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Cement Clinker Modified by Photocatalyst – Selected Mechanical Properties and Photocatalytic Activity during NO and BTEX Decomposition
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29 August 2024
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29 August 2024
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Abstract
In this paper, a new way to obtain photoactive cements was presented. In this method amorphous TiO2 is added to cooler during the cooling of the cement clinker (Górażdże company) during cement production. Amorphous TiO2 was taken from the installation for obtaining titanium dioxide using the sulphate method. During the studies amorphous TiO2 was added to clinker at different temperature 300, 600, 700 and 800 °C. The properties of the obtained cement were tested during the bending and compressive strength and beginning and the end of bending setting time measurements. The adhesion of the obtained materials to concrete block, ceramic brick and plasterboard were also evaluated. The photocatalytic activity of the obtained materials was studied during NO and BTEX (benzene, toluene, ethylbenzene, p-,m-,o-xylenes decomposition) decomposition. Cement with 5 wt.% TiO2 added to clinker at 700 C had the highest photocatalytic activity and the best mechanical properties.
Keywords:
Subject: Engineering - Civil Engineering
1. Introduction
Photocatalysis is called reverse photosynthesis. During photosynthesis from carbon dioxide and water, organic compounds are produced, during photocatalysis organic compounds are decomposed to carbon dioxide and water. This advanced oxidation process is used to modify the surface of building materials to give them self-cleaning and air purification properties. Plasters, glass panes or photoactive paints are very often used. Large surface structures as well as the lack of need for additional intervention after the use of photoactive cladding, cause that photocatalysis arouses increased interest [1, 2]. The most current way to give photocatalytic activity to building materials is to coat their surface with special paints. Currently, however, photoactive cements, which could be used to obtain photoactive plasters without the need to cover them with additional layer paint, are beginning to enjoy great interest. Such photoactive cements can also be used for architectural cladding.
Photoactive cements are obtained by adding several types of photocatalysts to the finished cement, such as TiO2 [3, 4]. After addition of nano-TiO2 (NT) into cement-based composites, the induction period increased from 1.62 h to 2.83 h. NT itself does not have hydration capacity and and the incorporation of TiO2 reduces the Ca2+ concentration in the solution and delays the nucleation of Ca(OH)2. The hydration process of cement pastes mixed with NT particles consists of three processes: nucleation and crystal growth (NG), interaction at the phase boundary (I), and diffusion (D). NT particles can promote cement hydration in NG process, but reduce cement hydration rate in I and D processes. Another photocatalysts added to cement is SnO2 [5]. Addition of these photocatalysts is responsible for the self-cleaning characteristic observed in these new building materials. Another material for cement modification is BiVO4 [6]. Bismuth vanadate (BiVO4)-cement composites were coated on concrete surfaces. The photocatalytic activity of these composites was tested during the Methylene Blue dye degradation. These experiments showed that the 40 wt.% BiVO4-concrete pellets attained ~ 58% MB dye degradation efficiency. There are also cements with addition of CeO2 [7]. The addition of CeO2 nanoparticles promotes the creation of C–S–H gel which is the main hydration product which controls the mechanical properties of materials.
Presently cement is produced mainly by dry method. In the past wet method was also used. This dry method involves introducing cement flour into a kiln to produce clinker. The temperature used in the preparation of cement clinker is 1450-1500°. After leaving the furnace the hot clinker is passed through a cooler. However, a high rate of clinker cooling between the temperature of the burning zone and about 1200°C is important if the best strength-giving properties [8]. In the cooler there is a temperature between 1200 ° and 100°C. Czas przebywania klinkieru w chłodniku wynosi około 30 minut. In the case of obtaining photoactive cements, cooler seems to be the best place to introduce amorphous TiO2. The aim of the study was to check at what temperature it is best to introduce amorphous TiO2 into the cooler and whether the time spent 30 minutes in the cooler is sufficient for the formation of a photoactive structure of TiO2.
2. Materials and Methods
2.1. Modified Cements Preparation
An intermediate product from the titanium dioxide production plant by sulphate method (amorphous TiO2) was added to cement clinker (Górażdże). Cement clinker was heated up to 300, 600, 700 and 800 °C. The amount of amorphous TiO2 was 1, 3 and 5 wt.% of the clinker weight. After addition of amorphous TiO2 the 30 minutes cooling process took place. Modified cement clinker was ground together with 5 wt.% gypsum obtained from the flue gas desulphurization installation of the Dolna Odra power plant (Poland) for 35 minutes at a speed of 450 rpm. During cooling amorphous materials transferred into crystalline structure. The results of XRD analysis and sulfur content of amorphous TiO2 annealed at different temperatures in our earlier paper are presented [9]. The sulfur content in the TiO2 samples calcined at different temperatures was 2% by weight. The average size of TiO2 crystallites was 7-8 nm.
Table 1.
Designations of materials adopted in the studies.
| Designation | abbreviation | The temperature at which the clinker was heated [°C] | weight % of TiO2 to the weight of clinker | weight % of gypsum to the weight of clinker with TiO2 |
|---|---|---|---|---|
| clinker+5% gypsum | clinker | - | - | 5 |
| clinker-300°C-TiO2-1% | 300/1 | 300 | 1 | 5 |
| clinker-300°C-TiO2-3% | 300/3 | 300 | 3 | 5 |
| clinker-300°C-TiO2-5% | 300/5 | 300 | 5 | 5 |
| clinker-600°C-TiO2-1% | 600/1 | 600 | 1 | 5 |
| clinker-600°C-TiO2-3% | 600/3 | 600 | 3 | 5 |
| clinker-600°C-TiO2-5% | 600/5 | 600 | 5 | 5 |
| clinker-700°C-TiO2-5% | 700/5 | 700 | 5 | 5 |
| clinker-800°C-TiO2-1% | 800/1 | 800 | 1 | 5 |
| clinker-800°C-TiO2-3% | 800/3 | 800 | 3 | 5 |
| clinker-800°C-TiO2-5% | 800/5 | 800 | 5 | 5 |
2.2. The Beginning and End of the Setting Time Measurements
Vicata Vicatronic automatic devices was used for measurements. The value of W/C=0.30 (water to cement) was applied to all variants of the tested grouts. Two measurements of the beginning and end of the setting time were taken. The tests were conducted following the standard PN-EN 196-3:2016 [10]. The samples were stored under water at a temperature of 20±1 °C.
2.3. Determination of Bending and Compressive Strength of Standard Mortar
Walter+Bai equipment for strength measurements was used. The strength test was conducted based on the standard PN-EN 196-1:2016 [11]. A standard composition: 450 g of cement, 1350 g of standard sand and 225 g of water was used. The measurements were conducted at beams 4x4x16 cm. The value of W/C=0.5 was applied for all mortars. During first 24 hours the samples were stored in a water bath with increased humidity. After 24 hours, the samples were demolded and stored underwater until evaluated. The tests were performed after 28 days of puberty. The bending strength measurements Rf were performed on three beams, and the measurements of compressive strength Rc were performed on six specimens.
2.4. Adhesive Strength
The tests for the adhesive strength of cement mortars to the substrate were conducted in accordance with the requirements of the PN-EN 1015-12:2016 standard [12]. The tests covered ceramic, concrete and plasterboard surfaces. The surfaces of the substrate materials were mechanically dedusted and primed with an appropriate primer for the given material, and then moistened with water. For the tested cements, the standard mortar composition was used: 450 g of cement, 1350 g of standard silica sand and 225 g of water. A 10 mm layer of mortar was applied to the surface of individual materials, using side profiles to maintain the same thickness over the entire surface of the element. For each type of mortar, a minimum of four discs were prepared for a given type of substrate. The specimens were stored for 28 days in a climatic chamber with a temperature of 20±1 °C and RH > 95%. The day before the test, metal discs were glued to specific places on the surface using a two-component epoxy adhesive. The tests were performed after 28 days of the mortar curing on the surface of the substrate materials. The BPS F20D pull off device was used to break the mortar from the substrate.
2.5. Photocatalytic Activity Test
The photocatalytic activity of prepared cement plates towards the degradation of air pollution was also proved. The NO gas (1.989 ppm ± 0.040 ppm, Air Liquide, Poland) was used as model pollution. NOx removal was evaluated using the experimental installation, which scheme was presented in Figure 1.
Eight studied cement plates (one at dimensions of 2 × 2 × 0.5 cm) were placed in the central part of the cylindrical reactor (Pyrex glass; Ø × H = 9 cm × 32 cm). Used NO was diluted with humidified synthetic air to obtain 1 ppm and 0.2 ppm initial concentration, the flow rate through reactor was 500 cm3/min, gas temperature was 25 °C. The equilibrium of dark conditions reach after 35 minutes, then UV lamps were turned on for 30 min. The irradiation cumulative intensity of 100 W/m2 UV and 4 W/m2 Vis was used for measurements. T200 NOx analyzer (Teledyne, USA) was used for NO and NO2 measurements.
Two studied cement plates (one at dimensions of 8 × 4 × 1 cm) were placed inside the reactor (Heraeus type reactor UV-RS-2; Ø × H = 8 cm × 21 cm) with a medium pressure mercury vapor lamp (TQ-150, λmax = 365 nm, I = 146 W/m2). The irradiation time during photocatalysis process was 10 minutes. The BTEX mixture (benzene 5 ppm, ethyl benzene 5 ppm, toluene 5 ppm, o-,p-,m-xylene 5 ppm) (AG Gases & Equipment, Stoke-on-Trent, England) was diluted with humidified synthetic air in a ratio 1:1. The oxygen and water molecules were necessary for forming oxidative species, which are essential in photocatalytic reactions. The polluted air flowed through the reactor for 10 minutes at a rate of 500 cm3/min. After 10 minutes outlet and flow were stop. Smart SPME Arrow (phase type: Divinylbenzene(DVB)/Polydimethylsiloxane(PDMS), phase thickness 120 μm) were used for gases analysis. Smart SPME Arrow was introduced into the reactor for 2 minutes and after that to injector into the GC–MS apparatus (Nexis GC-2030, Shimadzu, Japan), which consisted of a single quadrupole mass spectrometer model QP2020 NX ISQ, (Shimadzu, Japan). A capillary column Zebron-PAH (30 m length, 0.25 mm I.D. The starting oven temperature was held at 45 °C for 2 min and ramped to 105 °C at a rate of 10 °C/min.
3. Results and Discussion
3.1. Mechanical Properties of Obtained Modified Clinker
In Table 2 the bending strength and compressive strength values of modified clinker ground with gypsum are presented. The bending strength slightly increased with increasing of TiO2 presence but close to unmodified material. The highest increasing of this value was 22% for materials 700/5. The compressive strength at 28 days of curing increased slightly with the TiO2 content, with this being especially notable in the sample with 5wt.% of TiO2. The highest value of compressive strength in the case of two modified clinker 600/1 and 600/3 addition of amorphous TiO2 decrease the bending strength about 2% and 8%, respectively. In other cases, the addition of amorphous TiO2 to the clinker during its cooling increased the bending strength from a slight 1% for material 800/1 to 25% for clinker 300/5.
3.2. The Beginning and End of the Setting Time Measurements
Addition of amorphous TiO2 during clinker cooling may be a good way for controlling the begging and end of the setting time As it can be observed in Figure 3, 5 wt.% addition of amorphous TiO2 increased the begging of setting time from 39 minutes for unmodified material to 87 minutes for material 300/5, to 79 minutes for material 600/5 and to 74 minutes for 800/5. In all prepared materials modification increased the beginning of setting time from 6 minutes (for 800/1) to 39 minutes (for 300/5). The same observed can be done for the values of the end of the setting time presented in Figure 4., 5 wt.% of amorphous TiO2 has the highest influence on increasing of this value of the end of the setting time, from 89 minutes for unmodified material to 135 minutes for 300/5, to 126 minutes for 600/5 and to 127 minutes for 800/5.
3.3. Adhesive Strength
The best photocatalytic activity during NO decomposition and remarkably high values of compressive and bending strength has material 700/5. For this material, the adhesive strength tests were done. Three different substrates, such as ceramic, concrete, plasterboard, the most used in construction, were selected to perform the adhesion tests. As can be seen in Table 3, the modification of TiO2 clinker resulted in an improvement in the adhesion of these modified materials to all tested surfaces. The increase in adhesion was highest in the case of concrete, as the addition of TiO2 improved adhesion by as much as 39%, and the lowest in the case of ceramics, as the addition of TiO2 improved adhesion by 21%.
3.4. Photocatalytic Activity Tests
3.4.1. NO Decomposition
The photocatalytic activity of the new photoactive cements was evaluated during the decomposition of NO(II) under UV radiation, the results in Table 4 were presented. During the tests, no influence of clinker temperature on the degree of NO decomposition was observed. In the case where the research was conducted at lower concentrations of NO, it follows that at 5wt, % of the TiO2 content the highest NO decomposition is achieved. The highest photocatalytic activity was achieved by the 700/5 material. During 30 minutes of UV exposure to eight plates of modified clinker in NO streams with a concentration of 0.2 ppm, the NO removal rate was 14.4%.
3.4.2. BTEX Decomposition
The photocatalytic activity was evaluated during BTEX decomposition. The mixture of benzene, toluene, ethyl benzene and xylenes were used. The obtained results in Figure 5 were presented. Initially, the gas mixture was passed through the reactor for 10 minutes to achieve the complete filling of the reactor space with the gas. After 10 minutes, the outlet and inlet of the gases was closed. A Smart SPME Arrow was introduced into the gas reactor and for 2 minutes the gases were sorbed on the bed. After 2 minutes, the Smart SPME Arrow was inserted into the chromatograph injector and subjected to 1 minute of desorption. The mass detector was used to measure gases concentration, obtained values were marked as the initial concentration, marked on the graph as 100%. Then, two plates made of unmodified clinker were placed in the reactor and the procedure of filling the reactor with gases and the procedure of determining the concentration with Smart SPME Arrow were repeated. As can be seen in Figure 5, ethyl benzene and xylenes have been adsorbed on the surface of the unmodified clinker in the amount of 7% and 13%, respectively. After adsorption studies, studies on photolysis in the presence of unmodified clinker and photocatalysis in the presence of modified clinker were started. After 10 minutes of UV light irradiation, as it can be seen in Figure 5, there was a partial desorption of gases from the clinker surface, which is particularly visible in the case of ethyl benzene, whose concentration increased by 4%. In addition, it can be noted that after switching on UV radiation, partial photolysis of gases (ethyl benzene and xylenes were decomposed) occurred, as there was a clear increase in the concentration of benzene (by 21%) and toluene by (27%). Since research on the breakdown of BTEX is expensive, only one material has been selected for these tests, which has the highest applicability. It is a material that was created because of the addition of 5wt% amorphous TiO2 to cement clinker at a temperature of 700°C. As can be seen in Figure 5, after 10 minutes of irradiation, the level of ethyl benzene (by 37%) and xylene (by 62%) was significantly reduced. There was an increase in benzene concentration (by 25%), the level of toluene remained unchanged. These results mean that in the process of photocatalysis, the ethyl group of ethyl benzene and methyl group of xylenes broke off, which resulted in an increase in the concentration of benzene. The increase in benzene concentration is not proportional to the decrease in ethylbenzene and xylenes concentrations, as benzene could have been oxidized, the formation of phenol, benzoquinone, and hydroquinone certainly also occurred the benzene ring breaking and the formation of decomposition products such as CO2 and CO [13-14].
5. Conclusions
The research has shown that the new method of obtaining photoactive cements can be used when clinkers from various manufacturers are used. In our previous research, we used Lafarge film clinker [9], the research presented in the article was conducted with the use of Górażdże clinker. In addition, we can see that the obtained photoactive cement can be used to remove volatile organic compounds from the air. After 10 minutes of irradiation, the level of ethyl benzene decreased by 37% and xylene decreased by 62%. In addition, the modification leads to a material that is characterized by higher adhesion to ceramics, concrete and plasterboard. Adhesion to concrete increased by 39%, adhesion to ceramics increased by 21% and adhesion to plasterboard increased by 30%.
Author Contributions
Conceptualization, M.J.; methodology, M.J., J.S. and E.K.-N.; formal analysis, M.J., J.S. and E.K.-N.; investigation, M.J., J.S., K.Z. and E.K.-N.; writing—original draft preparation, M.J; writing—review and editing, M.J.; visualization, M.J.; supervision, M.J.; project administration, M.J.; funding acquisition, M.J. All authors have read and agreed to the published version of the manuscript.
Funding
This research was funded by National Centre for Research and Development program Tango V (TANGO-V-A/0012/2021-00).
Data Availability Statement
The original contributions presented in the study are included in the article, further inquiries can be directed to the corresponding author.
Conflicts of Interest
The authors declare no conflicts of interest.
References
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Figure 1.
The scheme of installation to photocatalytic removal of NO (S – a source of pollution; M – mass flower; H – humidifier; R - photocatalytic reactor with irradiation source; A – NOx analyzer [9].
Figure 1.
The scheme of installation to photocatalytic removal of NO (S – a source of pollution; M – mass flower; H – humidifier; R - photocatalytic reactor with irradiation source; A – NOx analyzer [9].
Figure 2.
The scheme of installation for photocatalytic removal of BTEX (S – a source of pollution; M – mass flower; H – humidifier; R - photocatalytic reactor with irradiation source).
Figure 2.
The scheme of installation for photocatalytic removal of BTEX (S – a source of pollution; M – mass flower; H – humidifier; R - photocatalytic reactor with irradiation source).
Figure 3.
The beginning of the setting time of the modified clinkers.
Figure 4.
The end of the setting time of the modified clinkers .
Figure 5.
Photocatalytic decomposition of BTEX with under UV light irradiation .
Table 2.
The values of bending and compressive strength for modified clinkers.
| materials | The bending strength [MPa] | Standard deviation | The compressive strength [MPa] | Standard deviation |
|---|---|---|---|---|
| clinker | 5.24 | 0.11 | 35.27 | 0.88 |
| 300/1 | 5.57 | 0.02 | 36.20 | 1.67 |
| 300/3 | 5.38 | 0.04 | 34.17 | 1.44 |
| 300/5 | 6.56 | 0.50 | 42.67 | 1.66 |
| 600/1 | 5.12 | 0.39 | 35.17 | 0.63 |
| 600/3 | 4.83 | 0.30 | 30.57 | 1.73 |
| 600/5 | 5.95 | 0.29 | 41.04 | 0.82 |
| 700/5 | 6.41 | 0.19 | 41.53 | 2.37 |
| 800/1 | 5.37 | 0.14 | 33.95 | 1.83 |
| 800/3 | 5.30 | 0.22 | 35.32 | 0.78 |
| 800/5 | 5.63 | 0.21 | 38.56 | 2.03 |
Table 3.
The values of adhesive strength for modified clinkers .
| Materials | Adhesive strength [MPa] | |||||
|---|---|---|---|---|---|---|
| Ceramic | Standard deviation | Concrete | Standard deviation | Plasterboard | Standard deviation | |
| clinker | 1.598 | 0.333 | 0.787 | 0.200 | 0.486 | 0.071 |
| 700/5 | 1.932 | 0.323 | 1.287 | 0.176 | 0.630 | 0.044 |
Table 4.
Photocatalytic decomposition of NO with an initial concentration of 1 and 0.2 ppm under UV light irradiation .
Table 4.
Photocatalytic decomposition of NO with an initial concentration of 1 and 0.2 ppm under UV light irradiation .
| materials | NO decomposition [%] | |
|---|---|---|
| 1 ppm | 0.2 ppm | |
| Clinker | 2.0 | 2.7 |
| 300/1 | 3.7 | 5.9 |
| 300/3 | 5.2 | 7.0 |
| 300/5 | 3.0 | 7.8 |
| 600/1 | 5.0 | 6.0 |
| 600/3 | 7.4 | 7.8 |
| 600/5 | 8.3 | 9.5 |
| 700/5 | 6.0 | 14.4 |
| 800/1 | 4.8 | 7.6 |
| 800/3 | 5.5 | 5.0 |
| 800/5 | 5.1 | 10.9 |
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