Soufiane Hmamouchi1, Ahmed El Yacoubi1,2, Brahim Chafik El Idrissi1. 1. Advanced Materials and Process Engineering Laboratory, Faculty of Sciences, Ibn Tofail University, Kenitra, Morocco. 2. Laboratory of Applied Chemistry and Environment, Mineral Solid Chemistry Team, Mohamed First University, Oujda, Morocco.
Abstract
Nanoparticles of undoped hematite (α-Fe2O3) and Co doped α-Fe2O3 were prepared by a simple, green, and cost-efficient process using Co and Fe chlorides and freshly isolated hen egg white. Several techniques of characterization, such as differential thermal and thermogravimetric analysis (DTA/TG), Fourier transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), EDS analysis, X-ray diffraction analysis (XRD), and Ultra-violet Visible (UV-Vis) analysis were applied. The incorporation of Co particles into the hematite matrix limits the growth of the α-Fe2O3 crystalline grain and favours the apparition of γ-Fe2O3 phase. SEM analysis reveals that there are no significant morphological differences among α-Fe2O3 and Co-α-Fe2O3 particles, whereas the XPS analysis confirms the existence of Fe and Co particles in the as-prepared samples. The optical study shows a slight reduction of band gap energy for Co doped α-Fe2O3 compared to the non-doped α-Fe2O3, which has shown enhanced visible light adsorption performance. On the other hand, the α-Fe2O3 and Co-α-Fe2O3 nano-photocatalysts with an average crystallite size of 21 and 43 nm respectively, were used to remove the Methylene Blue (MB) dye from aqueous solutions after being exposed to visible light. In a mechanistic study, the radicals OH• and •O2 - were shown to be important in the degradation of MB dye. To optimise the effective parameters on MB dye degradation, the experimental parameters applied in the adsorption experiments, such as pH, photocatalyst dosage, contact time, and temperature, were tested. The optimal conditions were determined as pH = 12, photocatalyst dosage = 0.2 g/L. Degradation efficiency in the optimal conditions is 91.8 % after 120 min of irradiation. The pseudo-first and second orders were used to model the kinetic data. The removal of MB using α-Fe2O3 and Co-α-Fe2O3 photocatalysts matched well with pseudo-second-order reaction kinetics. Furthermore, the thermodynamic study reveals that MB dye adsorption on the Co-Fe2O3 absorbent was an endothermic and spontaneous process.
Nanoparticles of undoped hematite (α-Fe2O3) and Co doped α-Fe2O3 were prepared by a simple, green, and cost-efficient process using Co and Fe chlorides and freshly isolated hen egg white. Several techniques of characterization, such as differential thermal and thermogravimetric analysis (DTA/TG), Fourier transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), EDS analysis, X-ray diffraction analysis (XRD), and Ultra-violet Visible (UV-Vis) analysis were applied. The incorporation of Co particles into the hematite matrix limits the growth of the α-Fe2O3 crystalline grain and favours the apparition of γ-Fe2O3 phase. SEM analysis reveals that there are no significant morphological differences among α-Fe2O3 and Co-α-Fe2O3 particles, whereas the XPS analysis confirms the existence of Fe and Co particles in the as-prepared samples. The optical study shows a slight reduction of band gap energy for Co doped α-Fe2O3 compared to the non-doped α-Fe2O3, which has shown enhanced visible light adsorption performance. On the other hand, the α-Fe2O3 and Co-α-Fe2O3 nano-photocatalysts with an average crystallite size of 21 and 43 nm respectively, were used to remove the Methylene Blue (MB) dye from aqueous solutions after being exposed to visible light. In a mechanistic study, the radicals OH• and •O2 - were shown to be important in the degradation of MB dye. To optimise the effective parameters on MB dye degradation, the experimental parameters applied in the adsorption experiments, such as pH, photocatalyst dosage, contact time, and temperature, were tested. The optimal conditions were determined as pH = 12, photocatalyst dosage = 0.2 g/L. Degradation efficiency in the optimal conditions is 91.8 % after 120 min of irradiation. The pseudo-first and second orders were used to model the kinetic data. The removal of MB using α-Fe2O3 and Co-α-Fe2O3 photocatalysts matched well with pseudo-second-order reaction kinetics. Furthermore, the thermodynamic study reveals that MB dye adsorption on the Co-Fe2O3 absorbent was an endothermic and spontaneous process.
Because of their adjustable surface morphology, distinctive crystal structure, and intrinsic catalytic properties, transition metal oxides have received a lot of technological and scientific attention [1]. Among these, hematite α-Fe2O3 has recently been discovered as an important alternative and promising candidate for solar photocatalysis, which can degrade organic dyes with excellent photo-oxidation activity [2, 3]. Iron oxide α-Fe2O3 (Hematite), the most stable iron oxide with a rhombo-hexagonal structure, has received extensive research, especially in photocatalytic applications, due to its low-cost, non-toxicity, exceptional stability, excellent anti-ferromagnetic characteristics, simple recovery [4, 5], and appropriate band gap energy Eg (2.0–2.3 eV). These properties allow it to absorb more than half of the visible light (λ > 600 nm), collect up to 40% of the energy from the incident solar spectrum, and remain stable in the vast majority of aqueous solutions (pH > 3) [6]. Cobalt ferrites, among the various ferrites, have recently attracted interest, due to its excellent chemical stability, extremely high electrical resistivity, excellent mechanical hardness, and significant permeability at high frequencies as well as to being low-cost [7, 8]. Contaminated water is major problem these days. the photocatalytic method has attracted the interest of researchers for reducing the content of dye molecules in used water before it is discharged into the environment. Methylene blue (MB) dye is widely utilized in textile industries such as dyeing and printing. It is also employed in medical field because of its antifungal characteristics. However, over use of MB dye can cause serious dietary and health problems such as vomiting, gastrointestinal distress [9]. Therefore, it is necessary to develop low-cost, eco-friendly and effective materials for the degradation of many dyes from wastewater. As one of the potential photocatalysts with high photocatalytic reactivity, α-Fe2O3 appears to be an essential material to remove several dyes and organic pollutants [10]. Generally, the photocatalytic performance of such a photocatalyst can be affected by several factors, including exposed surface facets, crystalline phase, porous structure, specific surface area, and morphological characteristics [11, 12]. According to the literature, α-Fe2O3 powders in various shapes, such as nanoparticles [13] nanorods [14] nanoflowers [15] nanodisks [16] Nanospheres [17] and spindles [18] have been prepared by different techniques, including hydrothermal [19], solvothermal [20], sol-gel [21] and co-precipitation [22]. To choose a simple process for the synthesis of nano-ferrites, the use of low-cost and nontoxic precursors seems to be the key issue. Moreover, because of the link between biological structures and inorganic molecules, green synthesis is one of the top interesting subjects of nanomaterials research [23]. The gelling, foaming, and emulsifying properties of egg white proteins are well recognized [24]. It has been used to shape materials as a binder or gel. Although it is less proficient, the use of egg white facilitates the process and offers another alternative method to synthesize the nano-crystalline particles with low-effective method. To the best of our knowledge, there is no method that provides the production of pure α-Fe2O3 and Co-α-Fe2O3 particles using egg ovalbumin.The current findings show the synthesis of α-Fe2O3 and Co-α-Fe2O3 nanoparticles at a relatively low temperature by a simple, ecologically, and cost-effective process using CoCl2·6H20, FeCl3·6H2O and using, for the first-time, hen egg white as a precursor. The structural, optical, and morphological properties of α-Fe2O3 and Co-α-Fe2O3 nanoparticles were studied by DTA/TGA, XRD, FTIR, UV-visible spectroscopy, and SEM. The photocatalytic efficiency of α-Fe2O3 and Co-α-Fe2O3 was evaluated by examining the degradation of MB dye under visible light irradiation.
Materials and methods
α-Fe2O3 and Co-α-Fe2O3 synthesis
All substance reagents used in present work were of analytical grade and utilized with no supplementary purification. The α-Fe2O3 and Co-α-Fe2O3 NPs were elaborated, for the first time, by an aqueous co-precipitation process using a hen egg white as a source of oxygen. Iron (III) chloride hexahydrate (FeCl3.6H2O, >97%) and cobalt chloride's hexahydrate (CoCl2.6H2O, 98%) were provided by Sigma Aldrich and were used as received.In a conventional method, the freshly extracted hen ovalbumin was first mixed and homogenized with distilled water under vigorous agitation at 500 rpm for 30 min to get a well-homogenized solution (Solution A). Subsequently, the desired amounts of metal precursors FeCl3.6H2O and CoCl2.6H2O were first dissolved in distilled water (Solution B) and added dropwise to the as-prepared ovalbumin solution. For the synthesis of Co- α-Fe2O3 NPs, 1.189g of CoCl2.6H2O and 2.703g of FeCl3.6H2O were added to solution A to achieve an atomic ratio of Co/Fe = 0.5. Throughout the synthesis process, the pH of the mixture is not controlled. The resultant yellow suspension was then heated for 2h, under continuous stirring (500rpm), in a hot plate at 80 °C. Finally, the pale-yellow suspension was filtered and washed, for several occasions, by means of warm distilled water to eliminate any potential impurities or any possible contaminants and dried overnight at 100 °C. The obtained deep red samples were crushed into powder with agate mortar and annealed at 550 °C for 2h and then decreased to ambient temperature to get α-Fe2O3 and Co- α-Fe2O3 NPs. Figure 1 shows a quick overview of the synthesis of undoped and Co doped α-Fe2O3 photocatalysts.
Figure 1
Schematic representation of the synthesis of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
Schematic representation of the synthesis of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
Characterization techniques
The different crystalline phases present in the as prepared powders were identified by a Shimadzu 6100 Diffractometer, with a wavelength λ of copper Kα radiation equal to 1.5406 Å, operating at 40 kV in the scan range of 20–70° with a step scan of 0.02°. Infrared patterns were recorded in the range of 350–4000 cm−1 with an attenuated total reflection ATR-FTIR spectrometer. The morphological properties and surface compositions of elaborated samples were carried out by a scanning electron microscopy (SEM) coupled with Energy dispersive system X-ray micro-spectrometer (EDAX). To understand the thermal behaviour of the involved samples, the thermogravimetric analysis (TG/DTG) was investigated using a Shimadzu DTG-60 thermal analyser with a heating rate of 10 °C/min.
Photocatalytic activity assessment of the prepared photocatalysts
The photocatalytic features of α-Fe2O3 and Co-α-Fe2O3 nano-photocatalysts were performed by degrading methylene blue (MB) dye in an aqueous medium when exposed to visible light (36 LED Lamp). The vertical distance between the LED lamp and the dye solution, in axial opposition, is kept constant and equal to 10 cm. To reach the adsorption-desorption balance, the photocatalyst powder and solution dye mixture was placed, under magnetic agitation (800 rpm), in the dark for 30 min. The absorption values were collected at the wavelength corresponding to the most extreme adsorption of the used inorganic dye (λmax = 664 nm). Typically, the desired amount of the prepared photocatalyst was scattered into 50 mL of MB dye aqueous solution (1 g/L), under constant stirring (700 rpm), and irradiated by a visible light lamp for the required time. The result suspensions were periodically centrifuged to remove the photocatalyst powder from the dye solution. The degradation rates (%) of the photocatalyst were carried out using UV-visible 2005 spectrophotometer (Eq. (1)).Where A0 and A are the initial and the final absorbance after irradiation process, respectively.
Results and discussion
Characterization
The XRD patterns of hematite α-Fe2O3 and Co-doped hematite Co-α-Fe2O3 nano-photocatalysts are shown in Figure 2. Among these, the two samples were switched well with the rhombohedral space group of α-Fe2O3 phase (R-3c (167), a = b = 0.50356 Å, c = 1.37489 Å, JCPDS card N°: 33–0664), which illustrates that the presence of Co particles does not affect the α-Fe2O3 crystal type. Table 1 summarizes all the x-ray diffraction peaks for α-Fe2O3 specimen. In the case of the Co doped sample, additional very weak peaks can be detected at 30.16 and 43.35°. Such peaks correspond to γ-Fe2O3 phase, which is thermodynamically less stable. From these results, it may be deduced that Co2+ ions doping limits the proliferation of α-Fe2O3 crystals and promotes the growth of γ-Fe2O3 phase. Other authors have reported the same observations in the literature [25, 26]. In addition, due to the existence of Co, the diffraction peaks of the Co doped powder hematite α-Fe2O3 have been moved to lower angles in the pattern, compared to those of the pure α-Fe2O3 powder, confirming the successful insertion of Co ions into the pure hematite lattice. These angular variations are generally synonymous with a modification of the distance between two diffraction planes due to the incorporation of Co ions in the α-Fe2O3 lattice (different ionic radius). The average crystallite size of particle was determined using the well-known Scherer formula (Eq. (2)) from the full width at half maximum (FWHM) of XRD patterns [27].where D is the average crystallite size (nm), β is the peak's broadening or FWHM (rad), λ is the Cu-Kα X-ray wavelength and θ is the Bragg-position of the concerning peak determined from the XRD pattern.
Figure 2
XRD patterns of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
Table 1
Peak positions and Miller indices of hematite α-Fe2O3 photocatalyst.
Peak position 2θ (°)
Miller indices (facet direction)
24.21
(012)
33.21
(104)
35.72
(110)
40.93
(113)
49.54
(024)
54.14
(116)
57.60
(122)
62.50
(214)
64.07
(300)
XRD patterns of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.Peak positions and Miller indices of hematite α-Fe2O3 photocatalyst.The peak width FWHM at low-angle is more relevant to estimating the grain size from XRD data. Hence, the particle size of nanoparticles was computed using the maximum intensity peak (104). According to the preceding method, the average size of the α-Fe2O3 and Co- α-Fe2O3 nanoparticles was 43 and 21 nm, respectively. It is clear that the crystalline size of α-Fe2O3 decreases significantly with the insertion of Co ions, which indicates that the Co particles limit the growth of the crystalline grain.FT-IR spectroscopy is a characterization technique, based on the adsorption of infrared radiation by the analysed material, which gives the different functional groups present in the sample. Figure 3 depicts the FT-IR spectra for pure α-Fe2O3 and Co-α-Fe2O3 samples from 360 to 4000 cm−1. The absorption bands for the two FT-IR spectra are quite similar. The spectra show two characteristic bands at 427 cm−1 and 519 cm−1 which correspond to the Fe-O stretching vibration mode of iron oxide. The strong and medium intense adsorption bands at 519 cm−1 and 439 cm−1 arise from the intrinsic stretching vibrational mode ν1 of the Fe-O liaison and the bending vibration ν2 of the O-Fe-O [28], respectively.
Figure 3
FTIR spectra of α-Fe2O3 and Co-α-Fe2O3 samples calcined at 550 °C for 2 h.
FTIR spectra of α-Fe2O3 and Co-α-Fe2O3 samples calcined at 550 °C for 2 h.Figure 4 displays only the thermal behavior of Co-α-Fe2O3 photocatalyst from room temperature to 800 °C. The decomposition process starts with the vaporization of hydrated water (a minor weight loss), followed by a series of TG steps (major weight loss) due to the decomposition of remaining organic moieties present in the egg-white after the synthesis step. Weight loss and the very large endothermic peaks at ~110° and 205 °C are synonyms of the loss of adsorbed and surface-bound water molecules. The two exothermic DTA peaks located at 280 and 324 °C can be ascribed to the decomposition of the organic substance. The large exothermic DTA at 462 °C can be attributed to the Co-α-Fe2O3 formation. There was no major weight loss observed after 570 °C. The formation of Co-α-Fe2O3 nanocrystalline was confirmed by a weak endothermic DTA peak at 540 °C which corresponded to the crystallization process of the hematite α-Fe2O3 phase, as confirmed by XRD and FT-IR analysis.
Figure 4
Thermal analysis DTA/TG of Co doped α-Fe2O3 nanoparticles.
Thermal analysis DTA/TG of Co doped α-Fe2O3 nanoparticles.Figure 5 illustrates the SEM images of α-Fe2O3 and Co-α-Fe2O3 photocatalyst materials. After analysing the SEM images, it is apparent that the grain size of both samples is inhomogeneous and gets agglomerated in some cases. The loss of nanostructure-stabilizing ions by washing with water is thought to be the cause of the agglomeration [29]. As can be shown in Figure 5, SEM images of Co-doped α-Fe2O3 samples (Figure 5a and b) were substantially clearer than those of undoped α-Fe2O3 samples, which might be attributed to enhanced electrical conductivity of α-Fe2O3 nanoparticles after Co doping [30, 31]. SEM images reveal also that the crystallites do not have a regular and uniform shape. By comparing the micrographs, we can clearly see that there are no significant morphological differences among α-Fe2O3 and Co-α-Fe2O3 specimens, indicating that the morphology of α-Fe2O3 is not influenced by cobalt doping. Grain sizes estimated by the XRD technique are significantly smaller than those seen by SEM. This difference in grain size could be explained by the fact that the SEM analysis gives only the average particle size of the analyzed surface, which means that each grain is constituted by the aggregation of many nanocrystals, whereas the XRD technique focuses on the crystallite size of single particles. Satheesh et al. report the same [22]. Furthermore, the composition of the synthesized photocatalysts was carried out by EDX analysis. Figure 6 depicts the EDX patterns of α-Fe2O3 and Co-α-Fe2O3 materials. All the elements constituting the hematite phase appear at their corresponding keV energy values.
Figure 5
SEM images of the as-prepared photocatalysts materials A) α-Fe2O3 B) Co-α-Fe2O3.
Figure 6
Energy dispersive spectrum of [a] α-Fe2O3 and [b] Co-α-Fe2O3 photocatalysts.
SEM images of the as-prepared photocatalysts materials A) α-Fe2O3 B) Co-α-Fe2O3.Energy dispersive spectrum of [a] α-Fe2O3 and [b] Co-α-Fe2O3 photocatalysts.
Optical property
Extrapolation from the absorption may be used to calculate the optical bandgap (Eg) for α-Fe2O3 and Co-α-Fe2O3 nanoparticles employing the well-known Tauc's equation [32] (Eq. (3)):Where α, Eg, A, hυ and n are the absorption coefficient, bandgap energy, optical constant, energy of emitted light, and a constant characterizing the type of the electronic transition [33], i.e., n = 2 for direct transition and n = 1/2 for indirect transition [34]. Undoped and Co2+ doped α-Fe2O3 show direct as well as indirect transition. Figure 7a, b show the absorption edge (αhυ)n versus photon energy hυ for the two ways of transition (direct and indirect) and the obtained band gap energy is shown in Table 2. The valence band (EVB) and conduction band (ECB) potentials for α-Fe2O3 and Co- α-Fe2O3 were estimated by using Eqs. (4) and (5), respectively [3].
Figure 7
Tauc plots of α-Fe2O3 and Co-α-Fe2O3 for [a] direct transition [b] indirect transition.
Table 2
Bandgap values of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
Bandgap (eV)
Direct transition
Indirect transition
α-Fe2O3
2.28
1.87
Co-α-Fe2O3
2.03
1.79
Tauc plots of α-Fe2O3 and Co-α-Fe2O3 for [a] direct transition [b] indirect transition.Bandgap values of α-Fe2O3 and Co-α-Fe2O3 photocatalysts.Where χ, Ee and Eg correspond to the absolute Mulliken electronegativity (=5.87 eV), the energy of free electrons on the hydrogen scale (=4.5 eV) and the system band gap energy. The calculated EVB and ECB edge potentials were: EVB = 2,51 eV; ECB = 0.23 eV and EVB = 2.38eV; ECB 0.355 eV for α-Fe2O3 and Co-α-Fe2O3, respectively.The indirect transition is caused by the excitation of forbidden spin Fe3+ 3d→3d, whereas the direct transition is related to the transfer of charge O2− 2p→ Fe3+ 3d. According to the literature, the estimated bandgap values of direct and indirect transitions of α-Fe2O3 vary in the range of 2–2.6 eV [25, 35] and 1.38–2.09 [36] respectively. Our results are consistent with previous reports. Compared with the non-doped hematite specimen, the band gap of the Co doped α-Fe2O3 was slightly reduced, which indicates that the Co2+ doping process affects the conduction band edge of α-Fe2O3, leading to enhanced visible light absorption properties. However, supplementary density states, in the bandgap of α-Fe2O3 material, would be generated by the coupling interaction effect between the co dopant and Fe atoms, and consequently shift the conductive band minimum upward, closer to the redox level of H2O/H2 couple [34]. Since α-Fe2O3 is an excellent absorber of visible light irradiation, the insertion of Co particles could only slightly decrease the bandgap of α-Fe2O3 under these conditions [34].
Photocatalytic properties evaluation
The photocatalytic performances of the nano-photocatalyst samples were investigated by the degradation of methylene blue (MB) molecules after exposure to visible-light. As an initial starting point, the experiments were carried out at pH = 12 with a MB concentration of 10 mg/L and with a photocatalyst concentration of 0.2 g/L of MB solution. To estimate the self-photodegradation of MB dye effect, a control experiment was conducted under irradiation of visible light without a photocatalyst phase, which revealed that there was no remarkable change in MB concentration. Figure 8 depicts the absorbance of different times of MB dye in the presence of α-Fe2O3 and Co-α-Fe2O3 nano-photocatalysts. All UV–visible absorption spectra show a maximum absorbance at 664 nm. With the increase in irradiation time, the absorption intensity at 664 nm decreases confirming the degradation of the MB dye. At the beginning of reaction (t = 0) the color of the MB solution changed from navy blue to light blue. However, as adsorption increased, it became practically transparent, indicating that most of the MB molecules present in the dye solution were adsorbed by the α-Fe2O3 and Co-α-Fe2O3 photocatalysts. The adsorption efficiency of photocatalysts raise quickly in the initial 10 min, and reached to 71.3 and 82.3% for undoped and Co2+ doped α-Fe2O3 respectively, to stabilise after 120 min of visible irradiation at 90.2 and 91.8% respectively.
Figure 8
UV-Visible absorbance spectra of [a] α-Fe2O3 [b] Co-α-Fe2O3 photocatalysts.
UV-Visible absorbance spectra of [a] α-Fe2O3 [b] Co-α-Fe2O3 photocatalysts.
Effect of pH
Industries discharge waste water containing organic compounds at various pH values. Therefore, it is important to study the efficacy of catalysts towards the removal of dyes at different pH. The experiment was investigated at different pH values ranging from 5 to 13 for constant MB concentration (10 mg/L) and photocatalyst loading of 1 g/L. Figure 9 illustrates the photodegradation percentage of MB as a function of pH. As shown in Figure 8, with increasing pH, the efficiency of the photocatalysts for MB degradation increased and exhibited high color removal at pH = 12, after 60 min of irradiation, for both α-Fe2O3 and Co-α-Fe2O3 photocatalysts. This result may be explained by the effect of the adsorbent surface charge and point of zero charge (pzc) of α-Fe2O3 [37]. Indeed, the absorbent surface charge is mostly controlled by the pHPZC. From the pzc, given in Figure 10, pHpzc (α-Fe2O3) = 5.3. Therefore, the surface of α-Fe2O3 becomes positively charged below the pHpzc and becomes gradually more negatively charged above the pHpzc. The weak MB adsorption at low pH may be due to electrostatic repulsion forces between positively loaded MB (cationic dye) and positively loaded adsorption sites [38]. When the mixture pH increases, the contact surface of α-Fe2O3 becomes more negatively charged, and an important electrostatic attraction force is developed between the cationic molecules of MB dye and the negatively charged α-Fe2O3 surface, which in turn enhances adsorption efficiency [39].
Figure 9
Degradation efficiency of the two prepared photocatalysts for MB dye solution.
Figure 10
Point of zero charge (PZC) graph of α-Fe2O3.
Degradation efficiency of the two prepared photocatalysts for MB dye solution.Point of zero charge (PZC) graph of α-Fe2O3.
Photocatalyst dosage effect
As is well known, the degradation efficiency is widely influenced by the amount of catalyst dispersed in the pollutant solution. The photodegradation tests were performed by varying the catalyst dosages (α-Fe2O3 and Co-α-Fe2O3) ranging from 0.1 to 1.4 g/L at pH = 12 and keeping the MB concentration (10 mg/L) constant. Figure 11 illustrates the photodegradation efficiency of MB with photocatalyst dosage. According to Figure 11, the photodegradation efficiency beyond 0.2 g/L decreases as the photocatalytic dosage increases. The photodegradation percentage of MB is 82.88 and 85.71% at 0.2 g/L of α-Fe2O3 and Co-α-Fe2O3 respectively. The same phenomenon was observed by other researchers [20, 22, 40]. When the catalyst dosage is optimised (0.2 g/L), more active sites become available on the catalyst's surface. It also absorbs enough light to create sufficient active •OH radicals on the α-Fe2O3 and Co-α-Fe2O3 surfaces. This is assigned to the agglomeration of photocatalyst particles, which decreases the number of active sites on the surface area [20]. On the other hand, the high stirring speed with a high photocatalyst dose may limit the penetration of light into solution, leading to a decrease in the total photoactivated volume by affecting the electron-hole formation, hence the photocatalytic efficiency decreases.
Figure 11
Degradation efficiency with photocatalysts dosage.
Degradation efficiency with photocatalysts dosage.
Contact time effect
Contact time is a key issue in the absorption process because it relates to the amount of sorbent fixed and contact time. It is used to estimate how long it will take to reach sorption–desorption equilibrium. The effect of contact time on the removal of MB dye is shown in Figure 12. The adsorption process began with a higher adsorption rate and decreased progressively with increasing adsorption time to finally achieve equilibrium after 60 min of adsorption. At the start of absorption phenomena, the high adsorption rate might be attributed to the availability of too many unoccupied active adsorption sites on the α-Fe2O3 and Co-α-Fe2O3 surfaces, which could be used, leading to a rapid adsorption rate. As adsorption time increases, active adsorption sites are increasingly occupied by MB molecules, causing a lower adsorption rate. Furthermore, adsorbed and non-adsorbed MB ions create powerful repulsive forces, making the rest of the sites increasingly difficult to occupy until achieving an equilibrium state [38]. The low adsorption rate at the end of experiments suggests the eventual monolayer formation of MB on the photocatalyst surface [41]. A quick comparison of the current results with previously published experiments based on α-Fe2O3 doping is shown in Table 3.
Figure 12
Degradation efficiency of MB dye with irradiation time.
Table 3
A Comparative study of the present results with those reported in the literature.
(M = Cu, Mn, Cr, Nb, Mo, Ti, V,Zn, Ni and Co) doped α-Fe2O3
Hydrothermal
100–200
dodecahedron
Direct: 1.97–2.01Indirect: 2.04–2.08
–
[34]
Sn doped α-Fe2O3
combination of hydrothermal, co-precipitation and calcination
10–143
Nanorods nanoellipsoids nanocuboids
Sn-α-Fe2O3: 2.10–2.18
60% (30 min)Dye: RhB
[44]
Present work
Co-precipitation
21–43
No regular shape
α-Fe2O3: 2.28Co-α-Fe2O3: 2.03
92% (120 min)Dye; MB
–
Degradation efficiency of MB dye with irradiation time.A Comparative study of the present results with those reported in the literature.
Effect of the temperature
Temperature is an important physical parameter that can change the adsorption capacity of the adsorbent. This effect on the adsorption of MB dye on Co-α-Fe2O3 was investigated from 298 to 328 K under stirring for 30 min. Figure 13 shows the adsorption capacity increased from 43.025 to 46.93 mg g−1, when the temperature was increased from 298 to 328 K, which indicates that the adsorption is an endothermic process. This may be due to the strengthening of the attractive forces between MB and the active sites on the Co-α-Fe2O3 surface.
Figure 13
Temperature effect on the adsorption of MB dye on Co-α-Fe2O3 absorbent surface.
Temperature effect on the adsorption of MB dye on Co-α-Fe2O3 absorbent surface.
Photo-adsorption kinetics
The pseudo first order (PFO) kinetic model of Lagergren [45] is given by the Eq. (6):where, q is the amount of MB adsorbed (mg/g) at: equilibrium state qe and time t qt, while k1 represents the first order rate constant (min−1). A linear plot of ln(qe-qt) versus t provides a relationship between k1 and qe, which can be calculated from the slope and the intercept of the affine function ln(qe-qt) = f(t).The linearized form of the pseudo second order (PSO) rate equation is given by the Eq. (7):Where qe and qt are the adsorbed quantities of adsorbate system per unit mass of sorbent at equilibrium state and at any time (mg g−1), respectively, and k2 is the PSO rate constant (g mg−1 min−1). Taking into consideration the boundary conditions (t = 0 to t = t and q = 0 to q = qt), and after integration of the previous equation, the linear form of the PFO model expression is as follows (Eq. (8) and (9)):This linear form can be written as:A plot of t/qt versus t provides a linear relationship, from which the kinetic model constants of PSO (qe and k2) are calculated from the slope and interception. Figure 14 illustrates the PFO and PSO kinetic plots for α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
Figure 14
PFO and PSO kinetic plots for the adsorption of α-Fe2O3 and Co-α-Fe2O3.
PFO and PSO kinetic plots for the adsorption of α-Fe2O3 and Co-α-Fe2O3.Table 4 shows the results of applying MB adsorption data on α-Fe2O3 and Co-α-Fe2O3 to the PFO and PSO kinetic models. As can be shown in Table 4 and Figure 14, the PSO kinetic model has a higher correlation factor (R2 > 0.999) than the PFO kinetic model (R2 = 0.634). These results showed that the MB adsorption on the α-Fe2O3 and Co-α-Fe2O3 photocatalysts closely follows the PSO kinetics. Sivalingam et al. [46] and Koyuncu et al. [47] report the same results.
Table 4
Kinetic parameters of α-Fe2O3 and Co- α-Fe2O3 photocatalysts.
PFO model
PSO model
qe (mg g−1)
K1 (g mg−1. min−1)
R2
Qe (mg g−1)
qe2
K2 (g mg−1. min−1)
R2
α-Fe2O3
4,79
3,1. 10−4
0,63442
41,3206
1707,3925
3,99. 10−2
0,9998
Co-α-Fe2O3
3,43
2, 16. 10−4
0,4979
42,77
1829,4
8,85. 10−2
0,9999
Kinetic parameters of α-Fe2O3 and Co- α-Fe2O3 photocatalysts.
Adsorption thermodynamics
The thermodynamic parameters, such as the variation in Gibbs free energy (ΔG0, kJ mol−1), variation in enthalpy (ΔH0, kJ mol−1), and variation in entropy (ΔS0, kJ mol−1 K−1), were calculated for Co-α-Fe2O3 adsorption experiments at four different temperatures (25, 35, 45, and 55 °C), using the Eqs. (10), (11), and (12):Where Kd = qe/Ce is the adsorption distribution coefficient or thermodynamic equilibrium constant, R is a constant of gas (8.314 J mol−1 K−1) and T is a temperature (K). Using the Eq. (12), ΔH0 and ΔS0 were calculated from the slop and the intercept of Kd versus 1/T graph. The computed thermodynamics parameters are shown in Table 5. As can be shown, the ΔG0 values were all negative, implying a spontaneous adsorption process, and the adsorption of MB dye on the Co-α-Fe2O3 sample was a physisorption in nature [48, 49]. In addition, as the temperature increased, ΔG0 became more negative, suggesting that the process was spontaneous. Moreover, the adsorption process is generally chemisorption when ΔH0 is between 40 kJ mol−1 and 800 kJ mol−1, and physisorption when ΔH0 is less than 40 kJ mol−1 [50]. In our case, the ΔH0 value was positive and less than 40 kJ mol−1, which indicates that the adsorption of MB dye was physisorption in nature and an endothermic process. On the other hand, the Positive ΔS0 value for MB adsorption showed an increase in randomness at the solid-solution interface, which might be attributable to the electrostatic attraction of the MB adsorbate, replacing the surface hydration shell [49].
Table 5
Thermodynamic data for the adsorption of MB by Co doped hematite photocatalyst.
Sample
T (K)
lnKd
ΔG0 (kJ. Mol−1)
ΔH0 (kJ mol−1)
ΔS0 (kJ. Mol−1 K−1)
Co-α-Fe2O3
298
3.53
-8.75
20.80
0.99
308
3.84
-9.83
318
4.04
-10.69
328
4.31
-11.77
Thermodynamic data for the adsorption of MB by Co doped hematite photocatalyst.
Photocatalytic mechanism
In the photocatalytic reaction, a surface charge-transfer process is widely required [19]. Figure 15 illustrates the proposed mechanism for the MB photodegradation by α-Fe2O3 and Co-α-Fe2O3 photocatalysts. During the irradiation step on α-Fe2O3 and Co-α-Fe2O3 photocatalysts, the excited electrons (e−) jump from valence band VB to conduction band CB, and leaving holes (h+VB) at photocatalyst VB (Eq 13). Photogenerated holes can combine with water molecules H2O adsorbed on the photocatalyst surface to create highly reactive radicals of hydroxyl (OH•) and H+ ions (Eq.14), which have been considered to be the main active species in the photocatalytic mechanism [51]. In addition, the h+VB in the VB can also combine with OH− ions, present in the alkaline medium, to produce (OH•) radicals (eq.15). The photogenerated e− from CB (e−CB) reacts with the dioxygen (O2) dissolved in the dye solution and yields superoxide radical (•O2−) (Eq.16). OH• and •O2− attack MB molecules on or near the surface of photocalysts (Eqs. (17) and (18)).Therefore, in the presence of H2O, the super oxide radicals •O2 released during the irradiation process can react with holes to give OH• radicals and H2O2, or react with H+ ions to form O2 and H2O2 as shown by Eqs. (19) and (20) [16, 52, 53]:
Figure 15
The proposed mechanism for the MB photodegradation by α-Fe2O3 and Co-α-Fe2O3 photocatalysts.
The proposed mechanism for the MB photodegradation by α-Fe2O3 and Co-α-Fe2O3 photocatalysts.Furthermore, unlike α-Fe2O3, Co-α-Fe2O3 has a Co2+ impurity energy level that traps electrons, lowering the electron-hole pair recombination rate [40]. This is the main explanation for the slight improvement in photocatalytic activity of Co-α-Fe2O3 compared to non-doped α-Fe2O3 [25].
Conclusion
In light of this study, α-Fe2O3 and Co doped α-Fe2O3 nanoparticles were successfully synthesised by a green and low-cost chemical route using freshly extracted egg white for the first time. The thermal, structural, vibrational, morphological, and optical properties were analysed by DTA/TG, XRD, FTIR, SEM, EDS and UV-Vis analysis. XRD data of annealed samples (at 550 °C) revealed that the Co doping mainly produces the secondary phase γ- Fe2O3. The lattice parameters and crystallite size were affected by this doping. The EDX analysis reveals the existence of Co and Fe particles in the prepared specimens. UV-visible optical characterization of α-Fe2O3 and Co-α-Fe2O3 nanoparticles revealed direct and indirect band gap energy. The band gap values of Co doped α-Fe2O3 are decreased compared to undoped α-Fe2O3 nanoparticles. The removal efficiency of methylene blue (MB) dye using a photocatalysis process has been studied. The obtained results indicate that the prepared samples have demonstrated high adsorption efficiency. It was also found that doping by Co2+ slightly enhanced the photocatalytic degradation activity of α-Fe2O3 nanoparticles. The photo-adsorption kinetics agreed well with the pseudo-second order model. Thermodynamic study indicates an endothermic and spontaneous process of adsorption.
Declarations
Author contribution statement
Soufiane Hmamouchi: Performed the experiments; Analyzed and interpreted the data.Ahmed El Yacoubi: Analyzed and interpreted the data; Wrote the paper.Brahim Chafik El Idrissi: Conceived and designed the experiments; Analyzed and interpreted the data; Contributed reagents, materials, analysis tools or data; Wrote the paper.
Funding statement
This research did not receive any specific grant from funding agencies in the public, commercial, or not-for-profit sectors.
Data availability statement
Data will be made available on request.
Declaration of interests statement
The authors declare no conflict of interest.
Additional information
No additional information is available for this paper.
Authors: Halina K Dunn; Johann M Feckl; Alexander Müller; Dina Fattakhova-Rohlfing; Samuel G Morehead; Julian Roos; Laurence M Peter; Christina Scheu; Thomas Bein Journal: Phys Chem Chem Phys Date: 2014-11-28 Impact factor: 3.676
Authors: S P Keerthana; R Yuvakkumar; G Ravi; P Kumar; Mohamed Soliman Elshikh; Hussein H Alkhamis; Abdulwahed F Alrefaei; Dhayalan Velauthapillai Journal: Chemosphere Date: 2021-01-02 Impact factor: 7.086
Authors: A A Fauzi; A A Jalil; M Mohamed; S Triwahyono; N W C Jusoh; A F A Rahman; F F A Aziz; N S Hassan; N F Khusnun; H Tanaka Journal: J Environ Manage Date: 2018-08-29 Impact factor: 6.789
Authors: Mohamed Zbair; Kaisu Ainassaari; Asmaa Drif; Satu Ojala; Michael Bottlinger; Minna Pirilä; Riitta L Keiski; Mohammed Bensitel; Rachid Brahmi Journal: Environ Sci Pollut Res Int Date: 2017-11-04 Impact factor: 4.223