# New Surface Properties in Porcelain Gres Tiles with a Look to Human and Environmental Safety

Authors: C. L. Bianchi; C. Pirola; S. Gatto; S. Nucci; A. Minguzzi; G. Cerrato; S. Biella; V. Capucci
Journal: Advances in Materials Science and Engineering
 (2012)

---

## Abstract

Traditional photocatalysis is here brought forward for both the use of nanosized TiO2 crystallites and the possibility to have a release of TiO2 particles during the final use of the manufactured products. In the present paper both the preparation and characterization of a new generation of photocatalytic tiles are presented. The originality of these products is the surface presence of microsized TiO2 as it is not clear yet the impact of the nanoparticles on both human and environmental safety. TiO2 is here mixed with a silica compound and the final thermal treatment at 680°C allows the complete surface vitrification which, in turn, makes the tiles surface strongly resistant to abrasion. Photocatalytic efficiency towards the degradation of NOx in gas phase was measured in both a batch and a plug-flow reactor. The latter reactor configuration was also modeled by digital simulations.


---

## Body

## 1. Introduction

Porcelain gres tiles are characterized by a very low water absorption rate (less than 0.5%) and are manufactured under high pressure by dry-pressing fine processed ceramic raw materials with large proportions of quartz, feldspar, and other fluxes. Afterwards, the body of these materials is fired at very high temperatures (1200–1300°C) in kilns [1]. The final material is thus characterized by lack of porosity, complete water-proofing, durability, hardness, wear resistance properties, and a complete frost resistance.In the past decades porcelain gres tiles underwent significant transformations in terms of appearance and size. At the beginning of the industrial productions, porcelain gres tiles were considered as just a technical material characterized by strong resistance to both abrasion and acid attack, almost lack of porosity, but aesthetically not very beautiful. Today thanks to new industrial production methods, both properties and beauty of these materials completely fit the market requests. In particular, the possibility to prepare slabs of large sizes is the new frontier of building materials.Beside these noteworthy architectural features, new surface properties have been introduced in the last generation of these materials. The present paper reports the preparation and characterization at the base of a new kind of fired tiles able to reduce polluting molecules present in air thanks to its new photocatalytic properties. The extreme originality of these products is the surface presence of microsized  TiO2. In fact it is not clear yet the impact of the possible release in the atmosphere of nanoparticles, in particular nano-TiO2, on both human and environmental safety.Man-made nanostructured materials such as fullerenes, nanoparticles, nanopowders, nanotubes, nanowires, nanorods, nanofibers, quantum dots, dendrimers, nanoclusters, nanocrystals, and nanocomposites are globally produced in large quantities due to their wide potential applications, for example, in skincare and consumer products, healthcare, electronics, photonics, biotechnology, engineering products, pharmaceuticals, drug delivery, and agriculture. Human exposure to these nanostructured materials is inevitable, as they can enter the body through the lungs or other organs via food, drink, air, and medicine and affect different organs and tissues such as the brain, liver, kidney, heart, blood, and so forth and may cause cytotoxic effects, for example, deformation and inhibition of cell growth leading to various diseases in both humans and animals. Since a very wide variety of nanostructured materials exists, their interactions with biological systems and possible toxicity largely depend upon their properties, such as particle size, concentration, solubility, chemical and biological properties, and stability [2].Titanium dioxide nanoparticles are manufactured worldwide in large quantities for use in a wide range of applications including pigment and cosmetic manufacturing. Although TiO2 is chemically inert, TiO2 nanoparticles can cause negative health effects, such as respiratory tract cancer in rats. Trouiller et al. [3] investigate TiO2 nanoparticles-induced genotoxicity, oxidative DNA damage, and inflammation in a mice model.The possibility to use Microsized  TiO2 in a commercial manufactured product opens a new generation of material intrinsically safer than the traditional photocatalytic products for both workers in the factories and public safety, even though, with such materials that are surface vitrified, the release of TiO2 particles is extremely remote.In the present paper both preparation and characterization of photocatalytic porcelain gres tiles are reported, as well as specific tests, in gas phase, to verify the effective photocatalytic efficiency of the samples. A comparison is initially reported between the photoactivity in the photodegradation ofNOx in gas phase of a pure commercial powdered nano-TiO2 (AEROXIDE TiO2 P25 by Evonik, P25 referred in the following) and the commercial powdered micro-TiO2 (1077 by Kronos) used as starting material in the present tiles preparation. A specific session of the present paper will be also devoted to the discussion about the experimental setup to employ when tiles have to be investigated for the NOx photodegradation in air with a plug-flow reactor built following the ISO 22197-1 rule [4].


## 2. Experimental

### 2.1. Preparation

Industrial porcelain gres tiles are manufactured under high pressure by dry-pressing fine processed ceramic raw materials with large proportions of quartz, feldspar, and other fluxes and finally fired at high temperatures (1200–1300°C) in a kiln.Photoactive porcelain gres tiles by GranitiFiandre S.p.A were subsequently covered at the surface with a mixture of pure anatase micro-TiO2 (1077 by Kronos) and a commercial SiO2-based compound. To ensure the requested product stability, at the end of the preparation procedure tiles were treated at high temperature (min 680°C) for 80 min and then brushed to remove the powder present at the sample surface and not completely stuck (samples name: Orosei Active). For the sake of comparison, samples were also prepared with the same procedure but without adding the photoactive oxide into the SiO2-based compound (Orosei).


### 2.2. Characterization

Specific surface area (SA) of powdered samples has been determined by conventional N2 absorption at 77 K (BET method) using a Sorptometer 1042 instrument (Costech). Before the analysis, the samples have been heated at 100°C for 12 h and then pretreated at 200°C in a nitrogen flow.HR-TEM images were obtained by means of a JEOL 3010-UHR instrument (acceleration potential: 300 kV; LaB6 filament) equipped with an Oxford INCA X-ray energy dispersive spectrometer (XEDS) with a Pentafet Si(Li) detector. Samples were “dry” dispersed on lacey carbon Cu grids.X-ray powder diffraction (XRD) patterns have been taken with a computerized Philips PW1710 diffractometer using the CuKα  radiation, operating at 40 kV and 20 mA, step scan 1 min−1, and 1 s counting time in the 2–40° range at room temperature.XPS measurements were performed in an M-Probe Instrument (SSI) equipped with a monochromatic Al Kα source (1486.6 eV) with a spot size of 200 × 750 μm and a pass energy of 25 eV, providing a resolution for 0.74 eV. The energy scale was calibrated with reference to the 4f7/2 level of a freshly evaporated gold sample, at 84.00±0.1 eV, and with reference to the 2p3/2 and 3s levels of copper at 932.47±0.1 and 122.39±0.15 eV, respectively. With a monochromatic source, an electron flood gun was used to compensate the buildup of positive charge on the insulator samples during the analyses: a value of 10 eV was selected to perform measurements on these samples.The surface wettability was evaluated by static contact angle (CA) measurements performed with an OCA20 instrument (DataPhysics Co., Germany) equipped with a CCD camera and a 500μL-Hamilton syringe to dispense liquid droplets. Measurements were made at room temperature (~22°C) by means of the sessile drop technique and were replicated at least 15 times on each sample. Ultrapure water (HPLC grade, Sigma-Aldrich) was used as probe liquids and the volume of drop was fixed at 2 μL. The Young-Laplace fitting method was used in the calculation of static contact angles for all measurements giving an experimental error of ±5% due to the surface roughness of the samples [5, 6] that was experimentally determined by a laser profilometry (3D laser profilometer, UBM Microfocus Compact, NanoFocus AG, Germany) with vertical and lateral resolution of 10 nm. The parameters used during measurements follow the standard DIN 4768 and were adopted a transverse line measurement of 17.5 mm and a density of 150 dots per mm.


### 2.3. Photocatalytic Tests

Pure commercial powders (P25 and 1007) were tested towards the photodegradation ofNOx in air in a static experimental setup already described in [7, 8] under the following conditions: RH: 50%, 10 Wm−2, Vreactor=20 L, with a NOx starting value of 1000 ppb. Immobilized particulate TiO2 layers (ca. 0.05 g) were prepared on glass sheets by deposition from a suspension of the oxide in isopropanol [9].Pure 1077 and P25 powders (always immobilized on a glass sheet) and tiles were tested towards the same reaction but in flowing conditions using a plug-flow reactor built following strictly the ISO 22197-1 rule [4] with an effective volume of 0.025 L. Experimental conditions were maintained as follows: RH: 40%, 20 Wm−2, [NOx]inlet 500 ppb, and 180, 32.4, 9, and 4.2 L h−1 total flow, respectively.A chemiluminescent analyzer (Teledyne Instruments M200E) was used to check the final conversion of the pollutant in both batch and plug-flow reactor setpus.The reactor configuration under flowing conditions was also modeled by digital simulations carried out using COMSOL Multiphysics 4.0a coupling the laminar flow (experimentally verified) with the transport of diluted species physics in a 3D space with each geometry resembling the relevant reactor dimensions and considering steady-state conditions. Each simulation was carried out using the following values:C0,in = 2.04 × 10−5mol m−3 (equivalent to 500 ppb of NOx); ρ=1.165 kg m−3 (air density at 30°C); μ=1.86×10-5 Pa s (air dynamic viscosity at 30°C); D = 1.9 × 10−5 m2 s−1 (diffusion coefficient of NO2 in air [10]).Simulations were performed considering six different inlet fluxes:Vin (4.2, 9, 20, 32.4, 100, and 180 L h−1) and three different apparent reaction rate values, two of them calculated on the basis of the experimental results obtained using two catalysts studied in this work (Orosei Active and pure 1077, resp.) at 32.4 L h−1 and the third calculated at 180 L h−1. A first-order kinetic was considered for the reaction, as usual in photocatalysis with reactants such as NOx at sub-ppm level [11, 12]. The apparent kinetic constant was determined by performing simulations varying kapp until the NOx conversion resembled the experimental one. After this, kapp was used for the remaining Vin values.The reaction on the catalytic surface was simulated by imposing an outlet flux of matter through the central surface that corresponds to the photoactive tile. The flux, expressed in mol m−2 s−1, is set as equal to kapp·[NOx]s (the subscript indicates that [NOx] at the catalyst surface is considered). It follows that the rate constant values found in this work do not coincide with the real values of the chemical rate constant for the considered reaction. The following values were obtained: kapp = 2.3 × 10−3m s−1 (Orosei Active) or 4 × 10-3m s−1 (pure 1077) at 32.4 L h−1 and kapp = 1.0 × 10-4m s−1 for both Orosei Active and 1077 at 180 L h−1.


## 2.1. Preparation

Industrial porcelain gres tiles are manufactured under high pressure by dry-pressing fine processed ceramic raw materials with large proportions of quartz, feldspar, and other fluxes and finally fired at high temperatures (1200–1300°C) in a kiln.Photoactive porcelain gres tiles by GranitiFiandre S.p.A were subsequently covered at the surface with a mixture of pure anatase micro-TiO2 (1077 by Kronos) and a commercial SiO2-based compound. To ensure the requested product stability, at the end of the preparation procedure tiles were treated at high temperature (min 680°C) for 80 min and then brushed to remove the powder present at the sample surface and not completely stuck (samples name: Orosei Active). For the sake of comparison, samples were also prepared with the same procedure but without adding the photoactive oxide into the SiO2-based compound (Orosei).


## 2.2. Characterization

Specific surface area (SA) of powdered samples has been determined by conventional N2 absorption at 77 K (BET method) using a Sorptometer 1042 instrument (Costech). Before the analysis, the samples have been heated at 100°C for 12 h and then pretreated at 200°C in a nitrogen flow.HR-TEM images were obtained by means of a JEOL 3010-UHR instrument (acceleration potential: 300 kV; LaB6 filament) equipped with an Oxford INCA X-ray energy dispersive spectrometer (XEDS) with a Pentafet Si(Li) detector. Samples were “dry” dispersed on lacey carbon Cu grids.X-ray powder diffraction (XRD) patterns have been taken with a computerized Philips PW1710 diffractometer using the CuKα  radiation, operating at 40 kV and 20 mA, step scan 1 min−1, and 1 s counting time in the 2–40° range at room temperature.XPS measurements were performed in an M-Probe Instrument (SSI) equipped with a monochromatic Al Kα source (1486.6 eV) with a spot size of 200 × 750 μm and a pass energy of 25 eV, providing a resolution for 0.74 eV. The energy scale was calibrated with reference to the 4f7/2 level of a freshly evaporated gold sample, at 84.00±0.1 eV, and with reference to the 2p3/2 and 3s levels of copper at 932.47±0.1 and 122.39±0.15 eV, respectively. With a monochromatic source, an electron flood gun was used to compensate the buildup of positive charge on the insulator samples during the analyses: a value of 10 eV was selected to perform measurements on these samples.The surface wettability was evaluated by static contact angle (CA) measurements performed with an OCA20 instrument (DataPhysics Co., Germany) equipped with a CCD camera and a 500μL-Hamilton syringe to dispense liquid droplets. Measurements were made at room temperature (~22°C) by means of the sessile drop technique and were replicated at least 15 times on each sample. Ultrapure water (HPLC grade, Sigma-Aldrich) was used as probe liquids and the volume of drop was fixed at 2 μL. The Young-Laplace fitting method was used in the calculation of static contact angles for all measurements giving an experimental error of ±5% due to the surface roughness of the samples [5, 6] that was experimentally determined by a laser profilometry (3D laser profilometer, UBM Microfocus Compact, NanoFocus AG, Germany) with vertical and lateral resolution of 10 nm. The parameters used during measurements follow the standard DIN 4768 and were adopted a transverse line measurement of 17.5 mm and a density of 150 dots per mm.


## 2.3. Photocatalytic Tests

Pure commercial powders (P25 and 1007) were tested towards the photodegradation ofNOx in air in a static experimental setup already described in [7, 8] under the following conditions: RH: 50%, 10 Wm−2, Vreactor=20 L, with a NOx starting value of 1000 ppb. Immobilized particulate TiO2 layers (ca. 0.05 g) were prepared on glass sheets by deposition from a suspension of the oxide in isopropanol [9].Pure 1077 and P25 powders (always immobilized on a glass sheet) and tiles were tested towards the same reaction but in flowing conditions using a plug-flow reactor built following strictly the ISO 22197-1 rule [4] with an effective volume of 0.025 L. Experimental conditions were maintained as follows: RH: 40%, 20 Wm−2, [NOx]inlet 500 ppb, and 180, 32.4, 9, and 4.2 L h−1 total flow, respectively.A chemiluminescent analyzer (Teledyne Instruments M200E) was used to check the final conversion of the pollutant in both batch and plug-flow reactor setpus.The reactor configuration under flowing conditions was also modeled by digital simulations carried out using COMSOL Multiphysics 4.0a coupling the laminar flow (experimentally verified) with the transport of diluted species physics in a 3D space with each geometry resembling the relevant reactor dimensions and considering steady-state conditions. Each simulation was carried out using the following values:C0,in = 2.04 × 10−5mol m−3 (equivalent to 500 ppb of NOx); ρ=1.165 kg m−3 (air density at 30°C); μ=1.86×10-5 Pa s (air dynamic viscosity at 30°C); D = 1.9 × 10−5 m2 s−1 (diffusion coefficient of NO2 in air [10]).Simulations were performed considering six different inlet fluxes:Vin (4.2, 9, 20, 32.4, 100, and 180 L h−1) and three different apparent reaction rate values, two of them calculated on the basis of the experimental results obtained using two catalysts studied in this work (Orosei Active and pure 1077, resp.) at 32.4 L h−1 and the third calculated at 180 L h−1. A first-order kinetic was considered for the reaction, as usual in photocatalysis with reactants such as NOx at sub-ppm level [11, 12]. The apparent kinetic constant was determined by performing simulations varying kapp until the NOx conversion resembled the experimental one. After this, kapp was used for the remaining Vin values.The reaction on the catalytic surface was simulated by imposing an outlet flux of matter through the central surface that corresponds to the photoactive tile. The flux, expressed in mol m−2 s−1, is set as equal to kapp·[NOx]s (the subscript indicates that [NOx] at the catalyst surface is considered). It follows that the rate constant values found in this work do not coincide with the real values of the chemical rate constant for the considered reaction. The following values were obtained: kapp = 2.3 × 10−3m s−1 (Orosei Active) or 4 × 10-3m s−1 (pure 1077) at 32.4 L h−1 and kapp = 1.0 × 10-4m s−1 for both Orosei Active and 1077 at 180 L h−1.


## 3. Results and Discussion

### 3.1. Sample Characterization

A feature comparison of both pure TiO2 and TiO2 + SiO2-based compound after the calcination treatment at 680°C shows the decrease of the surface area from 11.0 to 2.6 m2g−1 (BET measurements). From the surface point of view, XPS analysis reveals the classical Ti2p doublet at 458.6 ev (Ti2p3/2) attributed to Ti4+ with a Ti/Si ratio of 0.20.The formulation with the SiO2-based compounds and the following calcination step lead to a decrease of the surface area but preservation of the pure anatase form verified by XRD measurements [13]. As reported by Anderson and Bard [14], the presence of SiO2, together with TiO2, enhances the formation of hydroxyl radical  OH•, which would be achieved via strong Brønsted acid sites at the TiO2/SiO2 interface region. Such incorporation inhibits the crystal growth of TiO2 allowing the preservation of the anatase structure at high temperature [15].In order to investigate the morphological features of the various samples, HR-TEM technique has been resorted to. P25 nano-sized TiO2 has been also investigated, and its images are reported in Figures 1(a) and 1(b): it can be observed that the P25 material is made up of highly crystalline closely packed particles, as either thickness or Moirè’s fringe patterns are evident (right-hand image) [16] with rather smooth edges. The average particle size is in agreement with literature data [17], that is, 20–50 nm range. The detailed inspection of the spacings among the interference fringes (d = 0.357 nm) indicates that the most frequently exposed planes belong to the TiO2 (101) anatase polymorph [18]. If both particle size and ultimate morphology of the plain Kronos TiO2 sample (see Figures 1(c) and 1(d)) are compared to the P25 features, it can be evidenced that (i) particles are still packed, but to a limited extent if compared to the P25, and the edges of the particles are quite smooth; (ii) the size of the crystallites has enormously enlarged, as in the present case the average size varies in the 100–250 nm range; (iii) if we inspect the distances among the fringes, it is evident that the spacings (d = 0.357 nm) are still ascribable to the anatase polymorph. When the presence of the SiO2-based compound is considered, it can be stated that, roughly morphologically speaking, the main features of the TiO2 particles are maintained: see, for instance, Figures 1(e) and 1(f), in which the large dimensions of the particles are evident (50–200 nm range), beside rather smooth edges. Nevertheless, some peculiarities have to be mentioned: in particular, the presence of the SiO2-based compound is evident (see either the inset in Figure 1(e) or Figure 1(f)), in the form of either small protruding crystalline particles or an amorphous coating covering the TiO2 particles. In any case, the very thin nature of these particles and/or coating allows to inspect the fringe patterns located below, confirming that the spacings among the fringes are still ascribable to the anatase TiO2 polymorph.HR-TEM images of the various TiO2 materials. (a) and (b): P25. (c) and (d): 1077. (e) and (f): Orosei Active. (a), (c), and (e) refer to low magnification, here as (b), (d), and (f) to high magnification.
(a)
(b)
(c)
(d)
(e)
(f)Wettability measurements were performed on 15 different areas of both Orosei and Orosei Active (Figures2(a) and 2(b), resp.). Drop shapes are dramatically different enhancing a completely different surface. Orosei sample shows a mean contact angle value of 78.2°, while Orosei Active shows very hydrophilic surface features with an average angle of 23.0°. This very low value can be explained by the super-hydrophilic property of TiO2 photocatalyst as already observed by other authors [19]. In particular the copresence of TiO2 and SiO2 can lead to a modification of the angle value depending on the TiO2/SiO2 ratio [20] with values in the range of 20–25° with a SiO2 content at 70–80% (molar basis), in agreement with the XPS Ti/Si ratio obtained on Orosei Active.Contact angle: (a) Orosei; (b) Orosei Active tiles.
(a)
(b)Samples roughness, measured as root mean squared (Rq), was 19.354 μm and 18.860 μm for Orosei Active and Orosei (Ti-free), respectively.


### 3.2. Photocatalytic Tests

#### 3.2.1. Batch Reactor

Figure3 reports the rate of NOx degradation for P25 and 1077. The NOx concentration is the sum of the NO and NO2 concentrations; the general mechanism of NOx oxidation by photocatalysts implies the oxidation of the nitric monoxide to nitric acid or nitrous by active oxygen species produced on the TiO2 surface [21].Figure 3
Comparison between P25 (◆) and 1077 (■) in the NOx photodegradation in a batch reactor.P25 is, as expected, more efficient than 1077 and it reaches a fullNOx degradation (1000 ppb) in about 2 h. On the contrary, 1077 never reaches a complete NOx degradation within the 6 h of test but, notwithstanding the larger crystallite size and the lower surface area, shows a 90% conversion after 100 min of irradiation.


#### 3.2.2. Plug-Flow Reactor

ISO 22197-1 rule provides for very sharp experimental conditions such as an inletNOx concentration of 1000 ppb coupled with a low irradiation power (10 Wm−2) and mainly with a very strong flow at 180 L h−1. These conditions are too extreme for our samples being vitrified at their surface and having no porosity.For these reasons, the operating conditions have been softened cutting the inlet concentration by half (500 ppb), doubling the power irradiation (20 Wm−2), and investigating the role of the flow per hour on the final NOx conversion. To check to have maintained the correct fluid dynamic conditions, the Reynolds number was calculated:
(1)Re=ρUDeμ,
where U is the is the velocity of the fluid (m s−1), μ is the dynamic viscosity of the fluid (kg m−1 s−1), ρ is the density of the fluid (kg m−3), and  De is the hydraulic diameter of the pipe (m), defined as 4 times the cross-sectional area (of the fluid), divided by the wetted perimeter. The wetted perimeter for a channel is the total perimeter of all channel walls that are in contact with the flow. In all chosen flows of the present paper, the laminar flow is confirmed (Table 1, second column).Table 1
Data from continuous reactor and Comsol simulations (NOx 500 ppb, 20 Wm−2, sample size 0.005 cm2, RH: 40%, run time: 3 h. For the Comsol simulation: laminar flow).
Flow(L h−1)
Reynold’s number
Space velocity(h−1)
Contact time(s)
1077NOx conversion (%)
Orosei ActiveNOx conversion (%)
Experimentaldata
COMSOLsimulation
Experimentaldata
COMSOLsimulation
1
80.0
112
7200
0.5
5.0
36.8
1.3
25.6
32.4
20
1296
2.8
89.1
87.5
74.2
74.9
9.0
5.6
360
10.0
90.0
99.8
72.6
98.8
4.2
2.5
168
21.4
90.1
100.0
82.0
100.0On the contrary, the modification of the flow per hour leads to the an evident change of the contact times that is the time the pollutant can stay “in contact” with the catalyst surface. As expected, increasing the contact time, the final conversion proportionally increases. This result is very evident for Orosei Active that shows a conversion varying from 1.3% to 82.0% at 180 L h−1 and 4.2 L h−1, respectively (Table 1, seventh column). On the contrary, a sample of pure 1077, prepared on purpose on a glass sheet following the same procedure used for the batch setup, shows higher NOx conversion, but flattened towards the same value (ca. 90%).This fact is very interesting and was observed also performing the test on a three-layer of P25. In this case a value of ca. 90% was observed at both 32.4 and 9 L h−1 too, and a complete degradation (100%) was never present in our operative conditions as some fluid dynamics problems could exist inside the reactor configuration and part of the gas stream could pass undisturbed through the reactor. Moreover, the difference in the photocatalytic efficiency between P25 and 1077 evidenced by the tests performed in the batch reactor seems to be completely invalidated with this kind of reactor configuration.The higherNOx conversion of pure 1077 than Orosei Active was fully expected as the number of surface of active sites on the tile surface is not comparable to a film of pure TiO2 on a glass sheet. For this reason, the obtained 82% conversion at 4.2 L h−1 flow can be considered a very good value.


### 3.3. Digital Simulations

Figure4 reports a xz cross-section of the gas stream 3D fluid dynamics digital simulation in the two extreme flow rates: 180 and 4.2 L h−1. In more detail, the figure reports the local gas linear speed in the inlet side of the photoreactor. It is evident that the linear velocity of the gas stream is strongly influenced by the inlet flow rate: at 4.2 L h−1 the gas stream follows a natural path from the inlet to the channel containing the photoactive material, while at 180 L h−1 the inlet speed makes the gas to hit the wall in front of the inlet.x
y cross-sections of simulated fluid dynamic under steady-state conditions of the reactor used for the photocatalytic test (flowing conditions). (a) Vin = 32.4 L h−1, (b) Vin = 4.2 L h−1. The cross-section follows the longitudinal symmetry and is focused on the inlet gas chamber and a portion of the channel containing the photoactive tile.
(a)
V
in
=
32.4 L h−1
(b)
V
in
=
4.2 L h−1Notwithstanding that this effect might generate some turbulence in the inlet chamber (not included in the present simulation), the fluid speed profile inside the channel containing the photoactive material remains homogeneous through the channel length. In both cases, in the channel containing the photoactive material, the gas follows speed profile typical of laminar flows.Figure5 represents the xz cross-section of the simulated NOx concentration profiles in the reactor volume under steady-state conditions. Note that the inlet is on the left side of the reactor (i.e., the same side considered in Figure 4), while the outlet is on the right. The color code represents in this case the concentration of NOx in the air stream, expressed in mol m−3 (500 ppb corresponds to 2.04 × 10−5mol m−3).Figure 5
N
O
x local concentration in the reactor volume, expressed in mol m−3 (kapp = 4 × 10−3 m s−1, 32.4 L h−1). Inset (a), zoom on the photoactive tile; inset (b), xz cross-section of the photoactive tile.It is evident that, as expected, the concentration gradient is located at the reactor center, in correspondence to the photoactive tile. This is better represented in the two insets, a (in which the 3D space is transparent) and b (xz cross-section). In particular, inset b suggests the formation of a concentration gradient generated by the consumption of NOx at the photoactive surface. The gradient is at the origin of mass transport, that, at the lowest flow rate values, might become the rate determining step of the whole process, just before the maximum conversion (100%) is reached; see the simulated points (Figure 6) and values in Table 1.Figure 6
Experimental (EXP) and simulated (SIM) percentage conversion in dependence on the flow rate, as reported in Table1 relevant to the two samples considered in the flowing condition experiments (1077 and Orosei active) or the relevant simulated apparent kinetic constants (4 ×  10−3 and 2.3 × 10−3 m s−1, respectively. The light blue curve corresponds to the simulated data adopting a lower apparent kinetic constant, 1 × 10−4 m s−1.This is even more evident considering the experimental and simulated percentageNOx conversion values in dependence on the flow rate, reported in Figure 6. In the case of simulated results, which include the data at 20 L h−1 and 100 L h−1 as well as a set of data corresponding to kapp = 1 × 10−4 s−1 it is evident that the trend follows the expected exponential decay predicted by a first-order kinetics:
(2)NOxconversion=([NOx]inlet-[NOx]outlet)[NOx]inlet⋅100=100⋅(1-e-kt).In fact, the flow rate is inversely proportional to the contact time and thus to the reaction time,t. At the lowest flow rates (highest reaction times) a limiting-value results are reached, as indicated in Figure 6 by the colored ovals. These limiting values are 100% for the simulated data and about 90% for the experimental. This unexpected discrepancy can be explained considering the existence of preferential gas paths on the tiles sides (uncovered by the catalyst) that lead to the presence of unreacted NOx at the reactor outlet.The figures also evidence that the only common points between simulated and experimental data are those obtained 32.4 L h−1, that is, the conditions at which the kinetic constants used in the simulations have been determined. In other words, this means that also the experimental results obtained at high flow rates do not find any correspondence with the simulated data. This might be explained by the formation, in the real reactor, of turbulence (likely in the inlet chamber) that can actually change the fluid dynamics of the whole system due to the reactor geometry.


## 3.1. Sample Characterization

A feature comparison of both pure TiO2 and TiO2 + SiO2-based compound after the calcination treatment at 680°C shows the decrease of the surface area from 11.0 to 2.6 m2g−1 (BET measurements). From the surface point of view, XPS analysis reveals the classical Ti2p doublet at 458.6 ev (Ti2p3/2) attributed to Ti4+ with a Ti/Si ratio of 0.20.The formulation with the SiO2-based compounds and the following calcination step lead to a decrease of the surface area but preservation of the pure anatase form verified by XRD measurements [13]. As reported by Anderson and Bard [14], the presence of SiO2, together with TiO2, enhances the formation of hydroxyl radical  OH•, which would be achieved via strong Brønsted acid sites at the TiO2/SiO2 interface region. Such incorporation inhibits the crystal growth of TiO2 allowing the preservation of the anatase structure at high temperature [15].In order to investigate the morphological features of the various samples, HR-TEM technique has been resorted to. P25 nano-sized TiO2 has been also investigated, and its images are reported in Figures 1(a) and 1(b): it can be observed that the P25 material is made up of highly crystalline closely packed particles, as either thickness or Moirè’s fringe patterns are evident (right-hand image) [16] with rather smooth edges. The average particle size is in agreement with literature data [17], that is, 20–50 nm range. The detailed inspection of the spacings among the interference fringes (d = 0.357 nm) indicates that the most frequently exposed planes belong to the TiO2 (101) anatase polymorph [18]. If both particle size and ultimate morphology of the plain Kronos TiO2 sample (see Figures 1(c) and 1(d)) are compared to the P25 features, it can be evidenced that (i) particles are still packed, but to a limited extent if compared to the P25, and the edges of the particles are quite smooth; (ii) the size of the crystallites has enormously enlarged, as in the present case the average size varies in the 100–250 nm range; (iii) if we inspect the distances among the fringes, it is evident that the spacings (d = 0.357 nm) are still ascribable to the anatase polymorph. When the presence of the SiO2-based compound is considered, it can be stated that, roughly morphologically speaking, the main features of the TiO2 particles are maintained: see, for instance, Figures 1(e) and 1(f), in which the large dimensions of the particles are evident (50–200 nm range), beside rather smooth edges. Nevertheless, some peculiarities have to be mentioned: in particular, the presence of the SiO2-based compound is evident (see either the inset in Figure 1(e) or Figure 1(f)), in the form of either small protruding crystalline particles or an amorphous coating covering the TiO2 particles. In any case, the very thin nature of these particles and/or coating allows to inspect the fringe patterns located below, confirming that the spacings among the fringes are still ascribable to the anatase TiO2 polymorph.HR-TEM images of the various TiO2 materials. (a) and (b): P25. (c) and (d): 1077. (e) and (f): Orosei Active. (a), (c), and (e) refer to low magnification, here as (b), (d), and (f) to high magnification.
(a)
(b)
(c)
(d)
(e)
(f)Wettability measurements were performed on 15 different areas of both Orosei and Orosei Active (Figures2(a) and 2(b), resp.). Drop shapes are dramatically different enhancing a completely different surface. Orosei sample shows a mean contact angle value of 78.2°, while Orosei Active shows very hydrophilic surface features with an average angle of 23.0°. This very low value can be explained by the super-hydrophilic property of TiO2 photocatalyst as already observed by other authors [19]. In particular the copresence of TiO2 and SiO2 can lead to a modification of the angle value depending on the TiO2/SiO2 ratio [20] with values in the range of 20–25° with a SiO2 content at 70–80% (molar basis), in agreement with the XPS Ti/Si ratio obtained on Orosei Active.Contact angle: (a) Orosei; (b) Orosei Active tiles.
(a)
(b)Samples roughness, measured as root mean squared (Rq), was 19.354 μm and 18.860 μm for Orosei Active and Orosei (Ti-free), respectively.


## 3.2. Photocatalytic Tests

### 3.2.1. Batch Reactor

Figure3 reports the rate of NOx degradation for P25 and 1077. The NOx concentration is the sum of the NO and NO2 concentrations; the general mechanism of NOx oxidation by photocatalysts implies the oxidation of the nitric monoxide to nitric acid or nitrous by active oxygen species produced on the TiO2 surface [21].Figure 3
Comparison between P25 (◆) and 1077 (■) in the NOx photodegradation in a batch reactor.P25 is, as expected, more efficient than 1077 and it reaches a fullNOx degradation (1000 ppb) in about 2 h. On the contrary, 1077 never reaches a complete NOx degradation within the 6 h of test but, notwithstanding the larger crystallite size and the lower surface area, shows a 90% conversion after 100 min of irradiation.


### 3.2.2. Plug-Flow Reactor

ISO 22197-1 rule provides for very sharp experimental conditions such as an inletNOx concentration of 1000 ppb coupled with a low irradiation power (10 Wm−2) and mainly with a very strong flow at 180 L h−1. These conditions are too extreme for our samples being vitrified at their surface and having no porosity.For these reasons, the operating conditions have been softened cutting the inlet concentration by half (500 ppb), doubling the power irradiation (20 Wm−2), and investigating the role of the flow per hour on the final NOx conversion. To check to have maintained the correct fluid dynamic conditions, the Reynolds number was calculated:
(1)Re=ρUDeμ,
where U is the is the velocity of the fluid (m s−1), μ is the dynamic viscosity of the fluid (kg m−1 s−1), ρ is the density of the fluid (kg m−3), and  De is the hydraulic diameter of the pipe (m), defined as 4 times the cross-sectional area (of the fluid), divided by the wetted perimeter. The wetted perimeter for a channel is the total perimeter of all channel walls that are in contact with the flow. In all chosen flows of the present paper, the laminar flow is confirmed (Table 1, second column).Table 1
Data from continuous reactor and Comsol simulations (NOx 500 ppb, 20 Wm−2, sample size 0.005 cm2, RH: 40%, run time: 3 h. For the Comsol simulation: laminar flow).
Flow(L h−1)
Reynold’s number
Space velocity(h−1)
Contact time(s)
1077NOx conversion (%)
Orosei ActiveNOx conversion (%)
Experimentaldata
COMSOLsimulation
Experimentaldata
COMSOLsimulation
1
80.0
112
7200
0.5
5.0
36.8
1.3
25.6
32.4
20
1296
2.8
89.1
87.5
74.2
74.9
9.0
5.6
360
10.0
90.0
99.8
72.6
98.8
4.2
2.5
168
21.4
90.1
100.0
82.0
100.0On the contrary, the modification of the flow per hour leads to the an evident change of the contact times that is the time the pollutant can stay “in contact” with the catalyst surface. As expected, increasing the contact time, the final conversion proportionally increases. This result is very evident for Orosei Active that shows a conversion varying from 1.3% to 82.0% at 180 L h−1 and 4.2 L h−1, respectively (Table 1, seventh column). On the contrary, a sample of pure 1077, prepared on purpose on a glass sheet following the same procedure used for the batch setup, shows higher NOx conversion, but flattened towards the same value (ca. 90%).This fact is very interesting and was observed also performing the test on a three-layer of P25. In this case a value of ca. 90% was observed at both 32.4 and 9 L h−1 too, and a complete degradation (100%) was never present in our operative conditions as some fluid dynamics problems could exist inside the reactor configuration and part of the gas stream could pass undisturbed through the reactor. Moreover, the difference in the photocatalytic efficiency between P25 and 1077 evidenced by the tests performed in the batch reactor seems to be completely invalidated with this kind of reactor configuration.The higherNOx conversion of pure 1077 than Orosei Active was fully expected as the number of surface of active sites on the tile surface is not comparable to a film of pure TiO2 on a glass sheet. For this reason, the obtained 82% conversion at 4.2 L h−1 flow can be considered a very good value.


## 3.2.1. Batch Reactor

Figure3 reports the rate of NOx degradation for P25 and 1077. The NOx concentration is the sum of the NO and NO2 concentrations; the general mechanism of NOx oxidation by photocatalysts implies the oxidation of the nitric monoxide to nitric acid or nitrous by active oxygen species produced on the TiO2 surface [21].Figure 3
Comparison between P25 (◆) and 1077 (■) in the NOx photodegradation in a batch reactor.P25 is, as expected, more efficient than 1077 and it reaches a fullNOx degradation (1000 ppb) in about 2 h. On the contrary, 1077 never reaches a complete NOx degradation within the 6 h of test but, notwithstanding the larger crystallite size and the lower surface area, shows a 90% conversion after 100 min of irradiation.


## 3.2.2. Plug-Flow Reactor

ISO 22197-1 rule provides for very sharp experimental conditions such as an inletNOx concentration of 1000 ppb coupled with a low irradiation power (10 Wm−2) and mainly with a very strong flow at 180 L h−1. These conditions are too extreme for our samples being vitrified at their surface and having no porosity.For these reasons, the operating conditions have been softened cutting the inlet concentration by half (500 ppb), doubling the power irradiation (20 Wm−2), and investigating the role of the flow per hour on the final NOx conversion. To check to have maintained the correct fluid dynamic conditions, the Reynolds number was calculated:
(1)Re=ρUDeμ,
where U is the is the velocity of the fluid (m s−1), μ is the dynamic viscosity of the fluid (kg m−1 s−1), ρ is the density of the fluid (kg m−3), and  De is the hydraulic diameter of the pipe (m), defined as 4 times the cross-sectional area (of the fluid), divided by the wetted perimeter. The wetted perimeter for a channel is the total perimeter of all channel walls that are in contact with the flow. In all chosen flows of the present paper, the laminar flow is confirmed (Table 1, second column).Table 1
Data from continuous reactor and Comsol simulations (NOx 500 ppb, 20 Wm−2, sample size 0.005 cm2, RH: 40%, run time: 3 h. For the Comsol simulation: laminar flow).
Flow(L h−1)
Reynold’s number
Space velocity(h−1)
Contact time(s)
1077NOx conversion (%)
Orosei ActiveNOx conversion (%)
Experimentaldata
COMSOLsimulation
Experimentaldata
COMSOLsimulation
1
80.0
112
7200
0.5
5.0
36.8
1.3
25.6
32.4
20
1296
2.8
89.1
87.5
74.2
74.9
9.0
5.6
360
10.0
90.0
99.8
72.6
98.8
4.2
2.5
168
21.4
90.1
100.0
82.0
100.0On the contrary, the modification of the flow per hour leads to the an evident change of the contact times that is the time the pollutant can stay “in contact” with the catalyst surface. As expected, increasing the contact time, the final conversion proportionally increases. This result is very evident for Orosei Active that shows a conversion varying from 1.3% to 82.0% at 180 L h−1 and 4.2 L h−1, respectively (Table 1, seventh column). On the contrary, a sample of pure 1077, prepared on purpose on a glass sheet following the same procedure used for the batch setup, shows higher NOx conversion, but flattened towards the same value (ca. 90%).This fact is very interesting and was observed also performing the test on a three-layer of P25. In this case a value of ca. 90% was observed at both 32.4 and 9 L h−1 too, and a complete degradation (100%) was never present in our operative conditions as some fluid dynamics problems could exist inside the reactor configuration and part of the gas stream could pass undisturbed through the reactor. Moreover, the difference in the photocatalytic efficiency between P25 and 1077 evidenced by the tests performed in the batch reactor seems to be completely invalidated with this kind of reactor configuration.The higherNOx conversion of pure 1077 than Orosei Active was fully expected as the number of surface of active sites on the tile surface is not comparable to a film of pure TiO2 on a glass sheet. For this reason, the obtained 82% conversion at 4.2 L h−1 flow can be considered a very good value.


## 3.3. Digital Simulations

Figure4 reports a xz cross-section of the gas stream 3D fluid dynamics digital simulation in the two extreme flow rates: 180 and 4.2 L h−1. In more detail, the figure reports the local gas linear speed in the inlet side of the photoreactor. It is evident that the linear velocity of the gas stream is strongly influenced by the inlet flow rate: at 4.2 L h−1 the gas stream follows a natural path from the inlet to the channel containing the photoactive material, while at 180 L h−1 the inlet speed makes the gas to hit the wall in front of the inlet.x
y cross-sections of simulated fluid dynamic under steady-state conditions of the reactor used for the photocatalytic test (flowing conditions). (a) Vin = 32.4 L h−1, (b) Vin = 4.2 L h−1. The cross-section follows the longitudinal symmetry and is focused on the inlet gas chamber and a portion of the channel containing the photoactive tile.
(a)
V
in
=
32.4 L h−1
(b)
V
in
=
4.2 L h−1Notwithstanding that this effect might generate some turbulence in the inlet chamber (not included in the present simulation), the fluid speed profile inside the channel containing the photoactive material remains homogeneous through the channel length. In both cases, in the channel containing the photoactive material, the gas follows speed profile typical of laminar flows.Figure5 represents the xz cross-section of the simulated NOx concentration profiles in the reactor volume under steady-state conditions. Note that the inlet is on the left side of the reactor (i.e., the same side considered in Figure 4), while the outlet is on the right. The color code represents in this case the concentration of NOx in the air stream, expressed in mol m−3 (500 ppb corresponds to 2.04 × 10−5mol m−3).Figure 5
N
O
x local concentration in the reactor volume, expressed in mol m−3 (kapp = 4 × 10−3 m s−1, 32.4 L h−1). Inset (a), zoom on the photoactive tile; inset (b), xz cross-section of the photoactive tile.It is evident that, as expected, the concentration gradient is located at the reactor center, in correspondence to the photoactive tile. This is better represented in the two insets, a (in which the 3D space is transparent) and b (xz cross-section). In particular, inset b suggests the formation of a concentration gradient generated by the consumption of NOx at the photoactive surface. The gradient is at the origin of mass transport, that, at the lowest flow rate values, might become the rate determining step of the whole process, just before the maximum conversion (100%) is reached; see the simulated points (Figure 6) and values in Table 1.Figure 6
Experimental (EXP) and simulated (SIM) percentage conversion in dependence on the flow rate, as reported in Table1 relevant to the two samples considered in the flowing condition experiments (1077 and Orosei active) or the relevant simulated apparent kinetic constants (4 ×  10−3 and 2.3 × 10−3 m s−1, respectively. The light blue curve corresponds to the simulated data adopting a lower apparent kinetic constant, 1 × 10−4 m s−1.This is even more evident considering the experimental and simulated percentageNOx conversion values in dependence on the flow rate, reported in Figure 6. In the case of simulated results, which include the data at 20 L h−1 and 100 L h−1 as well as a set of data corresponding to kapp = 1 × 10−4 s−1 it is evident that the trend follows the expected exponential decay predicted by a first-order kinetics:
(2)NOxconversion=([NOx]inlet-[NOx]outlet)[NOx]inlet⋅100=100⋅(1-e-kt).In fact, the flow rate is inversely proportional to the contact time and thus to the reaction time,t. At the lowest flow rates (highest reaction times) a limiting-value results are reached, as indicated in Figure 6 by the colored ovals. These limiting values are 100% for the simulated data and about 90% for the experimental. This unexpected discrepancy can be explained considering the existence of preferential gas paths on the tiles sides (uncovered by the catalyst) that lead to the presence of unreacted NOx at the reactor outlet.The figures also evidence that the only common points between simulated and experimental data are those obtained 32.4 L h−1, that is, the conditions at which the kinetic constants used in the simulations have been determined. In other words, this means that also the experimental results obtained at high flow rates do not find any correspondence with the simulated data. This might be explained by the formation, in the real reactor, of turbulence (likely in the inlet chamber) that can actually change the fluid dynamics of the whole system due to the reactor geometry.


## 4. Conclusions

Microsized  TiO2 can be really used as a valid choice for anti-pollutant photocatalytic processes avoiding the intrinsic risk due to the nanometric dimension. TiO2 larger size compared to more traditional nano-sized crystallites allows to reach fully comparable results in the photodegradation of NOx, reference molecule for outdoor air pollution.Good photocatalytic efficiency was achieved by the pure commercial microsized  powder in comparison to P25. Porcelain gres tiles prepared entrapping micro-TiO2 at the SiO2 surface also show a stable and reproducible photocatalytic activity towards the degradation of NOx in air as expected by the surface feature results (surface wettability and Ti content).EmployedNOx photoreactor was built following the ISO 22197-1 rule but the requested ISO experimental conditions, such as inlet NOx concentration, low irradiation power, and high flow, are too extreme for our tiles samples being vitrified at their surface and having no porosity. For these reasons, the operating conditions have been softened and the role of the flow per hour on the final NOx conversion was fully investigated.The discrepancies between the experimental data and the simulated ones might be related to the presence of preferential gas paths in the test reactor and to the formation of turbulence (due to the reactor geometry) in the case of the highest flow rate values.



---

*Source: 970182-2012-09-02.xml*