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Open Access Research Article

Effect of calcination temperature on the performance of hydrothermally grown cerium dioxide (CeO2) nanorods for the removal of Congo red dyes

1,2 * ORCID , 1 , 3 ORCID , 1 ORCID , 3 ORCID , 2,4 * ORCID

Vol. 1 No. 1 |pp. 9–14 |Received Jan 30, 2024 |Revised Feb 18, 2024 |Accepted Feb 20, 2024

Copyright © 2026 The Authors. This publication is licensed under CC BY 4.0 .

Abstract

This study investigates the transformation of CeO2 nanostructures through various calcination temperatures and their subsequent impact on morphological, structural, and photocatalytic properties. X-ray diffraction (XRD) analysis reveals the presence of cerium oxycarbonate in the uncalcined samples, transitioning to a face-centered cubic CeO2 phase post-calcination at 500 °C. The scanning electron microscopy (SEM) imaging delineates a morphological evolution from distinct, rod-like structures in the uncalcined state to sintered, agglomerated forms as calcination temperatures ascend from 500 °C to 800 °C. The crystallite size, calculated using Scherrer's Equation, displayed a proportional increase with temperature. The photocatalytic degradation of Congo red dye under UV light was analyzed using UV-Vis spectroscopy, with the calcined samples exhibiting varying degrees of adsorption and photocatalytic activity. The study found that higher calcination temperatures correlate with increased photocatalytic performance, potentially due to enhanced crystallinity. This assertion is supported by pseudo-first-order kinetic modeling, indicating improved photocatalytic efficiency with higher calcination temperatures, underlined by increasing rate constants. These findings underscore the intricate relationship between calcination-induced morphological and structural changes and the photocatalytic prowess of CeO2 nanostructures.

Keywords:
Rare-earth Metal Oxide Adsorption Degradation Wastewater Treatment Cerium Oxide

INTRODUCTION

Photocatalytic degradation has emerged as a compelling method to tackle the issue of dye pollution in wastewater treatment, due to its potential for complete mineralization of organic pollutants into non-toxic byproducts 1,2,3. Several semiconductors, such as \mathrm{ZnO}ZnO, \mathrm{TiO_{2}}TiO2, \mathrm{SnO_{2}}SnO2, \mathrm{MnO_{2}}MnO2, \mathrm{Fe_{2}O_{3}}Fe2O3, \mathrm{NiO}NiO, \mathrm{WO_{3}}WO3, \mathrm{Nb_{2}O_{5}}Nb2O5, and \mathrm{CeO_{2}}CeO2, have been developed as effective photocatalytic materials 4,5,6,7,8. Cerium dioxide (\mathrm{CeO_{2}}CeO2), in particular, has garnered increasing attention in the field of environmental engineering for its remarkable redox properties, high oxygen storage capacity, and stability 9,10. These attributes render it an indispensable material for applications in catalysis, fuel cells, and as an additive in diesel fuels to reduce emissions 11. Recent advancements in nanotechnology have further enhanced the utility of \mathrm{CeO_{2}}CeO2, especially in nanostructured forms, which exhibit unique properties attributable to their high surface-to-volume ratio and quantum size effects 12. These nanostructures are typically synthesized using various methods, with the hydrothermal process being one of the most favored due to its relatively mild conditions, scalability, and the quality of the resultant products 13,14. The resultant morphologies, including rod-like structures, are often determined by the synthetic conditions and can be fine-tuned to optimize the material’s performance for specific applications.

Figure 1. The XRD pattern of (a) calcined (\mathrm{CeO_{2}}CeO2-500) vs uncalcined \mathrm{CeO_{2}}CeO2 and (b) \mathrm{CeO_{2}}CeO2 calcined at different temperature. (c) The \mathrm{CeO_{2}}CeO2 crystallite size calculated from XRD patterns. (d) BET analysis of the \mathrm{CeO_{2}}CeO2-500 samples.

Our previous study highlighted the potential application of \mathrm{CeO_{2}}CeO2 nanorods, fabricated using the hydrothermal process, as photocatalysts in dye degradation 15. However, their performance needs enhancement to produce high-performance photocatalytic materials. Literature suggests that increasing the calcination temperature leads to materials with better photocatalytic performance 16. The calcination process plays a pivotal role in tailoring the properties of metal oxide nanostructures. It is known to induce morphological changes, enhance crystallinity, and remove organic residues or other volatile contaminants 17,18. These alterations are crucial as they directly influence the material’s catalytic activity, adsorptive capacities, and overall chemical reactivity. Calcination temperature is a critical parameter; it can dictate the phase stability and surface characteristics of the resulting \mathrm{CeO_{2}}CeO2. While lower temperatures may be sufficient to induce phase changes from precursors such as cerium oxycarbonate to pure \mathrm{CeO_{2}}CeO2, higher temperatures may lead to sintering, growth of crystallite size, and potentially the formation of secondary phases. This study aims to understand the relationship between calcination conditions and the characteristics of the resulting \mathrm{CeO_{2}}CeO2 nanostructures, which is essential for optimizing their performance in environmental applications.

Figure 2. The SEM images of the (a) uncalcined \mathrm{CeO_{2}}CeO2, and calcined \mathrm{CeO_{2}}CeO2 (b) \mathrm{CeO_{2}}CeO2-500, (d) \mathrm{CeO_{2}}CeO2-600, (e) \mathrm{CeO_{2}}CeO2-700, and (f) \mathrm{CeO_{2}}CeO2-800 samples

EXPERIMENTAL SECTION

Materials

Cerium nitrate hexahydrate (\mathrm{Ce(NO_{3})3.6H_{2}O}Ce(NO3)3.6H2O), urea (\mathrm{CO(NH_{2})2}CO(NH2)2), and Congo red (CR, C.I. 22120) were purchased from Merck, Darmstadt, Germany. The deionized (DI) water was used as solvent both during the hydrothermal and dye degradation measurements. All materials were used as received without any further purifications.

Preparation of \mathrm{CeO_{2}}CeO2 nanostructures and materials characterizations

The \mathrm{CeO_{2}}CeO2 nanorods were fabricated similar to our previously reported study 15. Typically, 3.0 g of \mathrm{Ce(NO_{3})3}Ce(NO3)3 and 4.2 g of \mathrm{CO(NH_{2})2}CO(NH2)2 were dissolved in 70 mL deionized water using a magnetic stirrer until the salt completely dissolved. The mixed solution was then placed inside a 100-mL Teflon-lined autoclave and sealed tightly for the hydrothermal process. The hydrothermal growth took place at a temperature of 100 ^\circC for 12 hours inside an electric oven. The solid was then washed with DI water and filtered several times using a vacuum filter. The solid powder was dried in an electric oven at 80 ^\circC for 4 hours before calcination. To investigate the effect of calcination temperature on the dye removal performance, the calcination temperatures were varied (i.e., 500, 600, 700, and 800 ^\circC) and the samples were named \mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800, respectively. Each sample was calcined using a predetermined holding temperature and held for 2 hours, with a ramp of 5 ^\circC/min. A yellowish powder was obtained for each calcination temperature and used for materials characterization and dye removal investigations. To investigate the effect of the calcination temperature on the \mathrm{CeO_{2}}CeO2 morphology and crystalline structure, scanning electron microscopy (SEM, JEOL JSM-6510) and X-ray diffractometry (XRD, BRUKER D8 ADVANCE ECO) were used respectively.

Photocatalytic dye degradation measurements

For the photodegradation investigation, we used a photoreactor chamber equipped with four Phillips UVC lamps (10 W, \lambda \approx 253.7λ253.7 nm). Congo red (CR) aqueous solution was prepared with a concentration of 10 ppm as the model dye. Typically, 50 mg of \mathrm{CeO_{2}}CeO2 powder was put into 100 mL CR solutions (10 ppm) and stirred inside the photoreactor chamber. The reaction was initially taken place under dark conditions for 30 min to achieve stable adsorption conditions. After that, the UV lamp was then turned on, and the CR solution was subjected to UV irradiations. Every 20 min, 3.5 mL suspension was taken and filtered using polyvinylidene fluoride (PVDF) syringe filters to separate the \mathrm{CeO_{2}}CeO2 powder. The absorption spectra of 3.5 mL of each time variation were then measured by a UV-Vis spectrophotometer (Shimadzu UV-1280). The measurement was done for all samples (\mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800). The concentration of the CR solutions was determined using the absorbance value at the maximum wavelength (\lambda = 498λ=498 nm).

RESULTS AND DISCUSSION

Figure 1 shows the XRD pattern of the uncalcined and calcined \mathrm{CeO_{2}}CeO2 samples. The uncalcined \mathrm{CeO_{2}}CeO2 samples show characteristics of cerium oxycarbonate (\mathrm{Ce_{2}(CO_{3})2O.H_{2}O}Ce2(CO3)2O.H2O) in accordance with the PDF number 44-0617 (Figure 1a), which is similar to previous literatures 19. This phase is a well-known oxycarbonate of cerium that is mostly obtained through precipitation of cerium salt through hydrolysis of urea 20. After calcination (\mathrm{CeO_{2}}CeO2-500), a new crystal phase was obtained, which has excellent similarity with the XRD pattern of face-centered cubic (FCC) \mathrm{CeO_{2}}CeO2 (PDF#43-1002) 21,22. Previous studies found that the organic residues obtained during the hydrothermal process of \mathrm{CeO_{2}}CeO2 start to decompose at a temperature of 320 ^\circC 40,23. Based on that information, we believed that a calcination temperature of 500 ^\circC is sufficient to convert cerium oxycarbonate into face-centered cubic \mathrm{CeO_{2}}CeO224. The peaks were observed at 2\thetaθ values of 28.5^\circ; 33.1^\circ; 47.5^\circ; 56.3^\circ; 59.1^\circ; 69.4^\circ; 76.7^\circ; 79.1^\circ; and 88.4^\circ, which correspond to the (hkl) planes of (111), (200), (220), (311), (222), (400), (331), (420), and (422), respectively.

Figure 3. The UV-Vis spectra of the Congo red (CR) dyes with increasing reaction times are shown for (a) \mathrm{CeO_{2}}CeO2-500, (b) \mathrm{CeO_{2}}CeO2-600, (c) \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800 samples. Panel (e) presents photograph images of the discoloration of CR solutions after increasing contact time with \mathrm{CeO_{2}}CeO2-500 and \mathrm{CeO_{2}}CeO2-800. Panel (f) illustrates the changes in CR peak intensity at \lambdaλ of 498 nm. The (g) C/C_0C/C0 and (h) \ln(C_0/C)ln(C0/C) vs. reaction time are also depicted.

The influence of various calcination temperatures on the crystalline phase of \mathrm{CeO_{2}}CeO2 is depicted in Figure 1b. Characteristic peaks of face-centered cubic (FCC) \mathrm{CeO_{2}}CeO2 were observed for all samples, without the presence of additional or secondary cerium phases, confirming the successful fabrication of \mathrm{CeO_{2}}CeO2 increased with the calcination temperature. Figure 1c presents the crystallite sizes of the \mathrm{CeO_{2}}CeO2 increased with the calcination temperature. Figure [FIGREF:1]c presents the crystallite sizes of the \mathrm{CeO_{2}}CeO2 samples at different calcination temperatures, calculated from the XRD data using Scherrer’s Equation 25,26. The crystallite size was calculated to be 7.2 nm, 8.6 nm, 13.4 nm, and 19.4 nm for the \mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800, respectively. The crystallite size increases with increasing calcination temperature. These findings are consistent with previously reported studies 27) adsorption-desorption isotherm using surface area analyzer (Quantachrome QuadraWin ©2000-16). The quantity adsorbed during adsorption/desorption process with various relative pressure were shown in Figure 1d. It shows type IV hysteresis loop revealing the existence of mesopore similar to previous literatures 28. We also performed the nitrogen (\mathrm{N_{2}}N2) adsorption-desorption isotherm using surface area analyzer (Quantachrome QuadraWin ©2000-16). The quantity adsorbed during adsorption/desorption process with various relative pressure were shown in Figure [FIGREF:1]d. It shows type IV hysteresis loop revealing the existence of mesopore similar to previous literatures 29,30,31 . Moreover, the BET (Brunauer, Emmett and Teller) surface area (SBET) of the CeO2-500 shows a remarkable value of 105.04 m^2m2/g, implying that the material has high surface area.

Figure 2 showcases the SEM images of (a,b) uncalcined \mathrm{CeO_{2}}CeO2, and calcined \mathrm{CeO_{2}}CeO2 at (c) \mathrm{CeO_{2}}CeO2-500, (d) \mathrm{CeO_{2}}CeO2-600, (e) \mathrm{CeO_{2}}CeO2-700, and (f) \mathrm{CeO_{2}}CeO2-800. The morphological effects of calcination temperature on \mathrm{CeO_{2}}CeO2 nanostructures were also investigated using the SEM images featured in Figure 2 sample without calcination treatment (Figure 2a and 2b) show that the \mathrm{CeO_{2}}CeO2 sample without calcination treatment (Figure [FIGREF:2]a and [FIGREF:2]b) show that the \mathrm{CeO_{2}}CeO2 has formed into elongated, rod-like structures with a relatively uniform size and orientation, indicative of the typical morphology of \mathrm{CeO_{2}}CeO2 fabricated via the hydrothermal process 15-500 (Figure 2c) also shows a relatively uniform rod-like structure. However, as the calcination temperature were increasing for 32-800 samples in which shown in Figure 2d to 2f a more distinctive different were observed. Upon calcination, the \mathrm{CeO_{2}}CeO2 sample after calcinations. For example, the \mathrm{CeO_{2}}CeO2-500 (Figure [FIGREF:2]c) also shows a relatively uniform rod-like structure. However, as the calcination temperature were increasing for \mathrm{CeO_{2}}CeO2-600 to \mathrm{CeO_{2}}CeO2-800 samples in which shown in Figure [FIGREF:2]d to [FIGREF:2]f a more distinctive different were observed. Upon calcination, the \mathrm{CeO_{2}}CeO2 samples exhibit a distinct morphological evolution from well-defined, rod-like structures to increasingly sintered and agglomerated forms. Initially, the uncalcined \mathrm{CeO_{2}}CeO2 displays discrete and uniform rods, indicative of a lower temperature synthesis with minimal particle fusion. As the calcination temperature rises, these rods gradually lose their distinctness; they broaden, fuse, and exhibit smoother edges - a transformation signifying increased diffusion and coalescence of particles 33. At the highest temperatures observed, the rods become almost indistinguishable, with significant agglomeration leading to a bulkier and denser morphology.

Figures 3a to 3d present the UV-Vis spectroscopy spectra of Congo red (CR) solutions with varying contact times for all calcined \mathrm{CeO_{2}}CeO2 samples. The CR solutions exhibit maximum absorption at a wavelength of 498 nm, with peak intensities decreasing as contact time increases, indicating a reduction in CR concentration. This trend is consistent across all samples, demonstrating a clear discoloration of the dye upon reaction or contact, which is visually confirmed (Figure 3e). Initially red, the CR solutions progressively lighten upon extended contact with the calcined \mathrm{CeO_{2}}CeO2. This also agrees with the UV-Vis spectroscopy investigation previously.

Figure 3f elucidates the concentration changes of the CR solutions over increasing contact times, assessed by the intensity at the peak wavelength of 498 nm. In the absence of light, the CR concentration diminishes to varying extents across the samples, with decreases of over 44%, 46%, 37%, and 32% after 30 minutes of dark contact for \mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800, respectively. This behavior is attributed to the adsorptive capabilities of \mathrm{CeO_{2}}CeO2, as documented in previous literature 34,35. Previous studies state that with rising calcination temperatures, which typically reduce the surface area of the materials, the contribution of adsorption decreases 36,37.

Under UV irradiation, the CR concentration further declines for all samples, showcasing their photocatalytic activity. The CR degradation rate (C/C_0C/C0), defined as the ratio of the initial CR concentration (C_0C0) to the concentration after a certain contact time (CC), was calculated to evaluate the photocatalytic behavior of \mathrm{CeO_{2}}CeO2 at different calcination temperatures (Figure 3f). The results reveal an accelerated CR concentration reduction for \mathrm{CeO_{2}}CeO2-800 compared to the other samples. Specifically, after 120 minutes of UV irradiation, the CR concentration decreased by approximately 39%, 50%, 47%, and 54% for \mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800, respectively. This increase in photocatalytic performance with higher calcination temperatures is likely due to the enhanced crystallinity of the materials, as indicated by the XRD results 38,39.

Photocatalytic pseudo-first-order kinetic modeling was employed to further understand the CR degradation by the calcined \mathrm{CeO_{2}}CeO2, based on Equation (1):

where \mathrm{C_{0}}C0, (CC), (kk), and (tt) are the CR initial concentration (ppm), CR solution concentration at given time (ppm), the pseudo-first-order constant (min^-1min1), and the contact time (min), respectively. The kinetic modeling, displayed in Figure 3g, exhibits a linear correlation with high fitting parameters (R^2R2 values) of 0.96832, 0.98445, 0.97148, and 0.98586 for \mathrm{CeO_{2}}CeO2-500, \mathrm{CeO_{2}}CeO2-600, \mathrm{CeO_{2}}CeO2-700, and \mathrm{CeO_{2}}CeO2-800, respectively. Furthermore, the rate constant k shows an increase with the calcination temperature of the \mathrm{CeO_{2}}CeO2, implying an enhanced photocatalytic performance.

CONCLUSION

In this study, \mathrm{CeO_{2}}CeO2 nanostructures were successfully fabricated through a hydrothermal process followed by subsequent calcination at varying temperatures. SEM imaging revealed that all samples maintained a rod-like structure, with crystallite sizes increasing alongside the calcination temperatures. This pattern sharpening and narrowing with elevated temperatures indicate enhanced crystallization and an increase in the size of the \mathrm{CeO_{2}}CeO2 particles. The photocatalytic capabilities of the calcined \mathrm{CeO_{2}}CeO2 were assessed through the degradation of Congo red (CR) dye, demonstrating promising potential for wastewater treatment applications. The reduction in CR concentration can be attributed to a combination of adsorption and photocatalytic degradation mechanisms. However, it was observed that higher calcination temperatures somewhat diminish adsorption performance, likely due to alterations in surface charges and a decrease in material surface area. Conversely, the same increase in calcination temperatures correlated with improved photocatalytic activity, which can be ascribed to the higher crystallinity of the materials. These findings highlight the dual role of calcination temperature in modulating both the physical characteristics and functional properties of \mathrm{CeO_{2}}CeO2 nanostructures. Thus, the optimal calcination temperature for \mathrm{CeO_{2}}CeO2 nanostructures must balance these effects to maximize their efficacy in environmental applications, particularly in the domain of pollutant degradation in water treatment scenarios.

Acknowledgments

This study receives no funding.

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