The Synthesis of Magnetic Nitrogen-Doped Graphene Oxide Nanocomposite for the Removal of Reactive Orange 12 Dye

Herein, we report the nanofabrication of magnetic calcium ferrite (CaFe2O4) with nitrogen-doped graphene oxide (N-GO) via facile ultrasonication method to produce CaFe2O4/N-GO nanocomposite for the potential removal of reactive orange 12 (RO12) dye from aqueous solution. The successful construction of the nanocomposite was confirmed using different characterization techniques including scanning electron microscopy (SEM), transmission electron microscopy (TEM), Fourier transform-infrared spectroscopy (FT-IR), and X-ray diffraction (XRD). The magnetic properties were studied using vibrating sample magnetometer (VSM) indicating ferromagnetic behavior of the synthesized materials that facilitate their separation using an external magnetic field after adsorption treatment. The addition of N-GO to CaFe2O4 nanoparticles enhanced the BET surface area from 24 to 52.93 m2/g as resulted from the N2 adsorption-desorption isotherm. The adsorption of the synthesized nanomaterials is controlled by several parameters (initial concentration of dye, contact time, adsorbent dosage, and pH), and the RO12 dye removal on the surface of CaFe2O4 nanoparticles and CaFe2O4/N-GO nanocomposite was reached through the chemisorption process as indicated from the kinetic study. The adsorption isotherm study indicated that the adsorption process of RO12 dye was best described through the Langmuir isotherm approving the monolayer adsorption. According to the Langmuir model, the maximum adsorption capacity for RO12 was 250 and 333.33 mg/g for CaFe2O4 nanoparticles and CaFe2O4/N-GO nanocomposite, respectively. The adsorption capacity offered by CaFe2O4/N-GO nanocomposite was higher than reported in the literature for adsorbent materials. Additionally, the regeneration study indicated that CaFe2O4/N-GO nanocomposite is reusable and cost-effective adsorbent. Therefore, the nanofabricated CaFe2O4/N-GO hybrid material is a promising adsorbent for water treatment.


Introduction
Water is essential for human, plant, and animal life alike. From an environmental point of view, the water pollution causes concerns worldwide [1]. The environmental pollution causes about 25.0% of human diseases as stated by the World Health Organization (WHO) [2]. Dye wastewater is responsible for one of the major environmental pollution problems and represents about 20.0% of the industrial wastewater pollution as stated by the World Bank (WB) [2]. Dyes cause harmful effects on the environment and humans due to its carcinogenic, toxic, and mutagenic nature [3]. Various synthetic dyes are used heavily in different industries (textile, pharmaceutical, leather, food, printing, and paper industries) and discharged along with different wastewaters into the natural ecosystem causing the human organs' toxicity [4]. The most serious problem of these dyes is their nonbiodegradable nature due to its complex chemical structure [5] that causes its accumulation inside human body. Serious problems associated to dyes pushed the scientists to find solutions for the treatment of dye wastewater. Various methods including biological treatment, anodic oxidation, oxidation, electrocoagulation, photocatalysis, flocculation/coagulation, adsorption, and membrane filtration were examined and used for the treatment of real textile and dyeing effluents [6][7][8][9][10][11][12][13][14][15][16]. Among the available technologies, adsorption is the most used method due to cost-effectiveness, high efficiency, and easy operation [17]. The adsorption is a procedure based on the transfer of pollutant from aqueous solution to the adsorbent. However, the using of conventional adsorbents faces many problems (insufficient hydrophilic surface, insufficient functional groups, material losses during regeneration, etc.). These problems of conventional adsorbents can be overcome by using nanomaterials with exceptional properties such as the ease synthesis, high surface area, simple functionalization, and low cost [18][19][20]. Dye removal was achieved using several types of materials included carbonaceous materials such as graphene oxide (GO), carbon-nanotube (CNT), and activated carbon [21][22][23] due to its large surface area. Among all carbonaceous materials, GO is the widely used carbon-based nanomaterials for the removal of dyes due to its fluorescence quenching properties, easy surface modification, and good water solubility. Additionally, GO has several oxygencontaining groups such as CO, OH, and COOH that represent about 60.0% of its surface and act as claws for capturing different pollutants. Moreover, hydrophilic oxygenated surface area and hydrophobic pristine graphene that are present in GO increase its surface heterogeneity and enhance its ability to bind different pollutants via hydrophobic interactions, Van der Waals interactions, electrostatic interactions, π-π stacking, and H-bonding [24]. Carbon nanomaterials doping with a heteroatom like N, S, and O could increase its adsorption efficiency besides its surface area [25]. For instance, the adsorption capacity of reduced graphene oxide was folded 1.4 times toward the removal of 2methylanthraquinone and anthracene when doped with Natom as reported by Song et al. [26]. However, the advantages of GO as adsorbents, their separation from the reaction medium is a drawback that obstacles their application in water treatment applications. Interestingly, the presence of magnetic material in the adsorbents can facilitate their separation using an external magnetic field [27,28]. This magnetic separation could reduce the overall cost of the treatment process and allowed the adsorbent reusability for several times. Adsorption of dyes and heavy metal using magnetically separable metal ferrite nanoparticles has been reported in many studies [29][30][31][32] is considered the most biocompatible due to its eco-friendly and nontoxicity nature [33]. In this context, various investigations showed the successful synthesis of magnetically separable crystalline CaFe 2 O 4 nanoparticles and its potential use as an adsorbent for dyes such as reactive orange 12 (RO12) dye [34][35][36][37][38][39]. Therefore, GO can be combined with other nanomaterials such as CaFe 2 O 4 nanoparticles to form nanohybrid material, to remove contaminants from water efficiently.
The purpose of the current research is to investigate the behavior of calcium ferrite/nitrogen-doped graphene oxide (CaFe 2 O 4 /N-GO) nanocomposite in the adsorption of RO12 dye. The produced CaFe 2 O 4 /N-GO nanocomposite using the facile ultrasonication synthesis benefits from the advantages of each nanocomposite part and allowed the enhancement of the nanomaterial adsorption efficiency. The synthesized nanocomposite was well-characterized using familiar techniques and examined for the removal of reactive orange 12 dye (RO12) from water. The effect of different parameters on the removal of dye was explored such as the initial concentration of dye, contact time, adsorbent dosage, and pH. Also, the experimental data were fitted using different models of isotherms and kinetics to wellunderstand the removal process.  Figure 1 illustrated the synthetic route of CaFe 2 O 4 /N-GO nanocomposite.

Materials and Methods
2.5. Material Characterization. The synthesized materials were characterized using various methods. Fouriertransform infrared spectroscopy (FT-IR-6100 Jasco, Tokyo, Japan) was used to carry out FT-IR spectra in the range of 400-4000 cm −1 at room temperature and collected at a resolution of 4 cm −1 . X-ray diffractometer (XRD, X' Pert Pro, PAN analytical, Almelo, The Netherlands) was employed to determine XRD using CuKa radiation (λ = 1:5406 Å) operating at 45 kV. The diffraction intensities were recorded over the 2θ ranging from 5°to 90°with the constant scanning rate of 1°min −1 . A vibrating sample magnetometer (Lake Shore 7410, Lake Shore (Cryotronics Inc., Westerville, OH, USA)) was used to measure the magnetization of the nanocomposite. The morphology and size materials were determined using a scanning electronmicroscope (SEM, Quanta FEG 250, Eindhoven, The Netherlands) and a transmission electron microscope (TEM, JEOL JEM-2100 Plus, Hillsboro, USA), respectively, operated at 200 KV. conditions. All previous adsorption experiments were repeated three times to determine the error. After each experiment, the adsorbent was collected from the reaction medium using an external magnet, and the solution was analyzed for the presence of dye using a UV-vis spectrophotometer at λ max = 416 nm.

Adsorption capacity
The symbols C i , C e , V, and W denote the initial concentration, equilibrium concentration, volume of solution (L), and mass of adsorbent (g), respectively.
where the symbols k 2 , k 1 , q t , q e , K id , and C id denote pseudo 2 nd order rate constant, pseudo 1 st order rate constant, adsorption capacity (mg/g) at t time, adsorption capacity at equilibrium (mg/g), intraparticle diffusion rate constant, and intraparticle diffusion constant, respectively. The Langmuir and Freundlich adsorption isotherms models were used to study the adsorption mechanism. The Freundlich and Langmuir models can be represented by eq. (6) and eq. (7), respectively.
where q m and C e denote maximum adsorption capacity (mg/g) and equilibrium concentration, respectively, while n and K F denote the Freundlich constants. The reusability of CaFe 2 O 4 /N-GO nanocomposite for the removal of RO12 dye was investigated up to six successive cycles using 0.1 M of HCl as eluent at the optimum conditions. After each cycle, the adsorbent was collected using magnet and washed several times with HCl and H 2 O then dried in oven at 60.0°C for the next cycle.  [34]. For the N-GO spectrum, the characteristic bands of GO are present such as the peaks at 1114 cm -1 and 3410 cm -1 that represent C-OH stretching vibration and O-H stretching vibrations, respectively [41,42]. While the peak at 1315 cm -1 represented the C=N stretching vibrations, the peak at 1406 cm -1 represented the C-N stretching vibrations, and these two peaks are evidence for nitrogen doping [42,43]. The FT-IR spectrum of the nanocomposite showed the appearance of new absorption bands due to the C-O, C-N, and C=N bonds that appeared at 1086.7, 1164.6, and 1367.5 cm -1 , respectively, and approved the doping of N atom in the GO sheets. Also, the addition of N-GO sheets caused the shift of the O-H stretching band. The disappearance of the band corresponding to Fe-OH could result from the breaking of the OH bond due to the interaction between the COOH group in the nanosheets and Fe-OH. Additionally, the interaction between the nanosheets and ferrite nanoparticles could be confirmed by the shift of the Fe-O band from 712.2 to 693 cm -1 . The existence of spinel ferrite in the CaFe 2 O 4 /N-GO nanocomposite was confirmed by the appearance of bands at 551.7 and 644.7 cm -1 that represent the vibrations of the Fe-O bond. Also, the N-H bending vibration and O-H stretching vibration are represented by the bands that appeared at 1550.2 and 3435 cm -1 , respectively [44]. The FT-IR spectra of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite indicated the well construction of the nanocomposite [34,44].

Results and Discussion
For the determination of crystal structure and phase purity of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, the XRD was investigated (Figure 2(b)). According to Figure 2(b), XRD of CaFe 2 O 4 nanoparticles showed the presence of (401), (311), (320), (230), and (220) planes represented by the peaks at 54.53, 43.66, 34.90, 30.17, and 29.57°, respectively, indicating the face-centered cubic lattice [45]. For XRD of N-GO, the strong diffraction peak at 2θ = 10:2°can be attributed to the characteristic plane of GO. The XRD of the nanocomposite showed the appearance of the same peaks of CaFe 2 O 4 nanoparticles with the appearance of an additional peak at 10.0°, which is resulted due to the addition of N-GO nanosheets. To study the particle morphology, TEM analysis was performed for the synthe- To study the thermal properties of the synthesized materials CaFe 2 O 4 nanoparticles, N-GO, and CaFe 2 O 4 /N-GO nanocomposite, the thermogravimetric analysis (TGA) was used as shown in Figure 4(b). For CaFe 2 O 4 nanoparticles, N-GO, and CaFe 2 O 4 /N-GO nanocomposite, the slight weight loss that occurred below 100°C was attributed to the evaporation of physically adsorbed water molecules. For N-GO, the weight loss at temperature between 120 and 220°C was attributed to the decomposition of different functional groups while at higher temperature; the weight loss was attributed to the decomposition of carbon skeleton. For CaFe 2 O 4 nanoparticles, the TGA curve indicates their thermal stability with no notable weight loss with  nanoparticles and CaFe 2 O 4 /N-GO nanocomposite to determine their surface properties as shown in Figure 5. According to Figure 5, the synthesized materials have mesoporous structure as they have type IV isotherm of H3 type hysteresis loop. The CaFe 2 O 4 nanoparticles showed BET surface area of 24.0 m 2 g -1 . After the addition of N-GO nanosheets, this area was increased to 52.93 m 2 g -1 . The addition of nanosheets caused the well distribution of magnetic nanoparticles and prevented their agglomeration by magnetic attraction. This well distribution of nanoparticles was the reason for  7 Adsorption Science & Technology higher CaFe 2 O 4 /N-GO nanocomposite' BET surface area than CaFe 2 O 4 nanoparticles. Also, the higher surface area of CaFe 2 O 4 /N-GO nanocomposite suggested the higher mesoporosity than CaFe 2 O 4 nanoparticles. The determined surface area, pore volume, and pore diameter of synthesized materials using BET study were introduced in Table 1. CaFe 2 O 4 /N-GO nanocomposite showed a higher pore volume than CaFe 2 O 4 nanoparticles that reflected the higher surface area of the nanocomposite. Also, the higher surface area of the nanocomposite was indicated from the micropore volume values. This large micropore volume and BET surface area play a significant role in the removal of pollutants from aqueous solution as described in the literature [9, 10, 46].

Optimization of the Adsorption Conditions.
The adsorption process is controlled by several parameters such as initial concentration of dye, contact time, adsorbent dosage, and pH, which are the basis of all laboratory experiments laboratories aiming to determine optimum conditions to get the highest efficiency of the adsorbent. Subsequently, the next section includes the study of the effect of different parameters on RO12 removal on the surface of the synthesized nanomaterials. To study the effect of the adsorbent dosage on RO12 removal, different dosages ranging from 0.125 to 1 g/L were investigated for the removal of RO12 dye as shown in Figure 6(a). According to Figure 5(a), the removal efficiency of RO12 dye was increased from 25:0% ± 0:5 to 93:26% ± 0:38 and from 40:56% ± 0:42 to 96:77% ± 0:63 for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, respectively, when the dosage increased from 0.125 to 1 g/L. This increase of removal efficiency associated with the increase of adsorbent dosage is attributed to the presence of more available adsorption sites by increasing the dosage. While at adsorbent dosage higher than 1 g/L, there was no significance increase of RO12 removal efficiency on the surface of CaFe 2 O 4 nanoparticles or CaFe 2 O 4 /N-GO nanocomposite, which is attributed to the achievement of the saturation state and the agglomeration of the adsorbent particles and the blockage of adsorption sites [47]. The removal efficiency of dye on the surface of CaFe 2 O 4 /N-GO nanocomposite was higher than on the surface of CaFe 2 O 4 nanoparticles due to the presence of N-GO nanosheets providing more active sites and N-atoms for the chelation of dye molecules.
The effect of pH on the removal of RO12 dye using CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite was studied by varying the initial pH within the range of 2.0 to 7.0 as shown in Figure 6(b). According to Figure 6(b), the pH increase caused a decrease in the removal efficiency of RO12 until reaching the lowest value at pH of 7.0, which is equal to 20:28% ± 0:36 and 32:56% ± 0:54 for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, respectively. The highest removal efficiency was achieved at a pH of 2.0, which is considered the optimum pH value for dye removal. This behavior could be interpreted as at low pH value, and the adsorbent surface was protonated to form positively charged functional groups that act as chelation sites to uptake the anionic RO12 dye via electrostatic interaction. While at higher pH values, the functional groups of adsorbent become negatively charged and repulsed with the anionic dye causing the decrease in the removal efficiency. Moreover, at high pH value, the presence of OHgroups could compete with the anionic dye for the active sites on the adsorbent surface which affect the removal efficiency negatively [48,49]. As reported in the literature, pH affects the degree of ionization of the adsorptive molecules, the surface charge, and the dissociation degree of the functional groups of the adsorbent active site [50][51][52]. Therefore, the results of pH effect indicated that the pH is a key factor for dye adsorption. Moreover, the determination of point of zero charge (pH PZC ) for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite is important to determine the pH effect on the adsorption process. Subsequently, the pH PZC was determined for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite as shown in Figure 6(c). The pH PZC values were found to equal 5.21 and 5.33 for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, respectively. This means that below the pH PZC , the adsorbent is positively charged while above the pH PZC , and the adsorbent is negatively charged. The pH PZC determination interprets the high removal efficiency of RO12 dye at low pH values. At low pH value < pH PZC , the adsorbent surface was positively charged and attracted the anionic dye via the electrostatic attractions. While at higher pH value > pH PZC , the adsorbent surface was negatively charged and repulsed the anionic dye. So, the determination of pH PZC values enhances the results of pH effect on the adsorption process. The effect of the contact time on dye removal by CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite was studied at different intervals ranging from 10.0 to 120 minutes as shown in Figure 6(d). According to Figure 6(c), the dye removal rate increased with an increase in contact time. At the beginning, a rapid removal was observed, which is attributed to the availability of protonated adsorbent sites to interact with anionic dye through the electrostatic interaction. Then, there was a decrease in the removal rate until reached the equilibrium that is attributed to the reduced surface area of the adsorbent due to the adsorbed dye, and also the adsorbed molecules are repulsed with each other [53]. The optimum contact time for the adsorption of RO12 dye on the surface of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite was 80.0 minutes at which the equilibrium was reached as clearly shown in Figure 6(d). To study the effect of the initial dye concentration on the removal of RO12 using CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, the initial concentration was varied from 20 to 150 mg/L as shown in Figure 6(e). According to Figure 6(e), the removal efficiency of dye was decreased by increasing the dye concentration gradually until 80 mg/L, at which there was a drop in the removal efficiency. This behavior was attributed to the increased amount of dye mol-ecules against the fixed number of adsorption sites, causing the drop in the removal efficiency. However, at low dye concentration, several free adsorption sites are available to uptake the dye. To study the effect of ionic strength on the removal of RO12 dye on the surface of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, the removal efficiency was determined at different concentrations of KNO 3 salt as shown in Figure 6(f). According to Figure 6(f), the removal efficiency was decreased by increasing the ionic strength until reaching 45% and 48% for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, respectively, at ionic strength of 2.2 mol.L -1 . This behavior was expected in the presence of KNO 3 that supports the ion exchange mechanism of the adsorption process [51]. This means that the counterions around the adsorption sites weaken the attraction forces between adsorbent and adsorbate and cause a decrease in the removal efficiency [51].

Adsorption Kinetics and Isotherm.
The adsorption process is perfectly imaged through the study of the adsorption rate [54,55]. The adsorption rate is an important parameter that can be described using different kinetic models such as pseudo 1 st order model and pseudo 2 nd order model. Subsequently, the experimental data for the removal of RO12 dye  Figure 6. The kinetic parameters were calculated and presented in Table 2. From the results in Table 2, the R 2 values showed that pseudo 2 nd order model is higher fitting the experimental data than pseudo 1 st order model in case of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite. Additionally, the experimental values of q e indicated the agreement with pseudo 2 nd order. Also, Figure 7 indicates the excellent agreement with pseudo 2 nd order model to the experimental adsorption data. This agreement of adsorption data with the pseudo 2 nd order model indicates that the removal of RO12 dye achieved through the chemisorption between the dye and CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite [56,57].
This kinetic behavior is similar to many previously reported studies for the removal of RO12 dye [37,58]. To get an idea about the diffusion mechanism, the Webber's pore-diffusion model (intraparticle diffusion model) was used as shown in Figure 7(c). According to Figure 7(c), the plot of intraparticle diffusion model between t 0:5 and q t showed the existence of three different stages suggesting three different mechanisms of adsorption. The 1 st stage represents the diffusion of RO12 dye on the surface of adsorbents (CaFe 2 O 4 and CaFe 2 O 4 /N-GO) from the bulk solution, the 2 nd stage represents the pore diffusion, and the 3 rd stage represents the achievement of equilibrium state [18,59].
More insights about the adsorption process can be obtained from the study of the adsorption isotherm as the isotherm can describe the distribution of toxic ions at an equilibrium state between the solid-liquid phases [60]. Also, the isotherm study can be used for the determination of adsorption capacity as well as understanding the affinities between adsorbent and adsorbate ions. Therefore, in this study, the adsorption behavior was described using the adsorption isotherm models including Langmuir model and Freundlich model. Langmuir model suggests that the adsorbate molecules not interacted with each other and result a monolayer adsorption of the adsorbate on the homogeneous surface of adsorbent [61]. While the Langmuir model suggests multilayer adsorption process resulted from the adsorption of adsorbate molecules on the heterogeneous surface of adsorbent [62]. The linear plots of Langmuir and Freundlich isotherm models are shown in Figure 8, and the calculated parameters are presented in Table 2. According to the results in Table 1   According to Langmuir fitting results, the maximum adsorption capacities (q m ) are 250 mg/g and 333.33 mg/g for CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite, respectively. The enhancement of the adsorption capacity of CaFe 2 O 4 /N-GO nanocomposite can be attributed to the increased active sites associated with the addition of N-GO sheets to the magnetic CaFe 2 O 4 nanoparticles. As a result, N-GO sheets provide more quantities of functional groups to the adsorbent causing an increase in the capacity of the adsorbent. Moreover, the N-GO sheets provide 3-D porous skeleton that can uptake the adsorbate molecules inside and, hence, increase the adsorption capacity. Additionally, the doping of N atoms in GO provides the amine groups allowing the enhancement of the pollutants uptake via hydrogen bonding and electrostatic interaction. All these factors play a significant role in the enhanced adsorption process of RO12 dye on the surface of CaFe 2 O 4 /N-GO nanocomposite.
To get an insight about the removal mechanism of RO12 dye on the surface of CaFe 2 O 4 /N-GO nanocomposite, the FT-IR spectra of the nanocomposite were studied before and after the dye adsorption as shown in Figure 9. According to Figure 9, the FT-IR spectrum of CaFe 2 O 4 /N-GO nanocomposite showed many differences after the adsorption of RO12 dye. The band at 3435 cm -1 that correspond to OH group stretching vibrations was shifted, and its intensity was decreased indicating the contribution of OH groups in the removal mechanism. Similarly, the bands of other functional groups were shifted as a result of their contribution in the dye removal. Also, the appearance of the new bands at 1550 cm -1 and 1210 cm -1 was attributed to the azo-bond (N=N) vibrations, and sulfonate group of the dye, respectively, indicated the successful adsorption of the dye on the surface of nanocomposite.
To highlight the effectiveness of the synthesized CaFe 2 O 4 /N-GO nanocomposite as an RO 12 adsorbent, the maximum adsorption capacity obtained here for RO 12 was compared with previously reported results (Table 3). According to previously reported results, CaFe 2 O 4 /N-GO nanocomposite revealed excellent adsorption capacity for RO12 compared to the reported adsorbents. Therefore, it could be concluded that the designed magnetic CaFe 2 O 4 / N-GO nanocomposite will be a promising hopeful hybrid nanomaterial useful as adsorbent for the elimination of dyes from wastewater.
3.3. Reusability Study. The important advantage of any adsorbent is its reusability which could reduce the process cost and enhance its application at large-scale [63][64][65]. The reusability of the synthesized CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposites was determined by repeating the adsorption-desorption cycles up to 5 cycles. The adsorbents were allowed to adsorb the RO12 dye. Then, the adsorbents were collected using an external magnet, and the solution was examined for the presence of dye. The adsorbed dye molecules were desorbed by immersing the adsorbents in 0.1 M NaOH for half-hour. After that, the adsorbents were washed using 0.1 M HCl to be used in the next cycle. The reusability results for the removal of RO12 dye using CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposite are shown in Figure 10. The removal efficiency of CaFe 2 O 4 nanoparticles and CaFe 2 O 4 /N-GO nanocomposites remained above 80% ± 1 (after 3 rd cycle) and 90% ± 1 (after 5 th cycle), respectively.
Subsequently, both synthesized adsorbents are excellent choices for water treatment. But, the CaFe 2 O 4 /N-GO nanocomposite is better than CaFe 2 O 4 nanoparticles and more efficient due to the higher adsorption capacity and higher reusability results. All results indicated that the CaFe 2 O 4 / N-GO nanocomposite is a promising nanosorbent for the

Conclusion
The facile ultrasonication method was used for the successful synthesis of magnetic CaFe 2 O 4 /N-GO nanocomposite. The synthesized materials were characterized using different methods including FT-IR, XRD, SEM, TEM, magnetization curve, and N 2 adsorption-desorption isotherm. The synthesized magnetic CaFe 2 O 4 /N-GO nanocomposite was examined for the adsorption of RO12 dye and compared with CaFe 2 O 4 nanoparticles. In order to optimize the adsorption process, the effects of different factors including the initial dye concentration, pH, contact time, and adsorbent dose on the adsorption process were studied. The adsorption kinetics that was studied indicated that the pseudo 2 nd order model was the best for the description of RO12 uptake on the surface of CaFe 2 O 4 /N-GO nanocomposite and CaFe 2 O 4 nanoparticles. Langmuir and Freundlich isotherm models were used to study the adsorption isotherm, and the best fitting was achieved using Langmuir isotherm model. The addition of N-GO to CaFe 2 O 4 nanoparticles during the nanofabrication of the nanocomposite enhanced the RO12 removal efficiency. The maximum adsorption capacity (q m ) of CaFe 2 O 4 /N-GO nanocomposite for RO12 dye was 333.33 mg/g which was greater than that of CaFe 2 O 4 nanoparticles (250 mg/g). The higher adsorption capacity of CaFe 2 O 4 /N-GO nanocomposite was related to the addition of N-GO which increased the nanosorbent surface area and provided the nitrogen centers for capturing more toxic molecules. Interestingly, CaFe 2 O 4 /N-GO nanocomposite showed excellent adsorption capacity for RO12 compared to other adsorbents reported in the literature. Moreover, the reusability of the synthesized nanomaterials was studied up to 5 cycles with excellent results. Finally, it could be concluded that the nanofabricated CaFe 2 O 4 /N-GO will be a cost-effective and promising adsorbent for the elimination of RO12 from wastewater.

Data Availability
The research data used to support the findings of this study are included within the article.

Conflicts of Interest
The authors declare that they have no conflicts of interest.