the speed of this process was also carried out. It was performed by a specially developed method. Samples in the form of cubes with an edge of 10 mm were prepared from lime paste with a constant water-lime ratio of 0.5 and were used for the testing. After 24 h from preparation, the samples were removed from the molds and stored for 48 h in a desiccator above the layer of soda lime (a mixture of sodium hydroxide and calcium oxide, which absorbs moisture and carbon dioxide from the air). At the same time, the weight of the samples was constantly controlled by means of weighing on the electronic scales with an accuracy of ± 0.01 g. After 72 h from the beginning of sample preparation, they were attached on one side to a pre-weighed metal plate. The plates with samples were placed in a thermostatic chamber with a temperature of 20 ± 2 • C and a controlled relative humidity of 70 ± 5%. After placing the samples in the chamber, weighing was performed every 12 h. The weight gain of the samples was taken as the formed amount of calcium carbonate according to the reaction Ca(OH) 2 + CO 2 ↔ CaCO 3 + H 2 O.

Results
The average diameters of quicklime particles, hydrated lime particles and also hydrated lime particles activated at different times were calculated. As can be seen in Table 2, quicklime is characterized by a high content (1.95%) of ultra-disperse fraction of size less than 0.5 microns in comparison with other tested forms of lime. It is worth noting that the hydrated lime fraction of 1 µm is equal to 1.26%, and this is the lowest content of particles of this size in all the cases. In the process of the activation of hydrated lime, 10 and 20 min-long processing increased the content of particles up to 1 micron by 2.3 and 6.0 times, respectively. In the case of lime activated for 20 and 45 min, the fractions up to 0.5 µm are 0.23% and 0.14%, respectively. The effective diameters of d10, d50 and d90 for hydrated lime activated for 10 min were 1.56, 6.27 and 55.6 µm, respectively, while for lime activated for the optimal time (20 min), these diameters were reduced by 1.2-1.7 times.
Commonly used parameters, calculated automatically by the Mastersizer 3000 laser diffraction particle size analyzer software, were used to describe the granulometry results. The mean diameters D [4; 3] and D [3; 2] are defined by Equations (1) and (2): in which v i is the percentage of the volume of particles with an average diameter of D i in the total volume occupied by the tested sample. The effective diameters d10, d50 and d90 are calculated as the 10th, 50th and 90th percentiles of the particle volume distribution in the sample. The fraction content is calculated as cumulative sum of the volume of particles whose diameters are lower than the values given in the table. The calculated average volume diameter of D [4; 3] for quicklime is 89.7 µm, and for hydrated lime it is 25.4 µm, while in case of lime activated for 10 to 45 min, it varies between 3.93 and 3.24 µm. The maximum average diameter D [3; 2] of the particle distribution over the specific surface area for quicklime is 6.63 µm, while for hydrated lime, it is reduced 1.3 times, and for hydrated lime activated at the optimal time, by 2 times.
As can be seen in Figure 1, hydrated lime, as well as activated lime, is characterized by a bimodal distribution of particle dimensions. For hydrated lime, the amount of fine lime within the range of 0.75-10 µm was 52.53 vol%, and for lime activated for 10-15 min, the amount of fine lime particles  As can be seen in Figure 1, hydrated lime, as well as activated lime, is characterized by a bimodal Upon the interaction of lime with water, there is a transformation of the cubic crystal lattice of CaO into a hexagonal one for Ca(OH) 2 . The reaction proceeds mainly through the topochemical mechanism [28] with the formation of crystals in the form of hexagonal plates. The overwhelming majority of the hydrated lime formed is particles with sizes of 2-4 microns, which form larger aggregates with sizes of 30-40 microns as a result of attraction due to Van der Waals forces.
In the study of calcium hydroxide suspension in an optical microscope (Figure 2), it is seen that Ca(OH) 2 particles with sizes of 2-4 microns as a result of Van der Waals forces are connected by dipoles, forming a spatial grid. Smaller particles form chains of complex configuration. After vibro-treatment, their size decreases by 2.0-3.5 times, and at the same time, there is a complete destruction of the structure and alignment of the particle size.

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In the study of calcium hydroxide suspension in an optical microscope (Figure 2), it is seen that   After the increase in the time of vibro-treatment of hydrated lime from 20 to 45 min, the increase in the size of particles due to their aggregation is observed. At the same time, the maximum volume average diameter of D [4; 3] increases significantly (from 11.7 to 20.3 microns), and the maximum size of aggregated particles increases from 70 to 230 microns. These are undesirable phenomena, hence the conclusion that extending the vibro-activation time beyond 20 min is not advantageous.
Thus, the maximum vibrating time is 20 min. Further increases in time do not have a positive effect. For example, in the case of a 45-min vibrating process, the inverse effect occurs-the consolidation of activated lime particles. This can be explained by the fact that hydrated lime in the aquatic environment has dipole properties, but during long-term vibro-treatment, there is a process of destruction of dipoles, a redistribution of charges on their surface and their subsequent secondary grouping [29].
Unlike the structure, the configuration of the particles after the vibrating treatment practically does not change (Figure 3), and only the destruction of individual units occurs, which is accompanied by a general reduction in the size of the particles. Furthermore, it is shown that the vibro-treated lime is characterized by higher chemical activity (as shown by the example of the carbonation process) than lime, which was not treated in such a way.
In this paper, we also studied the process of the carbonation of samples obtained from calcium hydroxide with different activation times. It is known that the process of lime carbonation is accompanied by an increase in its mass. It allows the investigation of the process of the interaction of lime with CO 2 from air by the gravimetric method. The specific feature of this method is the holding of samples at constant humidity and temperature, and the control of the sample mass. The main disadvantage of this method is that measurements can be made only after 72 h from preparation of the samples. It is connected with the fact that during this time, as established by us, there is a complete evaporation of water and stabilization of the sample mass.

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The studies were carried out on cube specimens with a 10 mm edge. The specimens after curing The studies were carried out on cube specimens with a 10 mm edge. The specimens after curing for 72 h were attached to a pre-weighed metal plate with one side. The plate was placed in a thermostatic chamber with a constant temperature of 20 ± 2 • C and controlled relative humidity of 70 ± 5%. The mass of the samples was measured every 12 h.
As can be seen from the diagram of the dependence of mass growth (Figure 4), directly related to the effect of carbonation on the aging time, the process of calcium hydroxide carbonation, obtained by the hydration of CaO, after 20 days is practically stopped, reaching avalue of 3.1%. At the same time, all the samples after vibration treatment are characterized by a stable increase in mass up to 100 days of aging. From the course of the carbonation process, it can be concluded that the most active is calcium hydroxide after 20 min of treatment in the vibro-activator. A further increase in vibro-treatment time does not lead to an increase in the activity of calcium hydroxide particles.

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In this paper, we also studied the process of the carbonation of samples obtained from calcium

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The studies were carried out on cube specimens with a 10 mm edge. The specimens after curing  Such characteristics of calcium hydroxide carbonation are associated with the mechanism of lime carbonation [30,31], which occurs in several stages. At the first stage, calcium carbonate is formed on the surface of lime grains in the form of a dense layer as a result of the interaction of H 2 CO 3 and Ca(OH) 2 , which is a reaction taking place at the boundary of contact of liquid and solid phases.
Later on, in the presence of CO 2 in the air, calcium carbonate passes into calcium hydrocarbonate Ca(HCO 3 ) 2 .
The second stage is the interaction between the CaОН + and CaНCО3 + ions in the liquid phase. In this case, the lime grains are blocked and the reaction slows down. This can be explained by the fact that the determining factor in the interaction of calcium hydroxide and carbon dioxide is the specific surface of hydrated lime.

Conclusions
The vibro-processing of lime paste makes it possible to obtain lime of significantly increased activity and a noticeably finer grain size that accelerates the process of carbonation and increases the depth of conversion of hydroxide into calcium carbonate.
Changes in the duration of the vibration treatment of samples significantly affect the activity of calcium hydroxide particles. Thus, the optimal time for the vibrating treatment of hydrated lime is 20 min; its further increase is not effective, because the activity of Ca(OH) 2 is significantly reduced and the particles tend to form larger agglomerates.
Such a feature of the vibro-activated lime can be used for the deep cleaning of gas media from carbon dioxide, as well as other harmful products (e.g., SO 2 ), i.e., when the reaction between Ca(OH) 2 and the gas reagent takes place according to the scheme of the homogeneous heterophase process.